Document 0qDqXXVdBVazQXVoe8mNX2BDR

ABD00048708 Compliance Testing for Particulate Emissions Multiple Sources Georgia Gulf Chemicals and Vinyls, LLC Aberdeen, Mississippi June 14, 2000 - June 30, 2000 ______________________ ENTEC Project No.: 20148_________________________ ENTEC Emission Testing Services ABD00048709 Entec Services, Inc. 25 Commerce Avenue - Suite 104 Hueytown, Alabama 35023 Telephone: (205)491-6676 Fax: (205)491-6614 Results of the June 14, 2000 - June 30, 2000 Particulate Emissions Compliance Test on Multiple Sources at the Georgia Gulf Chemicals and Vinyls, LLC facility in Aberdeen, Mississippi Submitted to: Georgia Gulf Post Office Box 91 New Highway 25 Aberdeen, Mississippi 39730-0091 Attention: Mr. Kenny Akins Entec Project No. 20148 Date Report Submitted: July 28, 2000 Approved By: Glen Corley Project Manager ABD00048710 Table of Contents Executive Summary Detailed Test Results of Particulate Emissions Appendices A- Test Procedures B- Field Data Sheets C- Laboratory Analysis D- Equipment Calibrations E Test Calculations Page No. 1 3 23 27 211 229 272 ABD00048712 Prior to the first test run a preliminary velocity measurement of the exhaust gas was determined to verify the absence of cyclonic flow in the gas stream and to allow the selection of the appropriate nozzle diameter for isokinetic sample withdrawal. Two Nutech Model 2010, one Apex Model 522, and a Nutech Model 201 sampling trains which meet the specifications in the above- cited reference methods, were used to isokinetically extract the particulate samples by means of a heated stainless steel probe and heated filter compartment. Integrated flue gas samples for Fyrite analysis were extracted from the exhaust gases for determination of the flue gas oxygen and carbon dioxide. Due to the short exhaust configuration on each of the silo baghouse sources, an extension of the exhaust was attached and sealed to the outlet of each source in order for the test locations to meet the requirements of CFR 40 Part 60 Appendix A Method 1. Testing was conducted from two test ports oriented at 90 degree on the exhaust stack. The test ports were located at a minimum of 2.0 duct diameters downstream and 8.0 duct diameters upstream from the nearest disturbance. A 12 point traverse was used to determine the exhaust gas volumetric flow and to collect a representative sample of the particulate emissions. Each traverse was conducted for a total sampling time of sixty (60) minutes for each test run. No difficulties were encountered in the field collection of the samples or in the laboratory analysis of the samples by Entec Services, Inc. Testing was conducted in accordance with the applicable CFR 40 Part 60 Appendix "A" test procedures. On the basis of these facts and a complete review of the data and results, it is our opinion that the results reported herein are accurate and closely reflect the actual values which existed at the time the testing was conducted. Test results indicate the sources tested have an average combined emission rate of 18.12 lbs/ hr of particulate emissions. The No. 3 and No. 4 boil;er have a combined emission rate of 0.11 Ibs/hr for carbon monoxide and 3.84 Ibs/hr of nitrogen oxide. ABD00048713 Detailed Test Results ABD00048714 Georgia Gulf Aberdeen, Mississippi 675 Silo Baghouse Particulate Emissions Test Summary June 29, 2000 Test No. Stack Temperature Fahrenheit 1 2 3 Average 79.6 81.7 81.0 80.8 Stack Moisture, % 2.7 2.5 2.6 2.6 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 1,486 1,468 1,472 1,475 Stack Gas Flow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 1,418 1,399 1,403 1,407 0.0030 0.0032 0.0038 0.0033 0.04 0.04 0.05 0.04 ABD00048715 Georgia Gulf Aberdeen, Mississippi 676 Silo Baghouse Particulate Emissions Test Summary June 29, 2000 Test No. Stack Temperature Fahrenheit 1 2 3 Average 76.3 71.9 77.5 75.3 Stack Moisture, % 2.3 2.3 2.4 2.3 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 1,473 1,428 1,427 1,443 Stack Gas Flow DSCFM Particulate Concentration at Standard Conditions, Grains/F? Particulate Emissions lbs per hour 1,420 1,393 1,377 1,397 0.0040 0.0045 0.0028 0.0038 0.05 0.05 0.03 0.05 ABD00048716 Georgia Gulf Aberdeen, Mississippi 677 Silo Baghouse Particulate Emissions Test Summary June 29, 2000 Test No. Stack Temperature Fahrenheit 1 2 3 Average 74.0 76.8 81.9 77.6 Stack Moisture, % 2.4 2.9 2.7 2.7 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 1,613 1,574 1,601 1,596 Stack Gas Flow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 1,557 0.0071 0.09 1,504 1,519 1,527 0.0050 0.0063 0.0061 0.06 0.08 0.08 ABD00048717 Georgia Gulf Aberdeen, Mississippi 678 Silo Baghouse Particulate Emissions Test Summary June 30, 2000 Test No. Stack Temperature Fahrenheit 1 2 3 Average 74.1 76.6 76.8 75.8 Stack Moisture, % 2.7 2.2 2.1 2.3 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 1,644 1,543 1,457 1,548 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions ibs per hour 1,587 1,489 1,409 1,495 0.0021 0.0024 0.0037 0.0027 0.03 0.03 0.04 0.03 ABD00048718 Georgia Gulf Aberdeen, Mississippi 679 Silo Baghouse Particulate Emissions Test Summary June 29, 2000 Test No. Stack Temperature Fahrenheit 1 85.7 2 85.7 3 87.4 Average 86.3 Stack Moisture, % 3.0 3.1 2.5 2.9 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 1,201 1,203 1,181 1,195 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ft3 Particulate Emissions lbs per hour 1,130 1,131 1,114 1,125 0.0137 0.0089 0.0128 0.0118 0.13 0.09 0.12 0.11 ABD00048718 Georgia Gulf Aberdeen, Mississippi 679 Silo Baghouse Particulate Emissions Test Summary June 29, 2000 Test No. Stack Temperature Fahrenheit 1 85.7 2 85.7 3 87.4 Average 86.3 Stack Moisture, % 3.0 3.1 2.5 2.9 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 1,201 1,203 1,181 1,195 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ft3 Particulate Emissions lbs per hour 1,130 1,131 1,114 1,125 0.0137 0.0089 0.0128 0.0118 0.13 0.09 0.12 0.11 ABD00048719 Georgia Gulf Aberdeen, Mississippi 680 Silo Baghouse Particulate Emissions Test Summary June 29, 2000 Test No. Stack Temperature Fahrenheit 1 2 3 Average 76.3 75.0 72.0 74.4 Stack Moisture, % 3.5 3.2 2.3 3.0 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 1,129 1,468 1,508 1,368 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 1,075 1,405 1,465 1,315 0.0052 0.0018 0.0015 0.0028 0.05 0.02 0.02 0.03 ABD00048720 Georgia Gulf Aberdeen, Mississippi 687 Silo Baghouse Particulate Emissions Test Summary June 30, 2000 Test No. Stack Temperature Fahrenheit 1 2 3 Average 73.7 75.6 76.8 75.4 Stack Moisture, % 4.5 3.0 3.2 3.6 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Fiow ACFM 1,070 1,133 1,124 1,109 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particuiate Emissions lbs per hour 1,019 1,090 0.0051 0.0031 0.04 0.03 1,077 1,062 0.0040 0.0040 0.04 0.04 ABD00048721 Georgia Gulf Aberdeen, Mississippi 688 Silo Baghouse Particulate Emissions Test Summary June 30, 2000 Test No. Stack Temperature Fahrenheit 1 2 3 Average 80.3 80.0 79.3 79.8 Stack Moisture, % 4.1 4.5 4.4 4.3 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 1,577 1,451 1,574 1,534 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions ibs per hour 1,486 1,363 1,481 1,443 0.0035 0.0057 0.0062 0.0051 0.04 0.07 0.08 0.06 ABD00048722 Georgia Gulf Aberdeen, Mississippi No. 10 Cyclone Dryer Particulate Emissions Test Summary June 14, 2000 Test No. Stack Temperature Fahrenheit 1 106.4 2 105.3 3 105.0 Average 105.5 Stack Moisture, % 13.6 10.6 11.4 11.9 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Fiow ACFM 77,293 79,421 77,252 77,989 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 62,446 66,509 64,162 64,372 0.0045 0.0187 0.0059 0.0097 2.41 10.65 3.26 5.44 ABD00048723 Georgia Gulf Aberdeen, Mississippi No. 11 Cyclone Dryer Particulate Emissions Test Summary June 14, 2000 Test No. Stack Temperature Fahrenheit 1 106.5 2 106.4 3 106.8 Average 106.5 Stack Moisture, % 14.2 14.0 10.7 13.0 OxygimCo ncentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 73,236 74,985 70,590 72,937 Stack Gas Fiow DSCFM Particulate Concentration at Standard C onditions, Grains/Ff Particulate Emissions ibs per hour 58,805 60,338 58,939 59,361 0.0058 0.0065 0.0057 0.0060 2.92 3.35 2.86 3.04 ABD00048724 Georgia Gulf Aberdeen, Mississippi Fluidized Bed Dryer Particulate Emissions Test Summary June 15, 2000 Test No. Stack Temperature Fahrenheit 1 148.7 2 149.6 3 149.1 Average 149.1 Stack Moisture, % 24.2 24.9 26.0 25.0 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 33,709 33,605 34,663 33,992 Stack Gas Flow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 22,283 22,002 22,366 22,217 0.0092 0.0141 0.0023 0.0085 1.75 2.64 0.45 1.61 14 ABD00048725 Georgia Gulf Aberdeen, Mississippi Ventilation Baghouse Particulate Emissions Test Summary June 16, 2000 Test No. Stack Temperature Fahrenheit 1 2 3 Average 88.5 98.1 85.5 90.7 Stack Moisture, % 3.5 4.2 3.3 3.7 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Fiow ACFM 24,820 24,161 23,946 24,309 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 23,181 0.0068 22,013 0.0150 22,512 0.0098 22,569 / 0.0105 1.35 2.83 1.89 2.02 ABD00048726 Georgia Gulf Aberdeen, Mississippi Rotary Dryer No. 4 Particulate Emissions Test Summary June 14, 2000 Test No. Stack Temperature Fahrenheit 1 131.8 2 112.8 3 116.5 Average 120.3 Stack Moisture, % 7.1 6.9 6.6 6.8 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 23,631 24,906 23,982 24,173 Stack Gas Flow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 19,613 21,388 20,521 20,507 0.0039 0.0031 0.0044 0.0038 0.65 0.57 0.78 0.66 ABD00048727 Georgia Gulf Aberdeen, Mississippi Rotary Dryer No. 5 Particulate Emissions Test Summary June 15, 2000 Test No. Stack Temperature Fahrenheit 1 153.8 2 150.0 3 152.3 Average 152.0 Stack Moisture, % 7.1 6.4 6.8 6.7 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 22,101 23,722 21,265 22,363 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 17,731 19,310 17,153 18,064 0.0037 0.0098 0.0019 0.0051 0.56 1.62 0.28 0.82 ABD00048728 Georgia Gulf Aberdeen, Mississippi Rotary Dryer No. 6 Particulate Emissions Test Summary June 15, 2000 Test No. Stack Temperature Fahrenheit 1 156.4 2 158.1 3 157.3 Average 157.3 Stack Moisture, % 6.4 4.4 5.4 5.4 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Fiow ACFM 24,008 24,567 24,689 24,421 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 19,320 20,126 20,047 19,831 0.0033 0.0042 0.0047 0.0041 0.55 0.72 0.80 0.69 ABD00048729 Georgia Gulf Aberdeen, Mississippi Rotary Dryer No. 7 Particulate Emissions Test Summary June 16, 2000 Test No. Stack Temperature Fahrenheit 1 155.8 2 157.4 3 157.0 Average 156.8 Stack Moisture, % 7.7 7.1 6.2 7.0 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 25,672 27,328 25,585 26,195 Stack Gas Flow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 20,427 21,826 20,637 20,963 0.0122 0.0145 0.0125 0.0130 2.13 2.70 2.20 2.35 ABD00048730 Georgia Gulf Aberdeen, Mississippi Rotary Dryer No. 8 Particulate Emissions Test Summary June 15, 2000 Test No. Stack Temperature Fahrenheit 1 168.8 2 160.1 3 169.0 Average 166.0 Stack Moisture, % 3.9 3.5 4.7 4.0 Oxygen Concentration, % 20.0 20.0 20.0 20.0 Carbon Dioxide Concentration % 0 0 00 Stack Gas Flow ACFM 23,278 22,773 24,134 23,395 Stack Gas Fiow DSCFM Particulate Concentration at Standard Conditions, Grains/Ff Particulate Emissions lbs per hour 18,892 18,821 19,443 19,052 0.0034 0.0100 0.0059 0.0064 0.55 1.61 0.99 1.05 ABD00048731 Test No. Georgia Gulf Aberdeen, Mississippi No. 3 Boiler Pollutant Gas Emissions Test Summary June 29, 2000 123 Average Stack Temperature Fahrenheit Stack Moisture, % Oxygen Concentration, % Nitrogen Oxide Concentration ppm Carbon Monoxide Concentration ppm Carbon Dioxide Concentration % Stack Gas Flow ACFM Stack Gas Flow DSCFM Nitogen Oxide Emissions lbs per hour Carbon Monoxide Emissions lbs per hour 205.2 8.1 14.19 19.43 5.01 3.28 4,784 3,499 0.49 0.08 204.9 7.6 14.21 19.71 6.67 3.31 4,517 3,325 0.47 0.10 205.8 8.3 14.28 19.89 5.54 3.30 5,112 3,730 0.53 0.09 205.3 8.0 14.23 19.68 5.74 3.30 4,804 3,518 0.50 0.09 ABD00048732 Test No. Georgia Gulf Aberdeen, Mississippi No. 4 Boiler Pollutant Gas Emissions Test Summary June 29, 2000 1 23 Average Stack Temperature Fahrenheit Stack Moisture, % Oxygen Concentration, % Nitrogen Oxide Concentration ppm Carbon Monoxide Concentration ppm Carbon Dioxide Concentration % Stack Gas Flow ACFM Stack Gas Flow DSCFM Nitogen Oxide Emissions lbs per hour Carbon Monoxide Emissions lbs per hour 259.8 260.5 257.6 259.3 10.7 10.7 11.0 10.8 5.96 6.90 5.77 6.21 60.63 55.31 61.36 59.10 0.71 0.69 0.32 0.57 8.51 7.91 8.59 8.34 12,111 11,943 11,974 12,009 7,948 7,835 7,862 7,882 3.45 3.11 3.46 3.34 0.02 0.02 0.01 0.02 ABD00048733 Appendix A Test Procedures ABD00048734 Procedures The particulate emission rates were determined using EPA Methods 1-5, CFR Title 40, Part 60, Appendix A. The calibration and quality assurance procedures of EPA CFR 40 Part 60 Appendix A Methods 1, 2, 3, 4,5 and the "Quality Assurance Handbook for Air Pollution Measurement System" Volume III Stationary Source-Specific Methods were followed throughout the duration of the field and laboratory testing. The most current revision of each method (as described in the Federal Register) was used. Stack Gas Volumetric Flow The velocity of the gas stream was determined according to EPA Reference Method 1 and 2 by reading the instantaneous velocity head with an inclined manometer at each sampling point with a calibrated S-type pitot tube attached adjacent to the sample nozzle. The stack pressure was measured with the static side of an S-type pitot tube. A calibrated pyrometer was used to measure stack temperature at each sampling point. The stack was tested for cyclonic flow according to EPA Reference Method 1. Stack Gas Molecular Weight The carbon dioxide and oxygen concentrations was determined using EPA Reference Method 3. An integrated sample of the flue gas was extracted from the gas stream during each particulate test run at a constant flow rate and collected in a 7.5 liter tedlar bag. The bags were then returned to the laboratory and analyzed by Fyrite analysis. Standard commercially prepared solutions were used in the Fyrite analyzer. The molecular weight of the gas was calculated using the moisture, oxygen and carbon dioxide content and the measured stack gas temperature. The tedlar bags used for collecting the gas samples were verified to be leak free prior to collecting the bag samples. The Fyrite sampling system was also verified to be leak free prior to the analysis. 24 ABD00048735 Moisture Content The moisture content used for calculating the gas stream flow rate was determined by measuring the amount of condensed moisture in the impingers of the sampling train as described in EPA Reference Method 4 at the completion of each test. The moisture collection system consist of four glass impingers. The first two impingers are loaded with 100 ml of deionized water the third impinger is left empty and the fourth impinger is loaded with fresh silica gel. Ice is placed around the impingers to maintain a temperature <68 F. The outlet temperature of the fourth impinger is monitored and recorded throughout the duration of the testing to verify the temperature is below <68 F. Particulate Loading The particulate sample train consist of a heated stainless steel sample probe and liner equipped with a S-type pitot tube and thermocouple. The probe is attached to a sample module consisting of a heated filter compartment which houses the in-line filter holder equipped with a pre-weighed glass fiber filter for the collection of the particulate. The sample module also holds the impingers on the outlet side of the heated filter compartment for the collection of the condensed moisture. The sample module is connected to a control module by means of an umbilical cord. The control module consist of a dry gas meter, calibrated orifice, leak free pump, two inclined manometers, temperature controllers for the heated filter compartment and probe and a thermocouple indicator to monitor the required temperatures during the testing. Particulate samples are collected as follows: The sample gas is drawn through the sampling probe isokinetically and passed through a 3-inch Whartman glass fiber filter where particulates are removed. The sample gas is then passed through an ice-cooled impinger train and dessicant-packed column which absorbs any remaining moisture. The sample gas then passes through a vacuum pump followed by a dry gas meter. The ABD00048736 dry gas meter integrates the sample gas flow throughout the duration of the test. A calibrated orifice attached to the outlet of the dry gas meter provides real time flow rate data. A representative particulate sample is acquired by sampling for equal periods of time at the centroid of a number of equal area regions in the exhaust stack. The sampling rate is adjusted at each test point maintaining an isokinetic sampling condition. After the sampling is complete, the filter is removed and placed in a storage container for shipment back to the laboratory for analysis. The nozzle, probe liner and inlet side of the filter holder are quantively washed with a pure grade acetone and stored in a marked container. The samples are transferred back to the laboratory were they are logged in and analyzed. The volume of acetone rinse is noted and transferred to a tarred fleaker and evaporated off at 97-105 F. This temperature is used to prevent condensation of atmospheric moisture due to the cooling effects induced by the evaporating acetone. The acetone-free sample is placed in an oven and dried at 105 C for thirty minutes and then placed in a dessicator. After the sample has desiccated for twenty four hours the sample is weighed to the nearest 0.1 mg. The filter sample is transfered to the original petri dish in which the original weight was obtained and placed in a drying oven for 2 hours at 105 C. The filter and petri dish are then placed in a dessicator. After the filter and petri dish have desiccated for twenty four hours the sample is weighed to the nearest 0.1 mg. Visual examination of the samples are made to determine if any unusual characteristics of the samples are observed. The weight of the acetone rinse is corrected for the weight of the acetone blank. ABD00048737 Appendix B Field Data Sheets ABD00048738 675 Silo Baghouse Field Data Sheets ABD00048739 Schematic of Sampling Site Silo Baghouse No. 675 Vent Stack 29 ABD00048740 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35025 Client: Georgia Gulf Source: Silo No. 675 Job No.: 20148 Data Input By: L. Beane Run Number Date Time Beaan-Ended Samplina Time. Minutes Stack Area. Sauare Feet Barometric Pressure. Inches of mercury Stack Pressure. Inches of mercury Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter, Inches Meter Volume. Cubic feet Meter Temoerature. Degrees F Avq. Orifice Delta P. Inches of Water Volume H20 Collected. MilliLiters C02 Concentration. Percent 02 Concentration. Percent Ava. Sa. Rt. of Delta P. Inches of Water Stack Temperature. Degrees F Total particulate collected, grams Standard Meter Volume. Cubic Feet Standard Water Volume. Cubic Feet Moisture Fraction Molecular Weight Of Stack Cas Density Of Stack Cas Average Stack Gas Velocity. Feet/Second Stack Gas Flow Stack Conditions. ACFM Stack Gas Flow < Standard Conditions. DSCFM Isokinetic Sampling Rate, Percent Particulate concentration @ Std.Cond..Grains/Cu.Ft. Particulate emissions, lbs per hour INPUT DATA 1 2 3 AVERAGE 6-29-00 1537-1653 6-29-00 1704-1810 6-29-00 1823-1930 HHHHHH 60 60 60 60 0.785 0.785 0.785 30.02 30.02 30.02 30.02 30.00 30.00 30.00 30.00 0.84 0.84 0.84 0.997 0.997 0.250 0.250 0.250 37.055 36.765 36.870 36.897 81.4 87.4 84.0 84.3 1.26 1.25 1.25 1.26 21.0 19.0 20.00 20.0 0.0 0.0 0.0 0.0 20.0 20.0 20.0 20.0 0.553 0.545 0.547 0.55 79.6 81.7 81.0 80.8 0.0071 CALCULATED DATA 0.0073 0.0089 0.0078 fliqrriiWT'-V.mirtiriwjlMirw iltiMimin iihiwpwirwrirp iwfiiif 36.246 35.567 35.890 35.901 0.988 0.894 0.941 0.941 0.027 0.025 0.026 0.026 28.513 28.535 28.524 28.524 0.0726 0.0724 0.0725 0.0725 31.528 31.144 31.240 31.304 1.486 1.468 1.472 1.475 1,418 1.399 1.403 1.407 98.14 97.67 98.23 98.01 0.0030 0.0032 0.0038 0.0033 0.04 0.04 0.05 0.04 30 ABD00048741 ENTEC Services, inc. _______________________________________________________ 2S Commerce Ave.-Suite 104-Hueytown. Alabama 35023 Client: Source: Georgia Gulf Silo No. 675 Date: Run No.: 6/29/2000 1 Traverse Point M 1> 1,.-23 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 WiWMWMMMWi Delta P 0.17 0.19 0.30 0.29 0.40 0.37 0.19 0.23 0.30 0.40 0.44 0.50 0.32 So. Rt. Delta P 0.4123 0.4359 0.5477 0.5385 0.6325 0.6083 0.4359 0.4796 0.5477 0.6325 0.6633 0.7071 0.5534 Delta H 0.68 0.76 1.20 1.16 1.60 1.48 0.76 0.92 1.20 1.60 1.76 2.00 1.26 Tm In rn 79 80 80 81 82 83 85 84 . 85 84 85 86 82.83 Tm Out (*F) 78 79 79 79 79 79 81 81 81 81 81 82 81.4 Ts m 79 79 79 79 79 79 80 80 80 80 80 81 79.6 31 ABD00048742 J0 s ft r 3 u. pp ft p ? ft p 0 V>4*3 r* r ro r /00 0 r c* 6 3E3O C -- to t3 0 tnl V 0 oA Hi rC > 03 i f|* E in in K 0>3 3 i5 4i o> Xnfl CO 2* CD --< fc CL E H 0- r <c? rc- 3 0. 0 SK &z o3 ^ r Cr r2 <r*Nr<-H<rri& 9* l %- %cm n% ^3 UO. Iff-i L. (D -= 2 0eo3. g0e3. a0e3 o0c3. ifo2" %d J? 3 9 rb J3 iL) o a3 oJ3 w Ie3X E rv tO P ** in *> = <r> r p a .ft oa \n 3 P$ rj:8 S? < 01 d j3 t2 a < 0 71 fl *> o6 if rt C0 P h 603 0 'n s 1w> -*7j- r- `/) T Field Notes: 32 ABD00048743 Client: Source: Georgia Gulf Silo No. 675 ENTEC Services, Inc. 25 Commerce Ave.-Sulte 104-Hueytown, Alabama 35023 Date: Run No.: 6/29/2000 2 Traverse Point 1-1 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.14 0.19 0.28 0.37 0.43 0.47 0.50 0.48 0.40 0.20 0.16 0.14 0.31 PARTICULATE FIELD DATA, METHOD 5 Sa. Rt. Delta P 0.3742 0.4359 0.5292 0.6083 0.6557 0.6856 0.7071 0.6928 0.6325 0.4472 0.4000 0.3742 Delta H 0.56 0.76 1.12 1.48 1.72 1.88 2.00 1.92 1.60 0.80 0.64 0.56 Tm In m 82 81 85 88 88 93 96 95 88 89 91 92 0.5452 1.25 89.00 Tm Out rn 81 81 80 85 85 90 92 90 85 85 87 89 87.4 ts rn 80 80 80 80 82 83 85 84 80 81 82 83 81.7 I lilt's: 1 ABD00048744 0 $ < Q 0 09 0 >i re 5 0 O oN Oo zN 'p <oeo -1C0 S*t eo 5 rce 3ffl -- xi E SO Q. ON Is C MO 09 >^SU,_- E_2_c_J=S z*5 LL 8 > o. 5 re^ ?-: v-P t'-o 8 !/> Ig511 9 -iQ_-- s>o o 00o- 3>o 0 1 co I30-- 0 0 n3 UJ ijg 0 s* TCrJe <N E* Sre CD irSe ? 55 2 i?re ita- * r3tj<>3r J<Sre o o o c * o- % 0 , OC p0 <vJ re : Q I*re O .a gg fl n a Z3 Q. 0| ^%-N%P%9 Jft 09 5 3 ^ 0c9 a: acs a: "75 mo a. a. o. 2 E EE E. oZ 43 i '/3 Ore 55 t-O 5 Uj 'O 3 % V> vDC EcZ J0 S* 8* t M i? c3 w j2i "Qre 3 'll o: T0 H4 w JE 3 3are 01 HOr > *70 0 C. 0 i **1 H ffJ ** aca. r- $vIS E n *? ^ u. Is LoSrfesewx*as .N C* i/i * & a. E h* M 3* CO ^ ,-7 wr $ 8UK* 2 = l $0 0> x: <0 ? 0- % v j* 4 3 7? 4 0fti -- c6 ai fl al o . 09 Ma Jj 7re K) <t oo 5C t3 7> */? jJlj r ol fo>il rr ci >< j <r T 37 ^ <?r S -on- WH+H c o Q. Field Noles: 34 ABD00048745 Client: Source: Georgia Gulf Silo No. 675 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-HuevtOwn, Alabama 35023 Date: Run No.: 6/29/2000 3 Traverse Point 1-1 k V2 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 IliliJIlP Delta P 0.13 0.16 0.27 0.33 0.45 0.51 0.16 0.19 0.30 0.37 0.43 0.46 0.31 Sa. Rt. Delta P 0.3606 0.4000 0.5196 0.5745 0.6708 0.7141 0.4000 0.4359 0.5477 0.6083 0.6557 0.6782 0.5471 Delta H 0.52 0.64 1.08 1.32 1.80 2.04 0.64 0.76 1.20 1.48 1.72 1.84 1.25 Tm In m 84 84 85 85 84 84 84 85 85 85 85 86 84.67 Tm Out CF> 83 83 83 83 83 83 83 84 84 84 84 84 84.0 Ts CF) 81 81 80 80 80 81 80 81 81 82 82 83 81.0 35 ABD00048746 QK < o > IQ cs NO NO OON2 o ? 0$ 1*1 a 0o (0 CcD J%MZ * -- -- 5m 1o3fa* rSEgr gecs2| O r jg 2 O) at * 5S u- c E 2 c as E 3 o? >'l > r o i5 si t"' 4> 6ll3 HE i a >n o>0 CO <o a 2Oo3 . 0 J 1> 3 PD E4 8 0 #0^ rO 0 <r & p CD aa 55 (ft jCcD a tr aj _ * 9 SI 0 IM 2 co 89$ a *3 3 $ to r5 3 r -P tn j, . |ga 8 % 5 * do Vo D_ oo =cor =^^ r * J S gi O z a. nnj o %% U3-0OL) . 3u. kSO.) OI_) *--nm 2 _c c c c o Q.Q.Q.Q.*- 2 EEE E E - 6 f t I^ '/> A 81 l t j s m `i < j^j 52Q -3 D jot ~ co 55 3 *9 a: s a CZ 3) I J3 3 >> Q. o ^1 IJ .o1 o LX> Erf i- a 4 c~ E 01 o > 3* a. -4 E !* <a = .O* TS s a. HE 2 3* T 2 9* * J= ^ <0 Q. *5 Vi w g>* sffl ? ^3 I- c o CL ^O 0. JdQ K7 rfl rt ' 3 ^ ! 34 3 < V-H5) Q *54 *) ^ y*1 N 5d>^ wi3 3 1A T Vi t OQ $ <X V 9D 9r2 - 05 J */ d 01 w <\ ?.3 *r v) o W T ^rl `0 T 'r. 9 - .4 m \f> Field Notes: 36 ABD00048747 676 Silo Baghouse Field Data Sheets ABD00048748 Schematic of Sampling Site Silo Baghouse No. 676 Vent Stack 38 --team9%im Client: Georgia Gulf Source: Silo No. 676 ABD00048749 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35025 PARTICULATE EMISSIONS CALCULATIONS Job No.: 20148 Data Input By: L. Beane Run Number Date Time Beqan-Ended SamDlinq Time. Minutes Stack Area. Square Feet Barometric Pressure. Inches of mercurv Stack Pressure, inches of mercurv Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter. Inches Meter Volume. Cubic feet Meter Temperature. Deorees F Avo. Orifice Delta P. Inches of Water Volume H20 Collected. MilliLiters C02 Concentration, Percent 02 Concentration. Percent Avo. So. Rt. of Delta P. Inches of Water Stack Temperature. Deorees F Total particulate collected, arams Standard Meter Volume, Cubic Feet Standard Water Volume. Cubic Feet Moisture Fraction Molecular Weioht Of Stack Gas Densitv Of Stack Gas Averaqe Stack Gas Velocity. Feet/Second ktack Gas Flow <> Stack Conditions. ACFM Stack Gas Flow <> Standard Conditions, DSCFM Isokinetic Samolinq Rate. Percent Particulate concentration @ Std.Cond..Grains/Cu.Ft. Particulate emissions, lbs per hour 12 6-29-00 6-30-00 1017-1128 0830-0930 60 60 0.785 0.785 30.02 30.13 30.00 30.11 0.84 0.84 0.996 0.996 0.250 0.250 38.360 35.840 75.9 75.3 1.24 1.18 19.0 18.0 0.0 0.0 20.0 20.0 0.551 0.537 76.3 71.9 0.0098 0.0105 CALCULATED DATA 37.871 0.894 0.023 28.551 0.0732 31.280 1,473 1.420 102.37 0.0040 0.05 35.546 0.847 0.023 28.549 0.0740 30.326 1,428 1.393 97.95 0.0045 0.05 3 6-30-00 0947-1053 60 0.785 30.13 30.11 0.84 0.996 0.250 35.684 83.4 1.17 18.0 0.0 20.0 0.534 77.5 0.0064 34.861 0.847 0.024 28.544 0.0732 30.306 1,427 1.377 97.18 0.0028 0.03 AVERAGE 60 30.09 ?0-0 7 36.628 78.2 1.20 18.3 0.0 20.0 0.54 75.3 0.0089 36.092 0.863 0.023 28.548 0.0735 30.638 1.443 1.397 99.17 0.0038 0.05 39 ABD00048750 Client: Source: Georgia Gulf Silo No. 676 ENTEC Services, Inc. 25 Commerce Av<,-Suite 104-Hueytown, Alabama 3S023 Date: Run No.: 6/29/2000 1 Traverse Point 1-1 k 1-2 f 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.17 0.23 0.25 0.24 0.31 0.42 0.21 0.27 0.34 0.39 0.43 0.47 0.31 So. Rt. Delta P 0.4123 0.4796 0.5000 0.4899 0.5568 0.6481 0.4583 0.5196 0.5831 0.6245 0.6557 0.6856 0.5511 Delta H 0.68 0.92 1.00 0.96 1.24 1.68 0.84 1.08 1.36 1.56 1.72 1.88 1.24 Tm In rn 73 74 74 75 75 76 77 79 81 82 82 84 77.67 Tm Out rn 71 71 71 72 72 72 74 75 77 78 78 78 75.9 Ts rn 79 77 77 77 76 77 76 76 76 75 75 75 76.3 40 ABD00048751 ia >O V'm q oj c j c 01 $ iQ. ^ E 3 ^ 9 ^3 i 3 i c v-> 3* u. <0 s* 3cfeo 2 W3 t* r* CL HE =o3 3$ c M \ro yt* x* e? ? Si *r>* * C" \$J -N *q H $ Vfl 0 cm <n t| -- ^ M ^ VJ S3 off)i o) > a "~= S a=aacacHo 2 E E g r3 38 H * B* oS >j1^d W 5Q i *3 oC3: % HE sH a 1NO 4 <A !?# $ 3 c Wj| *3j'^-,'| *3|'3|'/>|^| 0o. r CL Field Notes: 41 ABD00048752 Client: Source: Georgia Gulf Silo No. 676 ENTEC Services, Inc. 25 Commerce Ave.-Sulte 104-Hueytown. Alabama 3S023 Date: Run No.: 6/30/2000 2 Traverse Point M | _1-2 * ,.3 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.21 0.27 0.25 0.22 0.30 0.37 0.12 0.25 0.31 0.40 0.41 0.44 fPMMPM 0.30 Sa. Rt. Delta P 0.4583 0.5196 0.5000 0.4690 0.5477 0.6083 0.3464 0.5000 0.5568 0.6325 0.6403 0.6633 0.5368 Delta H 0.84 1.08 1.00 0.88 1.20 1.48 0.48 1.00 1.24 1.60 1.64 1.76 1.18 Tm In CF) 70 71 73 73 74 76 77 79 79 82 84 85 76.92 Tm Out rn 70 70 71 71 71 72 74 75 75 77 79 79 75.3 Ts m 71 71 71 72 72 72 72 73 73 72 72 72 71.9 * ABD00048753 ct*rl tcor ;a - V t* Q <r $ s r* s'O') s1')? ft r* r* * W * <ao> p- r c 'r^ 0 a JT CD JD(0 ** *" .=|O3 eCc[_O H--ffl =z ?Q)ot_ cCD5_<05-s wf cZ oE 0 u s' CO > o ci CO > H to to at>o>, $To 5 a cft 3I as:<N rg o TM 8 o -l s?g li i m C. --O? J L > 0* --0o. -->-o1 5 tn % 3 ttoo -io T3c3) c Ifl. iCL 1 1 |O co Q: CM t * CD I CD 2 1! ir E <3 A yi * 1 2 oo oc o c * T" _ !0/> fl 8 tCOo O d d 4 To ^ 5 To O*3 8 & zo a2 0 0 d O' u S"* A ID '<0>1 .v* 10 Bra ss Ez %t- %m ae*3 ^stfc w i_ t_ u ^ to 3 TS *|5 CO) 3C3 0C3 OC) --O o. a. o. a f" 2 EE jEo Q (1 ju* 55 03 i 3 > o. U 5^1 l.w U) E 3 i^ > a0 taq *f_J M* S3 E a V v 1/J 5c 6 Z *f nl fl ii d 3 '!2 *i * *\ ^ !3 i i rt to 2^ 2n ES 5W a. Es 5 * /C - - A r\ r rr *??? 1? rp jr A u>o tc ie 44 8X i -3 <7 a ^s < C0 is* d <* f s at ClO < E 0 H 3 a: E f- O' c o 0 > W 3 - <t 5 a- * CL 1o CL Field Notes: 43 ABD00048754 Client: Source: Georgia Gulf Silo No. 676 ENTEC Services, Inc. 2S Commerce Ave.-Suite 104-Hueytown. Alabama 35023 Date: Run No.: 6/30/2000 3 Traverse Point 1-1 fc 1-2 * i. 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.20 0.29 0.30 0.35 0.31 0.37 0.14 0.17 0.23 0.28 0.46 0.41 0.29 So. Rt. Delta P 0.4472 0.5385 0.5477 0.5916 0.5568 0.6083 0.3742 0.4123 0.4796 0.5292 0.6782 0.6403 0.5337 Delta H 0.80 1.16 1.20 1.40 1.24 1.48 0.56 0.68 0.92 1.12 1.84 1.64 1.17 Tm In CF) 80 81 81 82 83 85 87 87 86 87 88 89 84.67 Tm Out m 78 78 80 80 81 83 84 84 84 84 85 85 83.4 Ts m 74 74 74 76 77 77 78 78 79 80 81 82 77.5 ABD00048.755 SQ $ < 0 a 0a9 >> 0 v c < C0C3O9 CM CM o i 8 *i i l' r- 0 T9 *4 0c3 to 45 50 -O 35 7c5 E 2 = 5 2 So CL NA O 2o 'tfc -- - I fe SS| =E E 3 O > u 5 T S* " 1/9 t osi^l! 8 s lilOslo 3to CO * 1* s CD s *S N. (L $ iS ' <35 18g 2^ O4 CL c%n 09 act 02 CM vj i-M* * E 1o <31 2 OctJ .>3_ 3 44 >1 ^ V '-0 V) 12f o 'i * * i llfc Ik W a t- I 5d*5| <3 <3 r C* ^Q| rs f* $8 Jc* ^r 5 M ft J* 94 M>-KwM * E*, /a v9 MM ~^ 3 < <0 Sto 8So Mli o3 i%- %cm ffl c5nft 0 '%>t 0 7n TS 09 39 09 09 is 52 cQ.CcL cQ. cQ. i"o 2 EE - S0 Z CL 5 <% Q^ d* t j? a4 O W M ai:n % O) % u. a n-- "f cZ a < <0 00 fH a * ^ ^ <3 <2 Q |>9 <- Q 3* <* V) tfl m4S = V9| f- V) n 4 !$$a rt c "5 Vw CL <!> wO CL Field Notes: 45 ABD00048756 677 Silo Baghouse Field Data Sheets ABD00048757 Schematic of Sampling Site Silo Baghouse No. 677 Vent Stack 47 ABD00048758 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama S502S Client: Georgia Gulf Job No.: 20148 Source: Silo No. 677 Data Input By: L. Beane INPUT DATA 1 "i ~ I flMMftllilHM II In i"HMT|lirill M>I11 HIM--11'HIM 1 Hln 'IMK 'imfc--iWF |Tl)T r H'i1' mmmmtmsmm "" ` | Run Number Date 1 6-29-00 2 6-29-00 3 AVERAGE ______6-29-00_____ HBHMW Time Beaan-Ended Samplina Time. Minutes Stack Area, Sauare Feet 1027-1130 60 0.785 1217-1321 60 0.785 1350-1457 60 0.785 Miv--* J60 Barometric Pressure, Inches of mercury 30.02 30.02 30.02 30.02 Stack Pressure, Inches of mercury Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter, Inches 29.96 0.84 0.997 0.240 29.96 0.84 0.997 0.240 29.97 29.96 0.84 * o^?6_____________ MBMBBB 0.240 ! Weter Volume, Cubic feet 38.310 37.955 38.483 38.249 Meter Temperature, Dearees F 77.3 78.7 87.8 81.3 Ava. Orifice Delta P. Inches of Water 1.49 1.39 1.43 1.44 Volume H20 Collected. MilliLiters 20.0 24.0 22.0 22.0 C02 Concentration, Percent 0.0 0.0 0.0 0.0 02 Concentration, Percent 20.0 20.0 20.0 20.0 Ava. So. Rt. of Delta P. Inches of Water 0.604 0.587 0.594 0.60 Stack Temperature, Degrees F 74.0 76.8 81.9 77.6 Total particulate collected, qrams 1 jinn MMBWMiiiCT iiiwiwiwaii 0.0174 CALCULATED DATA 0.0120 0.0152 0.0149 *1am a1 iimi wiiHMi'iwra 1 Standard Meter Volume, Cubic Feet 37.785 37.328 37.180 37.431 Standard Water Volume, Cubic Feet 0.941 1.130 1.036 1.036 Moisture Fraction 0.024 0.029 0.027 0.027 Molecular Weiaht Of Stack Gas 28.537 28.483 28.507 28.509 Density Of Stack Gas 0.0733 0.0728 0.0722 0.0728 Averaae Stack Gas Velocity. Feet/Second 34.243 33.417 33.986 33.882 fctack Gas Flow @ Stack Conditions. ACFM 1,613 1,574 1,601 1,596 Rack Gas Flow @ Standard Conditions. DSCFM 1,557 1,504 1,519 1,527 Isokinetic Samolina Rate. Percent 101.06 103.38 101.93 102.12 Particulate concentration <> Std.Cond..Grains/Cu.Ft. 0.0071 0.0050 0.0063 0.0061 Particulate emissions, lbs per hour 0.09 0.06 0.08 0.08 48 ABD00048759 Client: Source: Georgia Gulf Silo No. 677 ENTEC Services, Inc. 2S Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Date: Run No.: 6/29/2000 1 Traverse Point 1-1 1 I-2 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.20 0.31 0.35 0.33 0.32 0.52 0.28 0.30 0.53 0.50 0.43 0.39 0.37 Sa. Rt. Delta P 0.4472 0.5568 0.5916 0.5745 0.5657 0.7211 0.5292 0.5477 0.7280 0.7071 0.6557 0.6245 0.6041 Delta H 0.80 1.24 1.40 1.32 1.28 2.08 1.12 1.20 2.12 2.00 1.72 1.56 1.49 Tm In CF) 75 76 78 79 79 80 78 78 80 81 82 82 79.00 Tm out rn 72 73 74 75 75 76 76 76 77 77 77 78 77.3 Ts CF) 72 73 73 74 74 73 74 75 75 75 75 75 74.0 49 n1i l i [lilli 0 ABD00048760 * rj r Vn r V/>os 3 tr r J > \A ryO Is 0 0 So 04 0 O0 44 < OQ 5 0 y0 (0A3 1 C Q % ---- s g |hz 203 il rt .2 r, *: rf " - ~ os => |V, V'vtN; fv win o c W] 0 >O i3 >oro 0-- ^ rf in in _> c <tA C0 o CM CM OO O JoC @ V* O ? g 3 l! .a* JCL> toA .o2 CL > 3 t3in- v> )o ^ 30 c*foc A C Jo- <nl/1 3 E o CD o 703 * 0. K<L 5^Q!ft o ro 1h 55 2 0 C- /N O' =^ u. 4 1tn 0 0 din c o X m o 0 % t" %> 8 c N\ f oo := o o o. c r- 0** jD O_ S o ii i 0 0- 0 Z CL gg ir C Z 1%i_- (%iN-- %t- V%u (A = 05 D) O) 03 i2 cccco Q. Q. D. Q. ^ EcEE <JO>) < J >>li oV E b jcora: co %_ ^ rf] 2* Q-I41 r* rO CH P> V\ K V\ 2*; o- v > T O N N N <n N N > in r5o iu2 r^> 5w1 MSI' N Cl. hE- =3 N o wft N V\ y va v> v3|Q0 0* N rH to <# r4C0| i 3N r* V\ N Cl <5 < 01 r4 N1 V, Ol S .ae>Hf< s CflO) 0: f^U V' s > O Q QQcro C P `r4f j? . v-3 iF Sijri si? 55 c3 grP.0^ r4 < sv. oe CL Field Notes: 50 ABD00048761 Client: Source: Georgia Gulf Silo No. 677 ENTEC Services, Inc. 25 Commerce Aye,-Suite 104-Hueytown, Alabama 35023 Date: Run No.: 6/29/2000 2 Traverse Point 1-1 fe ]'2 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 fjWiirtllSP Delta P 0.22 0.29 0.34 0.31 0.31 0.47 0.26 0.31 0.41 0.45 0.41 0.40 0.35 Sa. Rt. Delta P 0.4690 0.5385 0.5831 0.5568 0.5568 0.6856 0.5099 0.5568 0.6403 0.6708 0.6403 0.6325 0.5867 Delta H 0.88 1.16 1.36 1.24 1.24 1.88 1.04 1.24 1.64 1.80 1.64 1.60 1.39 Tm In rn 78 78 80 81 81 81 83 83 83 84 85 84 81.75 Tm Out CF> 78 78 78 78 78 78 79 78 79 80 80 80 78.7 ts rn 76 76 76 77 77 77 77 77 77 77 78 77 76.8 51 ABD00048762 $ 0 a t((o00 >. CO 5Oto 0 COoM ?<=0: oo C 3 <5 to 05 i </) NJ 7.5fSl)' =%.I. u_(=0_s_C(0 2z- to o 0 fr* 00 rs) 0 > r* Vk N Vi N N V\ H Vk *4 > V- Vk TS * \A > N > f) (0 2^ 3O 5> W H QE0). i- . N K Is* 1$ CD CD CD oHNN NN <H o CD Od 0 - N CflOQ 00 to j<=0QQ3 Q C -c I2'So: M*<. fKr- Q CL Field Noles: 52 ABD00048763 Client: Source: Georgia Gulf Silo No. 677 ENTEC Services, inc. 2S Commerce Ave.-Sulte 104-Hueytown, Alabama 3S023 Date: Run No.: 6/29/2000 3 Traverse Point 1-1 h 1-2 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.21 0.30 0.34 0.32 0.39 0.49 0.29 0.30 0.47 0.43 0.40 0.35 0.36 PARTICULATE FIELD DATA, METHOD 5 Sa. Rt. Delta P 0.4583 0.5477 0.5831 0.5657 0.6245 0.7000 0.5385 0.5477 0.6856 0.6557 0.6325 0.5916 Delta H 0.84 1.20 1.36 1.28 1.56 1.96 1.16 1.20 1.88 1.72 1.60 1.40 Tm In fF) 82 84 86 87 89 90 92 94 92 92 93 93 0.5942 1.43 89.50 Tm Out CF> 81 82 83 85 86 86 88 87 87 89 90 90 87.8 . Ts fF) 82 82 81 82 82 83 82 82 82 82 82 81 81.9 ABD00048764 (005 loS 0 II (MNQN OOo^ rM r W) Jli9* V5 r J !0 V) _0C5 jn SI j; a 5 V) -S5 % _ -- t. ro JS c H n eIz w<J) = U. E = o ou o t/> re > o r > __ rt44 2 T gtol gelo U 00 ^" i V) _ D- > s oU) gA 41 o 50 (* E o re CQ J Eo_ . 0 j*u: l 0 CSOfc CO cCD TcOr TM _T_*h w% A 34 $ ft U- 3 2 w Q. fE- M <# _ -- 3 0Q| O - rO ^ % US M f P *c c S ft a* cj* j) A d- fit fid p <T Q C* l -J A <T (J <r cr *. u. <j <1 * % o oo o c *- - i!iz i*f-c C%M c*3 %*<T L. I_ l_ l_ (ft -= O) 05 05 O) -2 aE .a .a .aE^" SEES H j i 1 ri r -9 1r ( C CL co s E X b <*> u co KJ *fc < % *7 I'U E H 3S 0 S* Cl >| O" 5 rO o I u JS co c% 0 > W) CL e o Q- $.0 */ V\f>) CO -9 Field Notes: 54 ABD00048765 678 Silo Baghouse Field Data Sheets ABD00048766 Schematic of Sampling Site Silo Baghouse No. 678 Vent Stack 56 ABD00048767 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Client: Georgia Gulf Source: Silo No. 678 Job No.: 20148 Data Input By: L. Beane INPUT OATA Run Number Date Time Began-Ended 1 6-30-00 0819-0919 2 6-30-00 0941-1041 Sampling Time. Minutes Stack Area. Sauare Feet Barometric Pressure. Inches of mercurv Stack Pressure. Inches of mercurv Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter. Inches Reter Volume. Cubic feet Meter Temoerature. Dearees F 60 0.785 30.05 30,03 0.84 0.990 0.250 46.055 80.3 60 0.785 30.05 30.03 0.84 0.990 0.250 42.790 89.2 Avq. Orifice Delta P, Inches of Water 1.76 1.54 Volume H20 Collected. MilliLiters C02 Concentration, Percent 02 Concentration. Percent Ava. Sa. Rt. of Delta P. Inches of Water Stack Temperature. Degrees F 26.0 0.0 20.0 0.6160 74.1 20.0 0.0 20.0 0.5767 76.6 Total particulate collected, arams 0.0061 0.0064 CALCULATED DATA wt ni--uni. ,rr ;... inji..i,nwi'iwi.iiin,|ii i^iiiipiii ii iiiiimn tiiilimn mi1 ti; Standard Meter Volume. Cubic Feet Standard Water Volume, Cubic Feet 44.925 1.224 41.041 0.941 Moisture Fraction Molecular Weiaht Of Stack Gas Density Of Stack Gas Average Stack Gas Velocity, Feet/Second Stack Gas Flow @ Stack Conditions. ACFM Rack Gas Flow < Standard Conditions, DSCFM Isokinetic Sampling Rate. Percent Particulate concentration < Std.Cond.,Grains/Cu.Ft. Particulate emissions, lbs per hour 0.027 28.5136 0.073 34.898 1.644 1,587 108.67 0.0021 0.03 0.022 28.5578 0.073 32.756 1.543 1.489 105.81 0.0024 0.03 3 6-30-00 1105-1205 60 0.785 30.05 30.03 0.84 0.990 0.250 42.525 99.5 1.41 18.0 0.0 20.0 0.5448 76.8 0.0095 AVERAGE 60 bmmmi 30.05 30.03 43.790 89.7 1.57 21.3 0.0 20.0 0.5792 75.8 0.0073 40.025 0.847 0.021 28.5761 0.073 30.945 1.457 1.409 109.09 0.0037 0.04 41.997 1.004 0.023 28.5492 0.073 32.866 1.548 1.495 107.86 0.0027 0.03 57 ABD00048768 Client: Source: Georgia Gulf Silo No. 678 ENTEC Services, Inc. 25 Commerce Ave,-Suite 104-Hucvtown. Alabama 35023 Date: Run No.: 6/30/2000 1 Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 1-7 k 1-8 f,, 1-10 1-11 1-12 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 Delta P 0.24 0.24 0.27 0.27 0.28 0.36 0.38 0.43 0.45 0.61 0.58 0.58 0.57 0.53 0.51 0.48 0.45 0.42 0.38 0.41 0.33 0.24 0.20 0.17 0.39 Sa. Rt. Delta P 0.4899 0.4899 0.5196 0.5196 0.5292 0.6000 0.6164 0.6557 0.6708 0.7810 0.7616 0.7616 0.7550 0.7280 0.7141 0.6928 0.6708 0.6481 0.6164 0.6403 0.5745 0.4899 0.4472 0.4123 0.6160 Delta H 1.08 1.08 1.22 1.22 1.26 1.62 1.71 1.94 2.03 2.75 2.61 2.61 2.S7 2.39 2.30 2.16 2.03 1.89 1.71 1.85 1.49 1.08 0.90 0.77 1.76 Tm In CF) 80 80 81 80 82 81 82 81 82 83 82 83 84 85 85 85 86 86 86 85 85 86 85 84 83 Tm Out CF) 76 76 77 76 75 76 76 76 77 77 76 77 78 78 78 78 79 78 79 79 79 79 78 77 80 Ts TF) 72 72 73 73 74 73 73 74 75 75 74 75 74 74 74 75 76 76 74 74 75 74 75 75 74 58 r ABD00048769 (005 $<5 <> c 0 > O (v r- 0 s\r> 605 sT r- r r- o o _0c5 TO 5 =0*) T5 C TO 2 -- TO .o E U. C2 2o CL A#5 o ( fQA 2 i/' u O r C" o o .05 _ __ 5 =Su. uTO. .2 ^"St 0) U_ 3o TO^ > rof?o 1$ o _* 3E 3__ >TO TO 05 . C '-i r ss EO.X3 N >sfl C cr- o><J^* H (4 rl (V (V f* Ok f-'A V N. fA rA N (4 r d (n r. 51 \dsi sj O 0 |TO <C o | | llQ a)T0O5 S id 05 o = <"\ o'-' o CL > CL > CN CM O CM 82 fA 0 sS po TO 305 (A 2l oo. ^0 fa o TO CD TO 3 W fl- T0O5 f_i oTO ?I CO %CO 0055 TTT5OO =T CM wTO TO 05 .* 2TO -- p~. te r- r EToO. C' r _TO 3 ** O *T 0" vt C* r* r* 9" C> 00 CMJ Cv C" <r- o rP r r* r- <3SH <r "5) cO Qs o TCO ^ il 0 TO w OO --Oo O WA t-MTOM 3fc % % % 3^ l0_) lf_fi fl_fi fwfi C=O to 05 O) 05 05 iS S c c c c o q. a. 05 TS.0 TO \A ^ CM 0 i) p rUo o CUM .1 o d o o o 2 Q_ jO "Uto _ 0 0 0 P N -y c*M) 1a Nu CUM o 20' d o O Z CL 05 <> TO TO TO - a; _TrOo -- 55 TO -- "qj ' % S' jz o <V/\ Va zr \< t?a TO TO -- Cr =cz - sj MOf Vr i/\ (MV d c4 o , J-- ro Vs Vr tM CM P< r* f- r< >1^ *>a|Va --.iQ 1%/* rt r -- "In Oa.-* 52v^. ^Uj 03\ * i- ~c '--M' ss*'. 5 (A ^icnc" <r"s" \a VM 5j . ** <S ** t/* d O r< cJ -Q Sw r- <s> O r1 3 P* \t sC r T j) r- rA r*B o* r cr t~ " ^S* T < Cb La Ci oO LA y d C5 <-J o> c/> Ma pi o O vfsl 3 o o Sis* QTO ar1 % TO Eo I- o JC O Q. oE CL -- cy=> <j- -- H Field Notes: 59 ABD00048770 Client: Source: Georgia Gulf Silo No. 678 ENTEC Services, Inc. 2S Commerce Ave.-Sulte 104-Hueytown, Alabama 35023 Date: Run No.: 6/30/2000 2 Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 1-7 |> ,1--98 1-10 1-11 1-12 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 fc Delta P 0.16 0.18 0.21 0.21 0.28 0.38 0.40 0.51 0.49 0.47 0.45 0.39 0.45 0.50 0.48 0.40 0.35 0.35 0.33 0.29 0.26 0.25 0.21 0.21 0.34 Sq. Rt. Delta P 0.4000 0.4243 0.4583 0.4583 0.5292 0.6164 0.6325 0.7141 0.7000 0.6856 0.6708 0.6245 0.6708 0.7071 0.6928 0.6325 0.5916 0.5916 0.5745 0.5385 0.5099 0.5000 0.4583 0.4583 0.5767 Delta H 0.72 0.81 0.95 0.95 1.26 1.71 1.80 2.30 2.21 2.12 2.03 1.76 2.03 2.25 2.16 1.80 1.58 1.58 1.49 1.31 1.17 1.13 0.95 0.95 1.54 Tm In CF) 86 86 86 87 90 90 90 91 91 92 93 93 93 93 93 95 95 96 98 99 100 100 100 101 93 Tm Out CF) 79 79 80 80 82 83 83 84 84 84 85 85 84 84 84 85 85 86 89 90 91 92 93 93 89 Ts CF) 74 75 76 75 77 77 78 77 76 76 76 76 77 78 79 76 76 77 77 77 78 76 77 77 77 60 ABD00048771 <ODJ CO <5 Q <> 0 **r vS 0" c* ol* o CUtOli p- XZ aj, to ** ? 3 g i 5(0 ID.-- y E cZ X3 E " So CL r r*> -o -JJ r* r- r-'* w 2 o> % 503 l. Q> C..O JO C o U_ ' O U- 3 o o LA CO > cow > u -= Lr> 1 E nI^ c<d a to to to 0) O) o f-Mfl C rp 5? Ore so to n tO to W [CN \0 vQ SO nc sa h2 N R50 to CO 0 CJ CM O CNI 8z o "i|0 5 Ist 1 to 8 <2*o c[1o _j ua) CL --o > v 2 cn % to .* = <> / re 2*1 r \, fc Q. hEo* O3C" si r vJO r- p* l5i o h- Ms ..-2= 0o 0o o rO\ c -r- T- to O) 3c to *> sS a. . *3 CO 0) a cm -*o L. % CO CD o, re 55 2 o coo to _co V C0o _i 0 a*M 6 "gJ 0 Ns d re a X5 -p2 U . N N O to l/ <K s6 pu d pSv> 6 nu 6 a S a f^o* JV'J* PSpr; Luo> J \A .= * -"3T sj f>4 r% N% n% V% l_ i_ l_ k_ to ^ 03 OJ 05 03 iS CC C CO CL CL `S. CL IEEEE aO 0 00 $P 1 *4 & G> P\| = 3 c ^i> & 55 Q 2o _Ero Q- regsi 55 a ? < iiU O % 0) --Q- X(D3 i OL. 2^ a U) v J<r1^ i lr 5c Pit OeKV f" rJ c o 3T Mr a e o a A4 oo o 5S 5^ y C" <y p. W3| P- r-^ H of* La r -Hk" H P* <4 V/' 0 4 o erf 3* (P r- 51 vr Field Notes: 61 ABD00048772 ABD00048773 oTO <50 * 0 4 Q COtz/5) rr \r r- ctr cr r* os 0% o TCOO 5 2S (D II =z .O o ri <-4 C; ooO e 8 m "* d .5 ^ "?- re = U. .S=2 TM U_ II E >ore(S r< d C( 1* y\ O=Kr- nj VO S^ s' *0 a- > NO NO n pri* > 5\c no c< d c( d d ^ V> sD, \9 \J 3? o 0 CO __ > > 0 zr o? LL (A U) <CcO H? 0 *r CreO o CM N O N jc u _ VS/J O .s* -"r E 0 0- go 2 |o SoO J L > 2* 3 CO .* 3 V> gs^r o. HE- 8z c=tnfc IS c- *o rj- cj* ^ c> ^ p* -o -o r- c* c r r r r- r r1>rt- 3- r T*fP f*3 o* % J- 0 n9 3l. ccOn) o0 (0 CO fSA CD eg CD So UI IjuI *= CO 2 .S U- Oz. ^g.sD 0 nrt 2 0 0 /s 5 o o o Q c ls& CO .T1 r-' co o 0 re CL *O 03 |2 rg 5 rJ 2org o. o OG> T- fVook 20 r' TM5 rr c z 3r CM Cl <D % % >- l_ t_ t_ k. "<m0 *y5)003.003.003. 0Q3.*^- 2EEEE C4~ VS $ vi 3 ^jo C^2"> o< r0vIM 1 (0 Ore _Ere Q .ro*e rt CO C=CC< % <O>) D oozr' -- "2,^'j 2 r^ CL lu p=-r5- fsO r -- r/) 6"= o0 s<z r no ;x n r< cnVo [\a 2s CrieCr3o-. <S" r r E^ o-- Cl c ^ Qo. --' K' -.0 o* c* U o 1/ r r O' X* A/> r* 3" 00 r O "5 Lt cr ir lr tv- s' c< sS CM rg 0rfi xo ^ rr r> 2 2 *. - cr Sr5D^- sT <rl X- ff- gr . rr cfl' cr . O' ,d -- r~i r^- \r _^ Field Notes: 63 ABD00048774 679 Silo Baghouse Field Data Sheets ABD00048775 Schematic of Sampling Site Silo Baghouse No. 679 Vent Stack 65 ABD00048776 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 Client: Georgia Gulf Source: Silo No. 679 Job No.: 20148 Data Input By: L. Beane INPUT DATA m^iWmwnth [n>in itr 'nr irumii* nmnnwtob--mmi wimimuniMrawfirmiinri mui iwmin nn r 'iin nikmim--iniiiniMgii---- Run Number Date Time Beqan-Ended Samplinq Time, Minutes 6-29-00 1547-1649 60 2 6-29-00 1709-1811 60 3 AVERAGE 1835-1937 60 IHHBHH 60________ Stack Area. Sauare Feet 0.785 0.785 0.785 Barometric Pressure. Inches of mercurv Stack Pressure. Inches of mercury Pitot Tube Correction factor 30.08 30.01 0.84 30.08 30.01 0.84 30.08 30.01 0.84 30.08 30.01 Meter Correction Factor 0.992 0.992 Nozzle Diameter. Inches 0.250 0.250 peter Volume, Cubic feet Meter Temperature. Deqrees F 33.660 99.1 34.430 99.1 34.000 109.3 34.030 102.5 Avq. Orifice Delta P. Inches of Water Volume H20 Collected. MilliLiters C02 Concentration, Percent 0.91 21.0 0.0 0.91 22.0 0.0 0.89 17.0 0.0 0.90 20.0 0.0 02 Concentration. Percent Avq. Sq. Rt. of Delta P. Inches of Water Stack Temperature. Deqrees F Total particulate collected, qrams 20.0 0.445 85.7 0.0282 20.0 0.445 85.7 0.0187 20.0 0.437 87.4 0.0262 20.0 0.44 86.3 0.0244 CALCULATED DATA Standard Meter Volume. Cubic Feet Standard Water Volume. Cubic Feet Moisture Fraction Molecular Weiqht Of Stack Gas Density Of Stack Gas Averaqe Stack Gas Velocity, Feet/Second Stack Gas Flow @ Stack Conditions, ACFM pack Gas Flow < Standard Conditions. DSCFM Isokinetic Samplinq Rate. Percent Particulate concentration @ Std.Cond..Grains/Cu.Ft. Particulate emissions, lbs per hour 31.758 0.988 0.030 28.4740 0.072 25.504 1.201 1,130 107.88 0.0137 0.13 32.485 1.036 0.031 28.4664 0.072 25.538 1.203 1.131 110.28 0.0089 0.09 31.506 0.800 0.025 28.5325 0.072 25.077 1.181 1.114 108.58 0.0128 0.12 31.916 0.941 0.029 28.4909 0.072 25.373 1.195 1.125 108.91 0.0118 0.11 66 ABD00048777 ENTEC Services, Inc. Client: Source: Georgia Gulf Silo No. 679 MHMBiMHI Date: Run No.: 6/29/2000 Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 1-7 | 1-8 J ,-9 1-10 1-11 M2 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 s C' Delta P 0.10 0.30 0.26 0.25 0.20 0.18 0.19 0.18 0.13 0.27 0.25 0.24 0.20 0.18 0.19 0.15 0.16 0.25 0.20 0.17 0.14 0.12 0.29 0.24 0.20 Sa. Rt. Delta P 0.3162 0.5477 0.5099 0.5000 0.4472 0.4243 0.4359 0.4243 0.3606 0.5196 0.5000 0.4899 0.4472 0.4243 0.4359 0.3873 0.4000 0.5000 0.4472 0.4123 0.3742 0.3464 O.S385 0.4899 0.4449 Delta H 0.45 1.35 1.17 1.13 0.90 0.81 0.86 0.81 0.59 1.22 1.13 1.08 0.90 0.81 0.86 0.68 0.72 1.13 0.90 0.77 0.63 0.54 1.31 1.08 0.91 Tm In m 92 93 94 94 96 96 98 98 100 101 101 101 98 100 100 101 102 104 105 105 105 107 108 108 100 Tm Out (*F) 90 90 92 92 94 94 96 96 96 98 98 98 96 98 98 98 100 102 103 103 103 105 105 106 99 Ts CF) 80 80 82 82 84 84 85 83 87 87 87 87 85 87 88 88 88 87 87 87 88 88 88 88 86 67 ABD00048778 ^ cv cn 3 0 V "S ^ c cc: o CD CD CD CO 2 a.ao.aF- 2EEE N si i) * 4y * \) 1Q5 C' a3: ^ 2 Uj 4$ !> 5^> i s- ^$ QEJ i P *i c o N m a. ao Field Notes: 68 ABD00048779 ABD00048780 O) 2 <9c <3 $ <A (A N *3 V\ U. T r tOo) _c a*, to +c _-- ^2E-Z 2O r* oc < r>r _D5 to ro 5 c i-- k. iT c 3 y oo raj, >> & S' E 20 0 go c 0 |-vS S! ^ s9 NS Id o6 rsj Kjj fs& V \A N Q-- \i\A o f>l IS f\ \a V 0 0 v\ \r >JsJ w *4' V/> \A tvi O \a \r ^A 0w _>> c 0 < cra/J O CM CM O Ol 8z u O @r> to _ 0 |0 3o QO. >o ^ 3 %co Co y fcciSo Cl HE N CS5 H 05 5ft 43c Sflo? fcC* 5C ^ vS K 00 0-0" ho-<M 0 0" c oi 45 il c 0 c-=To-0or0- 0 SJ o) * 3to t"Cfr . TO *3- QOl 2C il a. JC on 2 aM CO 0 to ri to Co io e rJ do A V\ 3 cc PM r- .0 s CM to N N r< do 6 J if c 2 %- C%M C%O %Tf O) D)05O) =itso _c _c c _c o OE- Oc. "Eo. Q. I Z 0. 5 _ E>N o>> < = > > 5U s. 1 N& J> > X ii < s3 Vr 55 Q yro CO 3^ % .oor^< iNi l_L> ( '1 t\ HE (40r- H f .0 Q Q * 5>. Z1 * Q QO > CO Q ''.N Z t- - r *>l r4 r --.aH vi . .<r <# cA cfi CP vn Cl ISJ < ^ K5 V5 to o a,0 05 \A . >31 k rc ^0 0** "ro NWVC C:K^^ I2 r>p~ hrvj p MN *'-\ -fA CM N <j 0- rNHMn PM\y ^5 KS 1y PN vj 0 po5` V0 o0 tM 1a 0 N- r*r ^2 0 S|ti c 33" PA >ar N ^ n!Hr-- pn* 5 c "o pi n CL oc o. s 11-HH4 miT-i "Till 'V cr\ Field Notes: 70 ABD00048781 Client: Source: Georgia Gulf Silo No. 679 ENTEC Services, Inc. 25 Commerce Ave.-Sulte 104-Hueytown, Alabama 35023 Date: Run No.: 6/29/2000 S Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 1-7 k -1--8 f 1-10 1-11 1-12 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 Delta P 0.20 0.15 0.12 0.10 0.31 0.28 0.23 0.19 0.13 0.32 0.26 0.21 0.17 0.11 0.35 0.27 0.22 0.14 0.09 0.11 0.28 0.22 0.16 0.13 0.20 Sa. Rt. Delta P 0.4472 0.3873 0.3464 0.3162 0.5568 0.5292 0.4796 0.4359 0.3606 0.5657 0.5099 0.4583 0.4123 0.3317 0.5916 0.5196 0.4690 0.3742 0.3000 0.3317 0.5292 0.4690 0.4000 0.3606 0.4367 Delta H 0.90 0.68 0.54 0.45 1.40 1.26 1.04 0.86 0.59 1.44 1.17 0.95 0.77 0.50 1.58 1.22 0.99 0.63 0.41 0.50 1.26 0.99 0.72 0.59 0.89 Tm In CF) 108 108 109 109 109 no no no no no no no no in in m in in in m 112 112 112 112 110 Tm Out CF) 106 106 106 106 106 107 107 108 108 108 108 108 109 109 108 109 109 109 no 110 no no no no 109 Ts m 86 86 86 86 87 87 87 87 87 87 88 88 88 88 88 88 88 88 88 88 88 88 88 88 87 71 ABD00048782 rOTeO) lo < 0$ if T* UJ ? to a> c .wC S*f*c re re k re o s 32 H81z| 2o CL 0 OO UtO to Jre? %,_ 5 | 51 =z 0 u. iZ rree Ot?" re -- > >rree- _ 0o re O hj" An 0) to (0 c <(r0e O ore o H Ea 90 iis s re re -id > o 3p/no* OCOM OCM Oo ZTM rwwree a o re re re re *m O) O) o> O) is c cc co O. Q. 'o. O. *" EEEE *\ Vs <r sN5 0 n.22lAr< vr0oi 0/ a a to C _o so d 6 6 i25 CL "re O a SI 0 s " o r< zBo id CL o' O 6 o>> < re re E- _ro- O rree 55 a % r- =re > > >' <5MJ xr>e . 2v wCL A < $ ^5 CO *1 rev, % . O (l N. tA Q * 0 rree <^ nK > Vo ( w v|v Ns* 0 V\ i *0 o t0 0 Va roei i <* s3<5 >s _J__ ^ V* MS rO A va a) 15 Va v> fj v f* Sj\K A ^N5r\ 0 fx . 3iS a .r*e, reiS, Si rCAolsicAoSto^Noo Si CL E re re m = o ? \ \ -to <*0V K.Ql S?8i QC^q 5" 'fr- O o fH cm JZ to O vj > * < Ci V re .VA \A N| Va M N tl 0C^M Va 5$ -1+l+HiH'Hil+htHI'kHHI d o o_ ABD00048783 680 Silo Baghouse Field Data Sheets ABD00048784 Schematic of Sampling Site Silo Baghouse No. 680 Vent Stack 74 ABD00048785 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown. Alabama 35023 Client: Georgia Gulf Source: Silo No. 680 Run Number Date Time Began-Ended Sampling Time. Minutes Stack Area, Sguare Feet Barometric Pressure. Inches of mercury Stack Pressure. Inches of mercury Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter. Inches Meter Volume. Cubic feet Meter Temperature. Degrees F Avg. Orifice Delta P. Inches of Water Volume H20 Collected, MilliLiters C02 Concentration. Percent 02 Concentration. Percent Avq. Sa. Rt. of Delta P, Inches of Water Stack Temperature. Degrees F Total particulate collected, grams Standard Meter Volume. Cubic Feet Standard Water Volume, Cubic Feet Moisture Fraction Molecular WeiQht Of Stack Gas Density Of Stack Gas Average Stack Gas Velocity. Feet/Second Stack Gas Flow < Stack Conditions, ACFM Mack Gas Flow @ Standard Conditions, DSCFM Isokinetic Sampling Rate. Percent Particulate concentration <> Std.Cond..Grains/Cu.Ft. Paniculate emissions, lbs per hour Job No.: 20148 Data Input By: L. Beane INPUT DATA 1 6-29-00 0805-0906 60 0.785 30.02 30.00 0.84 0.992 0.250 32.000 102.60.80 23.0 0.0 20.0 0.4213 76.3 0.0102 29.940 1.083 0.035 28.4231 0.073 23.961 1,129 1,075 106.93 0.0052 0.05 2 6-29-00 0933-1040 60 0.785 30.02 30.00 0.84 0.992 0.250 41.013 90.6 1.36 28.0 0.0 20.0 0.5481 75.0 0.0045 3 6-29-00 60 0.785 30.02 30.00 0.84 0.250 42.280 82.4 1.45 21.0 0.0 20.0 0.5656 72.0 0.0041 CALCULATED DATA 39.260 1.318 0.032 28.4492 0.073 31.165 1.468 1.405 107.28 0.0018 0.02 41.094 0.988 0.023 28.5463 0.074 32.016 1.508 1,465 107.71 0.0015 0.02 AVERAGE ________60________ 30.02 30.00 38.431 91.9 1.21 24.0 0.0 20.0 0.5117 74.4 0.0063 36.765 1.130 0.030 28.4729 0.073 29.047 1.368 1,315 107.31 0.0028 0.03 75 ABD00048786 Client: Source: Georgia Gulf Silo No. 680 ENTEC Services, inc. 25 Commerce Ave.-SuHe 104-Hueytown. Alabama 35023 Date: Run No.: 6/29/2000 WMM4M Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 1-7 k-- 1-8 f 1-10 Ml 1-12 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 Delta P 0.18 0.16 0.22 0.20 0.16 0.17 0.16 0.19 0.16 0.20 0.21 0.19 0.18 0.19 0.16 0.17 0.19 0.16 0.14 0.18 0.17 0.18 0.17 0.18 0.18 Sa. Rt. Delta P 0.4243 0.4000 0.4690 0.4472 0.4000 0.4123 0.4000 0.4359 0.4000 0.4472 0.4583 0.4359 0.4243 0.4359 0.4000 0.4123 0.4359 0.4000 0.3742 0.4243 0.4123 0.4243 0.4123 0.4243 0.4213 Delta H 0.81 0.72 0.99 0.90 0.72 0.77 0.72 0.86 0.72 0.90 0.95 0.86 0.81 0.86 0.72 0.77 0.86 0.72 0.63 0.81 0.77 0.81 0.77 0.81 0.80 Tm In fF) 108 108 108 108 106 104 103 103 102 103 102 102 102 102 102 103 103 103 103 103 103 102 102 103 104 oo j Tm Out fF) 106 106 106 106 104 101 100 100 100 100 100 100 100 100 100 101 101 101 101 101 101 100 100 103 Ts fF) 77 77 77 77 77 77 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 ABD00048787 to o o> o < rN _ u (0 cn _c Vi f* pn/ 3" o 4 Q r O' O j3 E iO 0 o d*l TO>s" > s J P0 Q0 Q 0 <re/> 2 X3 EC i=s 8 31 at _ 5 2 5 r cz cn . ft I'* $ CD w \o \r\ CL otr TO ~ > oTO "'T > 0a ViU > > > >- rfl O ^ r*|rvNr4N ri N rJ ^ r4 ro <o OcTOn CM CM O W oz oo A) si3. fgfl I CL > o o ^o 0- > /0 3 Ho 0~ <r 3 2 Ai CL 0 1 o' gpO g TO CD 3 cn rkf*t uTO CO cant co E* T gu o: cm `t at --^ *> TO 50 $ <a 648 *t> ct> n cn 'X / Sd d a d at 8 00 3 yN TO 3 Q. E 33 o si 0 v> ft sj nS Ms N V *s- r4 t-4p p ^ Pr p" ^ C^ r- IV o ft o ft a o I o _ ft te <D ft|ft Wl ft .coa < ] r- pi S' r- ^ * ft ** o 00, r QC r- cs r < 2oo a --C o o<- o 00 r tt- cam fcot -aa- = Dlc_) Dlc_lcLO.l _LDc.-=ioi Q. DE.QE. QE. 1~ b 00 >al TO 0 Ssi a A A a Z8 CEL 4 o fl 0 D>) < E,, .55' ISb ^ _oro to g^> 2 5 iis2 svj <3V| JD o N <H # o vAl CM cC3r ' 4(l | Vi PQ vj Q TO at' 6o 0. \ t IV Qo_ & A*<& < -- o 0 M oc ra,$l ^Vs ^3 rvSsj ir v" mm ft CN. VJ?* o '4*1^ TO CL Vi Oft f- ftj rs Oft r*- ft 0- Ps ar*J>|;^N o- o 'aQQO E .W ft V o vu. V? N o Vv r^Jotr- -S ~- 0. ToL CL <4 OC re> r-qo TP Q f* *f\Z.^ ft^jcofCK Q0dO& Vo N\o 41S Vfl N PS 0 * r-|tc> m Field Notes: 77 ABD00048788 Client: Source: Georgia Gulf Silo No. 680 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown. Alabama 3S023 Date: Run No.: 6/29/2000 2 Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 1-7 k 1-8 9 ,.9 1-10 1-11 M2 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 k Delta P 0.30 0.32 0.27 0.25 0.35 0.38 0.37 0.33 0.30 0.37 . 0.38 0.32 0.18 0.20 0.27 0.31 0.27 0.36 0.32 0.34 0.30 0.26 0.25 0.27 0.30 Sa. Rt. Delta P 0.5477 0.5657 0.5196 0.5000 0.5916 0.6164 0.6083 0.5745 0.5477 0.6083 0.6164 0.5657 0.4243 0.4472 0.S196 0.5568 0.5196 0.6000 0.5657 0.5831 0.5477 0.5099 0.5000 0.5196 0.5481 Delta H 1.35 1.44 1.22 1.13 1.58 1.71 1.67 1.49 1.35 1.67 1.71 1.44 0.81 0.90 1.22 1.40 1.22 1.62 1.44 1.53 1.35 1.17 1.13 1.22 1.36 Tm In m 87 91 93 94 95 94 94 94 95 94 94 93 93 93 92 92 92 91 91 91 90 90 89 89 92 Tm Out CF) 85 87 89 89 90 91 91 90 91 91 91 90 90 90 90 90 89 89 89 89 88 87 86 86 91 Ts fF) 80 80 79 79 78 76 76 75 75 74 74 74 74 74 74 74 73 73 73 73 73 73 73 73 75 ABD00048789 E 5 W <1 <3 <3 0 * r. j? a^ E < -9 $ V) <r V) (o 3* W <ri tf VI M * </t 8 80 s?C =4 3* Id'S qn m 3co fEl few a. E03 t- = O VJH *M JS ** T><* v fs cJ-1 o o- O' S. ic ^ vP-* mu C >r0-"^ 3? mw* r sas <335* i X /> (A a3 K /) = <- a* $a * A V01 (0 s0 *0 'a _j r a <? a < < <0 X *; JjjiJ8 =2 * lo 2 * r * -r at Q w] ooj & E *" <! _c 0o_ o CL V (t N * c*) <3 4 o o *) "3 4 -o ax a sw*n.^ j* S v *> a v> JS.8 r* v> JX *4 uij c w Hi 4.1l!8 V) Field Notes: 79 ABD00048790 Client: Source: Georgia Gulf Silo No. 680 ENTEC Services, Inc. 2S Commerce Ave,-Suite 104-Hueytown, Alabama 3S023 Date: Run No.: 6/29/2000 3 Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 1-7 fc_____ 1-8 f ,9 1-10 1-11 1-12 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 Delta P 0.21 0.27 0.32 0.35 0.37 0.38 0.36 0.35 0.38 0.34 0.32 0.27 0.20 0.26 0.31 0.35 0.35 0.37 0.35 0.38 0.38 0.34 0.31 0.22 0.32 Sa. Rt. Delta P 0.4583 0.5196 0.5657 0.5916 0.6083 0.6164 0.6000 0.5916 0.6164 0.5831 0.5657 0.5196 0.4472 0.5099 0.5568 0.5916 0.5916 0.6083 0.5916 0.6164 0.6164 0.5831 0.5568 0.4690 0.5656 Delta H 0.95 1.22 1.44 1.58 1.67 1.71 1.62 1.58 1.71 1.53 1.44 1.22 0.90 1.17 1.40 1.58 1.58 1.67 1.58 1.71 1.71 1.53 1.40 0.99 1.45 Tm in rn 86 86 86 85 85 85 85 84 84 84 84 84 84 83 83 83 83 83 82 82 81 81 81 81 84 Tm Out m 84 84 83 83 83 83 82 82 82 81 81 81 81 81 81 81 80 80 80 80 80 79 79 79 82 Ts CF> 73 73 73 73 73 73 73 73 72 72 72 72 72 72 72 72 72 72 71 71 71 71 71 70 72 80 ABD00048791 8 *Qri M(ft (4 r1o0r* PP0 \ft <tj--> s*T O<r<3 0 t* 'n o* a <J 0 <* 4 Field Noles: 81 ABD00048792 687 Silo Baghouse Field Data Sheets ABD00048793 Schematic of Sampling Site Siio Baghouse No. 687 Vent Stack ABD00048794 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 Client: Georgia Gulf Source: Silo No. 687 Job No.: 20148 Data Input By: L. Beane Run Number Date Time Beqan-Ended Samplinq Time, Minutes Stack Area. Square Feet Barometric Pressure. Inches of mercury Stack Pressure, inches of mercury Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter, Inches Pieter Volume. Cubic feet Meter Temperature. Deqrees F Avq. Orifice Delta P. Inches of Water Volume H20 Collected. MilliLiters C02 Concentration, Percent 02 Concentration. Percent Avq. So. Rt. of Delta P. Inches of Water Stack Temperature, Deqrees F Total particulate collected, qrams Standard Meter Volume. Cubic Feet Standard Water Volume. Cubic Feet Moisture Fraction Molecular Weiqht Of Stack Gas Density Of Stack Gas Averaqe Stack Gas Velocity, Feet/Second Stack Gas Flow < Stack Conditions, ACFM ptack Gas Flow @ Standard Conditions. DSCFM Isokinetic Samplinq Rate, Percent Particulate concentration < Std.Cond..Grains/Cu.Ft. Particulate emissions, lbs per hour INPUT DATA 12 6-30-00 6-30-00 0737-0849 0912-1024 60 60 0.785 0.785 30.13 30.13 30.13 30.12 0.84 0.84 0.992 0.992 0.272 0.272 30.860 38.405 97.6 100.1 0.72 0.81 29.0 24.0 0.0 0.0 20.0 20.0 0.4007 73.7 0.4239 75.6 0.0097 0.0072 CALCULATED DATA 29.232 1.365 0.045 28.3182 0.073 22.728 1.070 1,019 93.07 0.0051 0.04 36.224 1.130 0.030 28.4734 0.073 24.057 1,133 1,090 107.78 0.0031 0.03 3 6-30-00 1053-1 159 60 0.785 30.13 1 AVERAGE 60 30.13 30.12 0.272 37.485 100.2 0.80 25.0 0.0 20.0 0.4199 76.8 0.0091 30.12 IHHillHI temmm 35.583 99.3 0.78 26.0 0.0 20.0 0.4148 75.4 0.0087 wmgmamtmS&Z 35.350 1.177 0.032 28.4521 0.073 23.869 1,124 1,077 106.46 0.0040 0.04 33.602 1.224 0.036 28.4145 0.073 23.551 1,109 1,062 102.44 0.0040 0.04 84 ABD00048795 Client: Source: Georgia Gulf Silo No. 687 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hutytown, Alabama 35023 Date: Run No.: 6/30/2000 1 Traverse Point M 1-2 1-3 1-4 1-5 1-6 1-7 k 1-8 f ,, 1-10 1-11 1-12 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 k Delta P 0.15 0.16 0.16 0.16 0.15 0.14 0.15 0.16 0.16 0.16 0.16 0.17 0.14 0.16 0.17 0.17 0.17 0.17 0.16 0.14 0.14 0.18 0.18 0.20 0.16 Sa. Rt. Delta P 0.3873 0.4000 0.4000 0.4000 0.3873 0.3742 0.3873 0.4000 0.4000 0.4000 0.4000 0.4123 0.3742 0.4000 0.4123 0.4123 0.4123 0.4123 0.4000 0.3742 0.3742 0.4243 0.4243 0.4472 0.4007 Delta H 0.68 0.72 0.72 0.72 0.68 0.63 0.68 0.72 0.72 0.72 0.72 0.77 0.63 0.72 0.77 0.77 0.77 0.77 0.72 0.63 0.63 0.81 0.81 0.90 0.72 Tm In rn 100 100 100 100 101 101 101 101 100 100 98 98 99 100 100 100 100 100 101 101 101 101 101 101 100 Tm Out fF) 94 94 94 95 95 95 95 95 95 95 95 94 94 95 95 95 95 95 95 95 96 96 96 96 98 Ts m 73 73 73 73 73 73 73 73 73 74 74 74 74 74 74 74 74 74 74 74 74 74 74 75 74 85 ABD00048796 A $M tf o \r 0) ccs ^ at to ** fill E iE- 2o o. wlw o D> a*. __ I o c|| tizsz IL a Is *3 o<o *- > gw > 3 o > 3 ai 3 3 E t7 c> O i-/i * f0t * fi? 0o 5C oi f" p % 8 o o o oo a ,*3/i <3j) P *1* *2 @yAj og6 ME 52 I t 8 5 ecoi <0 *wu. 5O 0 o =o fl CD -j 0. > CL > NNOSJ Oo O O z C ^ p <r <T ci 0wa5 to 0) a^ IS m2 o CO n to a) .c a Ei_ **! JT u. - CO P2 j* 5 i2S * p*/ cHI Hc-) r* w CL lE- 1 <5* i? p ? m i/) <r cr ~rt r? <V*t itot P Ja*c3r j s3fl385S588 - C 4 o 0- P< j: ` <0 $$ 0 *r I C 0^ ffl o o 5oc o _ c <rr f f- n n v d % % % sfc 3i_ ^ iS_ w iff-l OCBO "325 _ca).gco ca .ac> ios a a. a o.i" 2 E E EE 3 5" E- oi jao (75 5* < % i_ ffl iA 27 o 0 Dc3C E H a S J 4 * i1 i/i j 0 d <C3 0 03 o do r 31 Q& 05 A si 2 s ffl ^ CCg m?* 1*0 4v S 0" ^ J E / }- ^1 >A c o* CL 0. 0 'A 0 0 <3 V] C1 r tf> 0 <r\ J Field Notes: 86 ABD00048797 9 ENTEC Services, Inc. 25 Commerce Ave.*Sulte 104-Huevtown. Alabama 3S023 Client: Source: Georgia Gulf Silo No. 687 hhh mm^mm Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 1-7 k 1-8 f 1-10 1-11 1-12 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 Delta P 0.14 0.17 0.17 0.19 0.19 0.20 0.20 0.17 0.17 0.17 0.18 0.18 0.15 0.17 0.18 0.18 0.18 0.18 0.18 0.19 0.19 0.19 0.20 0.20 Sa. Rt. Delta P 0.3742 0.4123 0.4123 0.4359 0.4359 0.4472 0.4472 0.4123 0.4123 0.4123 0.4243 0.4243 0.3873 0.4123 0.4243 0.4243 0.4243 0.4243 0.4243 0.4359 0.4359 0.4359 0.4472 0.4472 Date: Run No.: 6/30/2000 2 Delta H 0.63 0.77 0.77 0.86 0.86 0.90 0.90 0.77 0.77 0.77 0.81 0.81 0.68 0.77 0.81 0.81 0.81 0.81 0.81 0.86 0.86 0.86 0.90 0.90 HUH METHOD 5 MHHifmMg&gm Tm In rn Tm Out CF) 100 97 100 95 101 95 101 95 101 96 101 96 102 96 102 96 101 97 101 97 102 97 102 97 104 97 104 97 104 97 105 98 105 98 105 98 105 98 105 98 105 99 105 99 105 99 106 100 Ts CF) 75 75 75 75 76 75 75 75 75 76 76 76 76 76 76 76 76 76 76 76 76 76 75 76 0.18 0.4239 0.81 103 100 76 ABD00048798 M NNOS oOOqZ c^r JOjr'o^ 1L ,, I IP V/l N \A V\ tlr (0 CQ J= at CD -- -- 51 ill 5 111 - z a2 O * u $?? <h (0 a> *t 5 a> l! J LL c d = d ss 3O a >> % I I @0 6C s I " ill Jfi Jo o n0 ^0 0s* > Q. > . 5 n >5 *oc E o n ffl ta3o <--* 0 S' CJ 55 M 0C9 *t: *N 2 $ 2 ; % 3 0 fl E 1o _ac > go. c 0 0c5 jTA\ I-9 8 C -- * r 2 o > ^ <t it ft LL to j* 2& re 2 r c* a. E t- 5 o3 r i/ JtT!tfol" rrr & v/i t/) to 5! B ?? <r fl ip si . a in 83 * rt> 4 01 r fl to U) '/I 1 ft fts Cr .o ns 3 4) \C v 3 S r3 r3= <T O' er Cr Cr* 0c<Jr^0r0 0 o 1! ^ 2 o Iv o 2 18$ 00 <$* cr o* o0 s<* s* 0o o 5? 0o H ooco C T- -T-c'jrs'T ffl % % & w. l_ ^ i_ u n 3 %g 0c9 _0c9 ac _ac "3ios 0.0.0. o.12 EE E E -- ft r % n>U "`n a. 0 o Q 09 I E. a* U %2 --A W 111) c HJS dc 3 *4 V > II Oa. 0^ XsoJ at <r $ n0 r* r r Cx V1 r 0 c o d0Q 0 0 oo;oo ; vs d P<cri -UM> CL c o CL ol d$ Field Notes: ABD00048799 Client: Source: Georgia Gulf Silo No. 687 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown, Alabama 3S023 Date: Run No.: 6/30/2000 3 Traverse Point M 1-2 1-3 1-4 1-5 1-6 1-7 t 1-8 * v9 1-10 1-11 1-12 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 fe Delta P 0.16 0.18 0.18 0.18 0.19 0.19 0.17 0.17 0.17 0.18 0.20 0.19 0.10 0.14 0.18 0.18 0.17 0.17 0.19 0.19 0.20 0.20 0.19 0.18 0.18 Sa. Rt. Delta P 0.4000 0.4243 0.4243 0.4243 0.4359 0.4359 0.4123 0.4123 0.4123 0.4243 0.4472 0.4359 0.3162 0.3742 0.4243 0.4243 0.4123 0.4123 0.4359 0.4359 0.4472 0.4472 0.4359 0.4243 0.4199 Delta H 0.72 0.81 0.81 0.81 0.86 0.86 0.77 0.77 0.77 0.81 0.90 0.86 0.45 0.63 0.81 0.81 0.77 0.77 0.86 0.86 0.90 0.90 0.86 0.81 0.80 Tm In CF) 101 101 101 102 102 102 102 102 102 102 102 103 104 104 105 106 106 106 107 107 107 108 108 108 104 Tm Out CF) 94 93 93 93 94 94 95 95 95 95 95 95 96 97 96 97 98 98 99 100 99 99 100 100 100 Ts rn 76 76 76 75 77 77 77 77 77 77 77 78 77 77 77 77 77 77 77 77 77 77 77 77 77 ABD00048800 % 1 iq o > m 09 O O I4 C3 00 a <0 i 4 Tlri co >* CO V CD o NNO OOo o 0 1 SsiJliS S?5^Il Qj c o .3 a. > Q- > I 0011 a2 A1 Sto (ft - old M o1 CD 55 nOot CacA> o CO K 1_ * s* u- \S\ ]S* \ <S t- O <yr 5c 0A r r r c r r- r r F`: Xc r r a,ir <T <3 M<y lx <r >X <r *X <X2TCJ- <y ? As A> r -s-^r aaoa S t o 3 J- 1 2nooc ^o,r. & 3t-t 5cvt no ^% 3 "S In oi o> a> ai 2 % = == P a. a. a. a. r~ 2 E EE JJ *9* r' * <s Ts Z L 09 ttI. 2a fLf)l 2* -- 55 2 U) 2 ii \ dl s & 3\ I"5 10 4 CO a J % 53 ts S VI V o^ o ai vjl tjg| o4 C v r- Q 0 C (COO r S S 12 o 6o - oct> c nsS*c5ar "r ri jj v> <9 <T S * .4 'jjl 0 3 90 90 JB O' H* <8 o K) CL aO. i/) $4 <0 v 3 3 Iff .pc cr fl - ti ^3 N Field Notes: 90 ABD00048801 688 Silo Baghouse Field Data Sheets ABD00048802 Schematic of Sampling Site Silo Baghouse No. 688 Vent Stack 92 ABD00048803 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 m PARTICULATE EMISSIONS CALCULATIONS iwawSia Client: Georgia Gulf Job No.: 20148 Source: Silo No. 688 Data Input By: L. Beane fwahiiw'i mniirMBrug imfllMdi in mjjiir i ~.i.'iuwT>iffi~iiiiri#iirTiTiii i i 'wuriaf <w * ii^iniMiTinTi^riifcwwMii *mjli**MM*rf^rfThTi<ri'`iiiinniB(iwwii INPUT DATA "'Tr'inni 'rpTiWH'iVii't^M' v |T,~|iiiri''i|iffrv(ir<(riignii'~m ~ t1 n~Tjfi~ti'^iiiBiiif7wiipi>ipni>iiWiiiiJMiBiHrai Run Number 1 2 3 AVERAGE Date Time Beqan-Ended 6-30-00 1237-1339 6-30-00 1400-1505 1525-1631 mSSS Samplinq Time. Minutes Stack Area, Square Feet 60 0.785 60 0.785 60 0.785 60 . . ... t Barometric Pressure. Inches of mercurv 30.13 30.13 30.13 30.13 Stack Pressure. Inches of mercury Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter. Inches Peter Volume. Cubic feet 30.10 0.84 0.996 0.250 39.310 30.10 0.84 0.996 0.250 36.265 30.10 0.84 0.996 0.250 39.305 30.10 i 1 r\ -! __ i 38.293 Meter Temperature. Deorees F 103.0 101.8 126.7 110.5 Avq. Orifice Delta P. Inches of Water 1,41 1.20 1.40 1.34 Volume H20 Collected, MiliiLiters C02 Concentration. Percent 34.0 0.0 34.0 0.0 35.00 0.0 34.3 0.0 02 Concentration. Percent 20.0 20.0 20.0 20.0 Avq. So. Rt. of Delta P. Inches of Water 0.586 0.539 0.585 0.57 Stack Temperature, Deqrees F 80.3 80.0 79.3 79.8 Total particulate collected, qrams 1 tifflfirmmisyriafM " 0.0085 CALCULATED DATA 0.0126 0.0143 0.0118 mamnr mwimm }^g*umctmrsa 1 Standard Meter Volume. Cubic Feet 37.089 34.269 35.587 35.649 Standard Water Volume, Cubic Feet 1.600 1.600 1.647 1.616 Moisture Fraction 0.041 0.045 0.044 0.043 Molecular Weioht Of Stack Cas Density Of Stack Cas 28.353 0.0724 28.318 0.0723 28.322 0.0724 28.331 0.0724 Averaqe Stack Gas Velocitv. Feet/Second frack Cas Flow @ Stack Conditions, ACFM Pack Gas Flow @ Standard Conditions, DSCFM 33.470 1,577 1.486 30.783 1,451 1.363 33.406 1.574 1.481 32.553 1.534 1,443 Isokinetic Samplinq Rate. Percent 95.86 96.59 92.26 94.90 Particulate concentration @ Std.Cond..Grains/Cu.Ft. Particulate emissions, lbs per hour 0.0035 0.04 0.0057 0.07 0.0062 0.08 0.0051 0.06 93 ABD00048804 Client: Source: Georgia Gulf Silo No. 688 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Date: Run No.: 6/30/2000 1 Traverse Point 1-1 1> 1--2 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.19 0.29 0.33 0.45 0.50 0.S1 0.16 0.27 0.30 0.37 0.45 0.42 0.35 Sa. Rt. Delta P 0.4359 0.5385 0.5745 0.6708 0.7071 0.7141 0.4000 0.5196 0.5477 0.6107 0.6708 0.6481 0.5865 Delta H 0.76 1.16 1.32 1.80 2.00 2.04 0.64 1.08 1.20 1.49 1.80 1.68 1.41 Tm in CF) 104 105 106 107 107 107 106 106 107 107 107 107 106.33 Tm Out CF) 97 99 99 100 100 100 99 100 100 100 101 101 103.0 Ts CF) 81 81 80 80 80 81 80 80 80 80 80 80 80.3 ABD00048805 re> < \ (L r f 0 C. % to ** TluO uj --. -- S1SI3 = ^Z o o. W In fb < \ $rr 6 _<o -S5 3*fc U. to re 5 | c ir H c Q) U. _0 oTO 4 > OTO _0 > 3E re tO > Oo TO |o) !rH 35 5 \jA r'/MICD* M] Cr-t/V4 _>N TO -- C < H (T0O o CJ N O N 8z 1 SI I !?! o W o = o -J CL > Q- > S %P5 I- "3 0 O' TSO r/ u TO E2 TO CQ ^ oTO c/5 (0 0c3 OXTT3OO' w TI % TO JJ to oo y 5rwe S3TO oO ^OO ?? 3,,$ Ig f*a 2 CL i%-C%NCO^*T ^TO LTO. IT_O Tl_O Tl_O -<=0 BS C__03 03 03 03 .3 CL 'CL Q. Q. EEEE oj oQ /I 4} TO TO E JQS rue w * fl VJ r\ ^ 1 O>) < %_TO V" TO l*J 0 % 'I cr r*i r rce LL J* 5T o* . -D * ft CL 4 3 ^ TO "3 re wG Xc3 TO E (- fii* cr 0 J11r J21 0 1? <3 01 J c o W) In $ rt*l> n Q_ n o CL "i Field Notes: 95 ABD00048806 Client: Source: Georgia Gulf Silo No. 688 ENTEC Services, Inc. 25 Commerce Ave.-Suitt )0<-Hueytown, Alabama 35023 Date: Run No.: 6/30/2000 2 Traverse Point 1-1 k 1-2 f ,.B 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.21 0.27 0.30 0.42 0.50 0.44 0.19 0.31 0.37 0.20 0.17 0.21 is*!** 0.30 Sa. Rt. Delta P 0.4583 0.5196 0.5477 0.6481 0.7071 0.6633 0.4359 0.5568 0.6083 0.4472 0.4123 0.4583 0.5386 Delta H 0.84 1.08 1.20 1.68 2.00 1.76 0.76 1.24 1.48 0.80 0.68 0.84 1.20 Tm In CF) 102 104 105 105 105 10S 106 105 105 105 105 106 104.83 Tm Out CF) 96 98 98 99 99 100 100 99 99 99 99 100 101.8 Ts TF) 81 81 81 80 80 80 80 79 80 80 79 79 80.0 ABD00048807 O U) a2 0 GV > < 0 U- l/> i3 r.P* Tp(c r -- 0 0 rti r t 'Tr3t (0 1 0 e iO >ro rO0| q 0 oo 0 jto i/> <$4 `ii a SO (rAe O OO O o Z c ^ - Ift 0 1/ O> rtJl Tb ^ xXi c t-o *t <tl H) 2.* T32S 0^(0 G ' Q. E G S< ^ | jJ W 5^ 0" V J 23 flr 3 ro , o '/ <r^ I C/3 Sfc IKS * 5 r gs od :G= oOOo o & r t- c%m n?= 5t? Gcct> Goc> .oc _O= *ioS= *r> V "a, *G. H" EEE ft o O' 41 , > i s <3 t* .3 * 3 $ 0 \ a rfl J) 4 G' L 03 0 C/3 G fb w "o e0 \/ma 4 ^ D0 1 </] S fl W 7 o - <> o. flj < |^ lg l\A '/ ? J 0 -. 40 0 0i ftlO' rO' V) r c( G (A Q </) ^^6 2! 0>|j-|-|'n|^^ o CL ^ <6 "0 o CL I Kl I Field Noles: 97 ABD00048808 Client: Source: Georgia Gulf Silo No. 688 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown. Alabama 3S023 Date: Run No.: 6/30/2000 3 Traverse Point 1-1 k> ,1--a2 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.21 0.25 0.30 0.38 0.42 0.49 0.17 0.29 0.41 0.44 0.47 0.37 wMmmSmm 0.35 PARTICULATE FIELO DAT Sa. Rt. Delta P 0.4583 0.5000 0.5477 0.6164 0.6481 0.7000 0.4123 0.5385 0.6403 0.6633 0.6856 0.6083 Delta H 0.84 1.00 1.20 1.52 1.68 1.96 0.68 1.16 1.64 1.76 1.88 1.48 Tm In <*F) 104 104 103 104 105 105 105 106 105 105 105 105 0.5849 1.40 104.67 W '''' Tm Out CF) 98 97 98 699 99 99 100 99 99 99 99 98 'P^:''^''' Ts CF) 79 79 80 79 79 79 79 79 79 79 80 80 126.7 79.3 98 ABD00048809 0CD3 5C S < -0 \t oc> C jfc CcOo a> k s 9 5 y &SZ 9 2 Q2. u i. ra r wQ) =U. cc 2 IT s* 0 0 > - *p i Uw G Q oCD f--r ! > _ra \iAj o *A Ks -a V) 7 T) i? '7 <3 7> >. CD _ SQ oCD oNOoWz 'ti <Ha .oO<CD Tca>o _CmJD 0O_.} > o. -*i S0 In o mCD !!<q 1 If 0 CL > %CO 5(0 *1 _COcO) TOC0OD)' CM cCOj co kJ o PS o o O r % n%n% '%T l- i_ l_ k_ <0 0) <13 0) 0) = 03 O) 03 03 is _C C JO C O a a a D.I" E EE _ ,0 CO a> AV CO _i. 0 n2 Oro -- N-- o Z CL Sa3 0>3 < 33 % <s ir c z ijj O CO ^ 3 9(D Ir w0 0r1 So. w E 03 jjf'4 CL 2? CTl PE 0" 9" <f $ 0 *i cd .^ (0 '/I \fi ? Go s ** Ml 8X ft di ?so< A 0- ^ ** 00 Ss*0) TD ^ fl vo CO S cc 0 Field Notes: 99 ABD00048810 No. 10 Cyclone Dryer Field Data Sheets ABD00048811 No. 10 Cyclone Dryer Sampling Port Information Stack Diameter: 55" diameter Stack Area : 16.499 Square feet Stack Height: Approx. 150 feet Test Port Data: A. Diameter: 4 inches B. Upstream Disturbance (L/D): 6.55 C. Downstream Disturbance (L/D): 7.21 Number of Traverse Points: Minimum Number of Traverse Points Required: 101 ABD00048812 ENTEC Services, inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 PARTICULATE EMISSIONS CALCULATIONS Client: Georgia Gulf Job No.: 20148 Source: No. 10 Cyclone Dryer Data Input By: L. Beane Run Number Date Time Began-Ended SamDlina Time. Minutes Stack Area. Sauare Feet Barometric Pressure. Inches of mercury Stack Pressure. Inches of mercury Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter. Inches Pieter Volume. Cubic feet Meter Temperature, Degrees F Avg. Orifice Delta P. Inches of Water Volume H20 Collected. MilliLiters C02 Concentration. Percent 02 Concentration. Percent Avg. Sa. Rt. of Delta P. Inches of Water Stack Temperature. Degrees F Total particulate collected, grams INPUT OATA wtmma&Mwmm 1 6-14-00 1737-1843 60 16.499 30.08 ]ir IfTH'0 llflir lii tfWMIlf MUlCI11|'| W 2 6-14-00 1905-2012 60 16.499 30.08 IIMIWItltfli'i'Ilf'BIHil'H 3 AVERAGE 6-14-00 2025-2132 wnfim 60 16.499 60 MMHH 30.08 30.08 30.02 0.84 0.996 0.200 52.750 30.02 0.84 0.996 0.200 54.300 30.02 0.84 0.996 0.200 53.710 30.02 mpi lip fjBjBPH 53.587 83.0 1.90 172.4 0.0 20.0 1.310 106.4 76.5 2.02 135.6 0.0 20.0 1.354 105.3 76.1 1.91 145.2 0.0 20.0 1.315 105.0 78.5 1.94 151.1 0.0 20.0 1.33 105.5 0.0151 0.0652 0.0205 0.0336 CALCULATED DATA 1 Standard Meter Volume, Cubic Feet Standard Water Volume. Cubic Feet Moisture Fraction Molecular Weight Of Stack Gas Density Of Stack Gas Average Stack Gas Velocity, Feet/Second Stack Gas Flow @ Stack Conditions, ACFM tack Gas Flow < Standard Conditions. DSCFM Isokinetic Sampling Rate. Percent @Particulate concentration Std.Cond..Grains/Cu.Ft. Particulate emissions, lbs per hour 51.578 8.115 0.136 27.332 0.0664 78.078 77.293 62.446 104.13 0.0045 2.41 53.756 6.383 0.106 27.654 0.0673 80.229 79.421 66,509 101.89 0.0187 10.65 53.192 6.835 0.114 27.570 0.0671 78.037 77.252 64,162 104.51 0.0059 3.26 52.842 7.111 0.119 27.519 0.0669 78.781 77,989 64,372 103.51 0.0097 5.44 102 ABD00048813 Client: Source: ENTEC Services, Inc. 25 Commerce Avc.-Sulte 104-Huytown. Alabama 35023 Georgia Gulf No. 10 Cyclone Dryer Date: Run No.: 6/14/2000 1 Traverse Point 1-1 1-2 1-3 1-4 1-5 k> ,1--76 1-8 1-9 M0 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 Delta P 1.00 1.70 1.90 1.80 1.80 1.90 1.80 1.90 1.90 1.80 1.50 1.50 1.50 1.60 1.70 1.70 1.70 1.80 2.00 2.00 wmmmim 1.73 PARTICULATE FIELD DATA. METHOD 5 nm Sa. Rt. Delta P 1.0000 1.3038 1.3784 1.3416 1.3416 1.3784 1.3416 1.3784 1.3784 1.3416 1.2247 1.2247 1.2247 1.2649 1.3038 1.3038 1.3038 1.3416 1.4142 1.4142 Delta H 1.10 1.87 2.09 1.98 1.98 2.09 1.98 2.09 2.09 1.98 1.65 1.65 1.65 1.76 1.87 1.87 1.87 1.98 2.20 2.20 Tm In rn 92 86 86 85 85 85 84 83 83 83 82 82 82 82.00 82.00 82.00 82.00 80.00 80.00 80.00 1.3102 1.90 83.30 Tm Out m 91 87 87 86 85 85 84 84 84 83 82 81 81 80.0 80.0 80.0 80.0 78.0 78.0 78.0 83.0 ts rn 106 106 106 107 106 107 106 106 107 107 106 107 106 106.0 107.0 106.0 107.0 106.0 106.0 106.0 106.4 103 ABD00048814 Wa"" s u: K ? tr r3 Q U- 3* r* T d 05 .C a*. to 45 CO _ -- s gss 5 |iz c2 2o Nfl rJ / 0 sj r* l/ tr rJ 0 0 6 2 2* % -- TO ^ to 2 TS $ TO C S | L*> =u_ Q. C 4 c i 3O I f >oTO 00 si v* 0 > U 0 0 0 N1' OD l 05 fsk <>e N.4J W sj 'O rW sX *1> S0| 4 fA s-OkO ts vi >45 J isg) 0 u<D JV>) <r CcO <CCOO o CM N ft (N OOo2 O jn SA rv 5" C\* LLP'1 <,rT C***. r< <0 .ra=0oo00,* , %e%g %co T4f 2^ fbf.l 0w) fwfl w) CO 05 05 05 05 .2 sO a&aa&a.Er-o ^ E E S tir "i V0 AX J? S'J O t-- CO 1 >-- TO ,2 > iS l-n 4o 11 5 ffi oQ iloc. > -i Qtoo. >.5o2 o oV.4 2 3(0 CO ay 0 lo oftft <5 CD CD 3 CO CO cA| Q.C* o' iSI CO CO t0co5 OTTOO >r0Ji5. ^l_ . Jr a <T *8 13 ns to 2, | So s * .5 76 O J js 4 CO_ hJ , o> S C\ Q z a^ 05 E oj:*t/) u Sl/> 0 ^ CO 1 * sUi % <* g sr c z JT3O 0 >^ Q. o-' E7 8^. a \r\ \\ 2 c- t3r E pe C A o> =n u . <0/5 5TO -Sd-Oo Q. w- E S5 ^3 c- ^ 0% 4 joc1<"C >J c C" c er 5 - <0 O' if C >3 S5 ^ 0 Ha r- sO, w .c o V* a? < < r< -- r V. a-* O n oO o o*<f& p 4: 0 _ ~TOvJD'jv 'Jv O r- m o V/5 o o cV A O f 5^rrafTz E sj Q- ri r< <S h ^O fs"' Co" ^ V T 3H ly^l \s ttb^iyddJddibty ro a Field Notes: 104 ABD00048815 Client: Source: ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown. Alabama 35023 Georgia Gulf No. 10 Cyclone Dryer Date: Run No.: 6/14/2000 2 Traverse Point 1-1 1-2 1-3 1-4 1-5 k _1i6___. f 1-7 1-8 1-9 1-10 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 impgiHpjMpmi Delta P 1.50 1.70 1.80 1.80 1.90 1.80 1.80 1.80 1.90 1.90 1.70 1.90 1.80 1.80 1.80 1.90 2.00 1.90 2.00 2.00 1.84 Sa. Rt. Delta P 1.2247 1.3038 1.3416 1.3416 1.3784 1.3416 1.3416 1.3416 1.3784 1.3784 1.3038 1.3784 1.3416 1.3416 1.3416 1.3784 1.4142 1.3784 1.4142 1.4142 1.3539 Delta H 1.65 1.87 1.98 1.98 2.09 1.98 1.98 1.98 2.09 2.09 1.87 2.09 1.98 1.98 1.98 2.09 2.20 2.09 2.20 2.20 2.02 Tm In rn 75 75 75 75 75 75 75 78 77 77 79 80 81 81.00 81.00 81.00 81.00 80.00 81.00 81.00 78.15 Tm Out rn 75 75 75 75 75 75 75 74 74 74 74 75 75 75.0 75.0 75.0 75.0 75.0 75.0 75.0 76.5 Ts CF) 107 105 105 106 105 106 105 105 105 105 105 105 105 105.0 105.0 105.0 106.0 105.0 105.0 105.0 105.3 105 ABD00048816 o > 0) OC) S- `O.N0 o o0 'Jj *j ^ 0 Sj *^sJJ Is* no <>> sX '4) /l k0 sO ^Oj d c Xfi o<% & o u rc CO 3 .o* r* ISs Q. 1 r tn r ^ rr rHC \r* Vo -^/* um r r-r pr rr rn o_ (Prf 0< see / Mlo Q) E k J> g 1 z\f.Zn p-; <h S t/r3} vf4^ C s!'* ?p L* ajk-jj O Q_ <-> k* cyN e . cS --L* P ;r V r- rf H Field Notes: 106 ABD00048817 Client: Source: ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueyiown, Alabama 35023 Georgia Gulf No. 10 Cyclone Dryer Date: Run No.: 6/14/2000 3 Traverse Point 1-1 1-2 1-3 1-4 1-5 fc______ 1-6 f ,7 1-8 1-9 1-10 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 PUPlis liiiifla Delta P 1.50 1.50 2.00 2.00 2.00 1.90 1.90 2.00 1.80 1.90 1.40 1.50 1.60 1.70 1.70 1.70 1.60 1.70 1.70 1.60 1.74 PARTICULATE FIELD DATA. METHOD 5 Sa. Rt. Delta P 1.2247 1.2247 1.4142 1.4142 1.4142 1.3784 1.3784 1.4142 1.3416 1.3784 1.1832 1.2247 1.2649 1.3038 1.3038 1.3038 1.2649 1.3038 1.3038 1.2649 Delta H 1.65 1.65 2.20 2.20 2.20 2.09 2.09 2.20 1.98 2.09 1.54 1.65 1.76 1.87 1.87 1.87 1.76 1.87 1.87 1.76 Tm In m 76 76 77 78 78 78 78 79 79 80 78 78 78 78.00 78.00 78.00 79.00 81.00 82.00 82.00 1.3153 1.91 78.55 Tm Out fF) 75 74 74 74 74 74 74 74 73 73 73 73 73 72.0 73.0 74.0 74.0 74.0 74.0 75.0 76.1 Ts CF) 105 105 105 105 105 105 105 105 105 105 105 105 105 105.0 105.0 105.0 105.0 105.0 105.0 105.0 105.0 107 ABD00048818 v fa> a Q- a 0 r% io (0 CcT r. * co ** CO -- r= _ 5 32it |i^| Aw 2o a. 5> r-0 r ^sfi(o0 IA CO o> l- co .2 -s 5 2= S | ff*- LL -- oo 0 ovO C0._A OO ^ SoLr-. H- {* > co 03 CO >\ so i< CO CO CD CMNQCM Oo O o Z g 2 3 |q CD S Oft J D. > J s %CO a) ctoo co (L^ o > I3 t*- CO Sjp rJ ftT *- o' |tv\ CO CD Din: o0 w-I* Ci U 91 C=Ol. n U-3- SCcO oo*- oo o * -- s 1 1 <1V) V Os 1 2 od d o d 52 ^ s i. <d 0 d d 6 o' Cl &O s' sfi 8 *r SS| IT c 2 % ?CfMc %M J CO .. 03 05 03 03 i2 5 = = C C P " Q. Q. Q. a H* s EEEE o 5 vO ij.* o E. joqM 55 OJ jo >ro 0 o.^.: O ^ 2^EViJ 0.U,^J M _os -r 3co-S 55^ Q c3e(lA ft S |o > 00 0 o o <akcM|vo kl 0 0O VO'sD sis. f-o I* \oft I*'*' 2^^ vD r-tfJ ^kb ^ SO sQ s0 oc>r-0_ k 3" cJ b1* -h0 ijh c^n i-gu iss a. E ^3 . T r -sio- r 3-JJ Luu Va ^ \/ c TT 3- ^ Sfi *je r r* ye *o isu 0 ft ttl So if a- \f* vS)rr >Qc- D >0 $$> D.0 < c< 00 Q Q| cfl o nJ C* vflcr 03 Va < ^r p r crfr1? <1 <Jl<H j -ffir, t^tn co r> po _ h^sS'f------- -- r< tS) V v Q. -- rO c Ho Q_ sac ddfttydJdddJndr. IMI Field Notes: 108 ABD00048819 No. 11 Cyclone Dryer Field Data Sheets ABD00048820 No. 11 Cyclone Dryer Sampling Port Information Stack Diameter: 55" diameter Stack Area : 16.499 Square feet Stack Height: Approx. 150 feet Test Port Data: A. Diameter: 4 inches B. Upstream Disturbance (L/D):6.55 C. Downstream Disturbance(L/D): 7.21 Number of Traverse Points: Minimum Number of Traverse Points Required: no ABD00048821 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 Client: Georgia Gulf Source: No. 11 Cyclone Dryer Job No.: 20148 Data Input By: L. Beane Run Number 1 23 Date 6-14-00 6-14-00 6-14-00 Time Beqan-Ended 0956-1 102 1140-1250 Samolinq Time. Minutes 60 60 60 Stack Area. Sauare Feet 16.499 16.499 16.499 Barometric Pressure. Inches of mercurv 30.08 30.08 30.08 Stack Pressure. Inches of mercurv 30.04 30.04 30.04 1 Pitot Tube Correction factor 0.84 0.84 0.84 Meter Correction Factor 0.996 0.996 Nozzle Diameter, Inches 0.200 0.200 Peter Volume. Cubic feet 49.860 52.160 49.560 Meter Temperature. Dearees F 112.0 95.1 95.0 Ava. Orifice Delta P, Inches of Water 1.71 1.78 1.60 Volume H20 Collected. Milliliters 162.2 172.5 120.6 C02 Concentration. Percent 0.0 0.0 0.0 02 Concentration, Percent 20.0 20.0 20.0 Ava. Sq. Rt. of Delta P. Inches of Water 1.240 1.269 1.202 Stack Temperature. Dearees F 106.5 106.4 106.8 Total particulate collected, qrams 1 m mi mi.......... .. 0.0174 0.0210 0.0174 mwmmmfcam! j M.iWi--riBiu CALCULATED DATA AVERAGE 60 30.08 30.04 50.527 100.7 1.70 151.8 0.0 20.0 1.24 106.5 0.0186 Standard Meter Volume. Cubic Feet Standard Water Volume, Cubic Feet Moisture Fraction Molecular Weiqht Of Stack Gas Density Of Stack Gas Averaqe Stack Gas Velocity. Feet/Second Stack Gas Flow < Stack Conditions. ACFM Rack Gas Flow < Standard Conditions. DSCFM Isokinetic Samplinq Rate. Percent Particulate concentration <3> Std.Cond..Grains/Cu.Ft. Particulate emissions, lbs per hour 46.258 7.635 0.142 27.270 0.0662 73.980 73.236 58.805 99.17 0.0058 2.92 49.880 8.120 0.140 27.288 0.0663 75.747 74.985 60.338 104.22 0.0065 3.35 47.379 5.677 0.107 27.644 0.0671 71.308 70,590 58.939 101.34 0.0057 2.86 47.839 7.144 0.130 27.401 0.0666' 73.678 72.937 59.361 101.57 0.0060 3.04 111 ABD00048822 Client: Source: ENTEC Services, Inc. 2S Commerce Ave.-Suite 104-Huevtown, Alabama 35023 Georgia Gulf #11 Cyclone Dryer Date: Run No. 6/14/2000 1 Traverse Point 1-1 1-2 1-3 1-4 1-5 fc 1-6 f ,.7 1-8 1-9 1-10 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 Delta P 1.20 1.20 1.50 1.60 1.70 1.70 1.70 1.80 1.80 1.90 0.70 1.10 1.50 1.90 1.60 1.60 1.60 1.50 1.70 1.80 1.56 Sa. Rt. Delta P 1.0954 1.0954 1.2247 1.2649 1.3038 1.3038 1.3038 1.3416 1.3416 1.3784 0.8367 1.0488 1.2247 1.3784 1.2649 1.2649 1.2649 1.2247 1.3038 1.3416 1.2404 Delta H 1.32 1.32 1.65 1.76 1.87 1.87 1.87 1.98 1.98 2.09 0.77 1.21 1.65 2.09 1.76 1.76 1.76 1.65 1.87 1.98 1.71 Tm In CF) 88 92 91 91 92 92 92 94 97 97 94 93 94 93.00 93.00 96.00 95.00 96.00 95.00 95.00 93.50 Tm Out CF) 88 888 88 88 89 90 90 91 91 91 91 91 92 92.0 92.0 92.0 91.0 92.0 92.0 92.0 112.0 Ts fF) 106 107 106 106 107 107 108 108 105 105 105 106 107 108.0 107.0 106.0 106.0 106.0 107.0 106.0 106.5 112 ABD00048823 * io 0 0 0 0 0 0 0 Q 0 Nfi SJ si 'i s( 0) C09 S\ i'" P0** sA s( \0 a0 sip: k* N0 xO nC g? O r> c*rJ 2CO iSjM 0) w Cl E Q) K 4 <s 5 <5 CO, :o 2 .nij\ SS o 39 y 0<j0 fC " r p C-vO 0 oo _t>d -9l p> d $ .0 a <* 3" <r cs sj <V oC QO Field Noles: tO I Q. --I 113 ABD00048824 Client: Source: ENTEC Services, Inc. 2S Commerce Ave.-Suite 104-Hucytown, Alabama 35023 Georgia Gulf #11 Cyclone Dryer Date: Run No.: 6/14/2000 2 Traverse Point 1-1 1-2 1-3 1-4 1-5 k> ,1.-76 1-8 1-9 1-10 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 Delta P 1.00 1.60 1.70 2.00 1.60 1.60 1.70 1.70 1.80 1.80 1.50 1.30 1.60 1.50 1.60 1.60 1.70 1.90 2.00 1.20 HNI 1.62 Sa. Rt. Delta P 1.0000 1.2649 1.3038 1.4142 1.2649 1.2649 1.3038 1.3038 1.3416 1.3416 1.2247 1.1402 1.2649 1.2247 1.2649 1.2649 1.3038 1.3784 1.4142 1.0954 1.2690 Delta H 1.10 1.76 1.87 2.20 1.76 1.76 1.87 1.87 1.98 1.98 1.65 1.43 1.76 1.65 1.76 1.76 1.87 2.09 2.20 1.32 1.78 Tm In m 93 93 94 96 96 96 96 97 96 96 97 97 97 99.00 99.00 99.00 100.00 99.00 99.00 99.00 96.90 Tm Out m 92 92 92 92 92 92 92 92 92 92 93 94 94 94.0 94.0 95.0 95.0 95.0 95.0 95.0 95.1 Ts (*F) 106 107 108 106 108 107 106 108 107 108 104 105 106 107.0 106.0 107.0 105.0 105.0 106.0 105.0 106.4 ABD00048825 0) o o |y l/-| i- > c< 33OE , o0 Co -J SO 4 xjsd Ol HU 0) Q.sfi E VO 4 4 VO L/\ ^ \jy \j V* La ^ 4 sfi s9 Lr* c0 Su Ort u. (0 8*tf c tfi isC po 0QL_). CO " HE0) %A o <r So 3" rs|<s V* 0 ca> c 4r 0 o -4 Vr o *- ** *4 tflff t+> cr ir ??IvJ* 's cr In 1 0" *H IPis? sO vD r-v- V o1s" cr ^ 7r 5 e'er* Q <4r 3* Hc <N-_ cr ^ <y 4: o c* c* O 4 Cl -or o ^O i* >. sm :-CD rVif'.l c&~ *4 -9 lp/** s5i *00*s 04 r J 3 < " 'S, svr>" C> r1 Co" rfVryo- as o 34JO d^V rf rr Q> .i l< j 0 b 1^ 1 w4 o o Lr<r os|or4" v_rt *? C cr V, X s ^ *o| 'sj f| wj oj ^j -| ^ tJ >| </| >s| rj ^J v| ^ I -h od CL Field Notes: 115 ABD00048826 Client: Source: ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown. Alabama 35023 Georgia Gulf #11 Cyclone Dryer Date: Run No.: 6/14/2000 3 Traverse Point 1-1 1-2 1-3 1-4 1-5 fc 1-6 fW 1-8 1-9 1-10 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 Delta P 1.10 1.50 1.30 1.50 1.50 1.50 1.50 1.60 1.60 1.80 1.20 1.20 1.20 1.50 1.50 1.70 1.50 1.40 1.40 1.50 1.45 PARTICI Sa. Rt. Delta P 1.0488 1.2247 1.1402 1.2247 1.2247 1.2247 1.2247 1.2649 1.2649 1.3416 1.0954 1.0954 1.0954 1.2247 1.2247 1.3038 1.2247 1.1832 1.1832 1.2247 Delta H 1.21 1.65 1.43 1.65 1.65 1.65 1.65 1.76 1.76 1.98 1.32 1.32 1.32 1.65 1.65 1.87 1.65 1.54 1.54 1.65 1.2020 1.60 Tm In m 92 92 93 94 95 97 97 100 100 99 97 98 95 95.00 94.00 94.00 98.00 98.00 99.00 97.00 96.20 Tm Out TF) 92 91 92 93 93 94 94 96 95 94 94 94 94 94.0 93.0 93.0 95.0 95.0 95.0 94.0 95.0 Ts CF> 107 106 106 107 106 108 107 107 107 108 106 107 108 107.0 107.0 106.0 106.0 107.0 107.0 105.0 106.8 116 1 iiliS ABD00048827 Q * < s 0 s' w c < 0 a CO 0 N PJ ft N OOo2 O o N0 O 0 s3r** v~ r rf r c* 0 &r tr d Sc3 w _T*_o I_t rr scs Z ni O 0 c< > c Q 0 r0 r c* 0 03 | fe g 1 L = ll ilz 3O 0 ^O 85 > 2_ o Q 5o $ 2 11 S _J CL O (j >v 0 3 a (L 073 S O SO gro CD 3 ^, Q." 1 c-oI1 C%O 03 Io ra o' $ CM^ a r-- fi M3 cr^ r- r s if Z E gu go CH 0 i&r 00 <J Q 00 c-cW_ no PO ( n(Ko ^ sfiv( >D */ J,v* ! u. 3 O U 'f ^ C- re iS if 0 0O CO -- 1* u T< <t|cV 0 PSc5o& *4 c* c/3 ro r <S CM c* u qo r< o <r -J\ 0-* cr rtf Lr dr- -2 ~t c- ^ -- <r V tf r <r <r j -- *v* cr r <rr r-3 L psO \n)V >0 ,j> n vi) rs; rJ r C> -S V c-J. < r6 NJ a. < o ta- cam cao %tr i_ k- i_ i_ CO 7= 03 03 03 03 i2 cccco a o. o. a IEEEE 0>3 < io > -r a-- O -- ,* P" Lu F? 03 =re .r is- cr 3* cr t* V0 V" <r j c rt sO r- c* Ci a >0 tr OVv' k3\rT> 0 rs V\0 & rr 5| rn 1- j.t3 v o ' t r o K' _-- r '3 >.J c/ y IP V c 'o 4 t*P y Q. aoc. +H& s J C 7 >/ J Field Notes: 117 ABD00048828 Fluidized Bed Dryer Field Data Sheets ABD00048829 Fluid Bed Sampling Port Information Stack Diameter: 45" diameter Stack Area : 11,045 Square feet Stack Height: Approx. 150 feet Test Port Data: A. Diameter: 4 inches B. Upstream Disturbance (L/D): 4.67 C. Downstream Disturbance (L/D): 8.13 Number of Traverse Points: 12 Minimum Number of Traverse Points Required: 12 3 119 ABD00048830 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 Client: Georgia Gulf Source: Fluid Bed Dryer Job No.: 20148 Data Input By: L. Beane l \;V . Run Number Date - ' . ; . .. .4 INPUT DATA 6-15-00 2 6-15-00 3 6-15-00 AVERACE 1 Time Beaan-Ended Samplinq Time. Minutes Stack Area. Sauare Feet 1320-1429 60 11.045 1515-1620 60 11.045 60 1 60 wmmm Barometric Pressure. Inches of mercury 30.1 3 30.13 30.13 30.13 Stack Pressure. Inches of mercury 30.11 30.11 30.11 30,11 Pitot Tube Correction factor 0.84 0.84 0.84 t Meter Correction Factor 0.996 0.996 Nozzle Diameter. Inches 0.221 0.221 Weter Volume, Cubic feet 34.050 34.150 34.655 34.285 Meter Temperature. Dearees F 93.5 93.0 85.4 90.7 Avq. Orifice Delta P. Inches of Water 0.68 0.68 0.72 0.69 Volume H20 Collected. MilliLiters 221.8 230.1 251.60 234.5 C02 Concentration. Percent 0.0 0.0 0.0 0.0 02 Concentration, Percent 20.0 20.0 20.0 20.0 Avq. Sq. Rt. of Delta P. Inches of Water 0.807 0.802 0.826 0.81 Stack Temperature, Deqrees F 148.7 149.6 149.1 149.1 Total paniculate collected, grams----------------------- -- ! MfWi'iihtfiiHi iij ii 11 ii Hi Standard Meter Volume. Cubic Feet 0.0194 SBraml 0.0298 0.0051 0.0181 CALCULATED DATA 1 M'liiff ip* wmwmmtmmm mmmmmmpmmmmimmm 32.620 32.742 33,694 33.019 Standard Water Volume, Cubic Feet 10.440 10.831 11.843 11.038 Moisture Fraction 0.242 0.249 0.260 0.250 Molecular Weiqht Of Stack Gas 26.181 26.115 25.991 26.096 Density Of Stack Gas 0.0593 0.0591 0.0589 0.0591 Averaqe Stack Gas Velocity. Feet/Second 50.866 50.709 52.306 51.294 Stack Gas Flow < Stack Conditions, ACFM Rack Gas Flow <> Standard Conditions. DSCFM 33.709 22.283 33,605 22.002 34,663 22.366 33,992 22.217 Isokinetic Samolinq Rate. Percent 101.18 102.85 104.12 102.72 Particulate concentration @ Std.Cond..Grains/Cu.Ft. Particulate emissions, lbs per hour 0.0092 0.0140 1 1.75 i 2.64 0.0023 0.45 0.0085 1.61 120 ABD00048831 ENTEC Services, Inc. 25 Commerce Ave.-Sulte 104-Huevtown. Alabama 3S023 Client: Source: Georgia Gulf Fluid Bed Dryer Date: Run No.: 6/15/2000 WMMKM Traverse Point 1-1 k 1-2 * ,, 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.63 0.64 0.64 0.62 0.65 0.68 0.68 0.70 0.69 0.65 0.63 0.61 WMMWMmm 0.65 Sa. Rt. Delta P 0.7937 0.8000 0.8000 0.7874 0.8062 0.8246 0.8246 0.8367 0.8307 0.8062 0.7937 0.7810 0.8071 Delta H 0.66 0.67 0.67 0.65 0.68 0.71 0.71 0.74 0.72 0.68 0.66 0.64 0.68 ggj&j Tm In CF) 91 93 93 93 93 94 95 95 96 97 98 98 Tm out rn 92 92 92 92 91 91 92 92 92 94 94 94 94.67 93.5 Ts CF) 145 147 147 148 149 150 149 149 150 150 150 150 148.7 121 < ABD00048832 $ SO < iO aif^ CO ocs "S % CO _ 55 c-- .Q S E = SO CL (vOT si) s> f*|ry k' 0S)5 % i_ __ 5 o cs w =u- E e o */> > _ 5-* 0CO) CO > |<a <CO0 CD cm cm OO o &\s> o sfi r oJC O 10 S |o JrCe c 0. o > 1" 0. > -* 3 3 CO CO f.8 2 CD 5 CO g(sn n OsA> 55 4 ct*t> COcO) *re t t .y- s 2 <n rn .EVo In LL t& <ficr <r\ C\ 3 o i \ <n\l rt A 3 000 in) r~ aJ % rO C~ <r E Io < 0 fA fv tn SA rA M3 >4 < Si sfl >XnD SO c > A* U CM LL. CO 3 0 */ 152^ y r r * w- o. IEv- fa'/>0 E 0 ri-r s- s' o nD Ml S' Va `A U J) " S' c* <r vr * cy r s' <r r <T .c^ rc < V' o T-zr rr oo S c o o O S' 0 T*fc-C%MC%OT%f L_ )_ k_ l_ k_ (/) 3 7= 05 O) O)05 is cc c c o 4= a aaal- 2EE EE Qk_ i-v- * 3* < <Sv -X O T P G ib ^^ ) -c Q 0 O) <> E a C/n jux---j'' CO % w. 2 E cZ Va >o O JU> S' "(S 3- a: % V> sX g 5a tO .i-i LTt c o fV\ CL tos Q_ S> rt <Inr ^ i<n \r* ^ S iy, aap*4vvadrr<y^ KLT,C^ s' H Field Notes: 122 ABD00048833 Client: Source: Georgia Gulf Fluid Bed Dryer ENTEC Services, Inc. 25 Commerce Avc.-Suite 104-Hueytown, Alabama 3S023 Date: Run No.: 6/1/2000 2 Traverse Point 1-1 k ]-2 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.51 0.70 0.75 0.68 0.64 0.60 0.53 0.68 0.65 0.64 0.68 0.68 0.65 So. Rt. Delta P 0.7141 0.8367 0.8660 0.8246 0.8000 0.7746 0.7280 0.8246 0.8062 0.8000 0.8246 0.8246 0.8020 Delta H 0.54 0.74 0.79 0.71 0.67 0.63 0.56 0.71 0.68 0.67 0.71 0.71 0.68 Tm In CF) 97 97 97 100 99 93 94 89 88 87 87 87 92.92 Tm Out TF) 97 96 96 98 97 95 95 91 90 88 88 87 93.0 Ts CF) 148 149 150 150 148 149 150 150 150 150 151 150 149.6 ABD00048834 o 5 CO >CO CD <CO0 O o8 ? yj ^Q U- So ccao> xCCDOi a*< 55 x) u2 'sCO -S e2 2o CL 90 r ^Iro 0S>5 %w. __ --CD i o) c2 ^=E e 0 Li. s'i o 2 > o i-r ts> E i0 N\ > ZT^r OcJ g-v O5> C^^M r r* L fO <A \a r>i J\j% ^0 * $H M) r V od -=r Zj 5 o rJ ? SM 04 118 !i8 2 j s n od > a<o0. ^>o 5 co 3Jr5er; cxso s' Co 1/(>0 U 0 to t CtOt _ OvT J JJ < sTl or cr -s' U \a 31 - o CO m v r v> < lo o |J8 *? ure 0 co TrSe3 OS 0 \lsA % \j<a;-i .S 5VXjftl <r . era" : e _ ~ 5 Emrif O t/> 6CO -- CO Id >uO..L Nil .O CeL*.*.* '4. 18a ,1^ PO <45 8& o V_/s &1 % E Vjn L/s > c Qo. -- c->k' S --Li tH V -P ^ H 1111 H Field Notes: 124 ABD00048835 Client: Source: Georgia Gulf Fluid Bed Dryer ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Date: Run No.: 6/15/2000 3 Traverse Point 1-1 k 12 f 1-3 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 0.45 0.70 0.62 0.65 0.68 0.71 0.75 0.81 0.81 0.72 0.68 0.64 WmSSSS 0.69 Sa. Rt. Delta P 0.6708 0.8367 0.7874 0.8062 0.8246 0.8426 0.8660 0.9000 0.9000 0.8485 0.8246 0.8000 0.8256 Delta H 0.47 0.74 0.65 0.68 0.71 0.75 0.79 0.85 0.85 0.76 0.71 0.67 0.72 Tm In rn 86 87 87 87 87 87 86 86 85 85 85 84 86.00 Tm out rn 86 86 85 86 86 85 84 85 84 84 84 83 85.4 Ts rn 150 148 149 150 150 149 148 148 149 150 150 148 149.1 125 Run Time \V ? Field Notes: ABD00048836 a < (3 C05O CO _>% CO <o CO 0 O 8z V^i o o VP pro *7* z r s? b. CacO> r-O JZ c<o0 0 0 ^ HIL C IZ 29 o2 Q. 0 -* <y jo 5a.S%=u__ _ug-_.-_ijgc Z VA sS u (U0 ort CO -- >> Jo0C .c O .CO. o0 I hP CO ffi 0 SI0 "0 i!0 _l CL > g-i a. > & 2 0 5 CO co It _o * %3 E 02 CD 0 3Cc0Oo--"3 a. 0 SSI w1 n% c0o5 c *5 s3 'V3C <T 2 <r - r* E io o 0 00 (No^ 0 05 2 r sO vO Jr ^ U c* 5? co io o 0 -- Ia 1 E 0 vS 3* 2.1 r*c< 2 vi .<0 3" 3" Kj Vl VvJnCi/%* to Q \a d* V i/c rJ C1 <~ta <r* * 1/5 0* ? T5 W^^ ^n" 0v .sU "S to cP J' c? ffi a`n 3*T? d d dCO J, Vi) % Vs. rs C" o .9 -- IT 5"U <n J cr rr 0oo ;S o o o c T- T- t-%C%M CO T%f ^3 t0 I- k. L. c=o w OlOIOIQ^ ^O a.Ea= a= Q= ^o 2 6E E 0w Sl8 Au % $A> Jfo c c d 05 I 2 a) 31 5o O'" C.V/ < =r 0?J ~^0 pi. 5 r* ci \y 0 'JC 0 P fH " >t rJ Vi so M ------Ci 'rP rftP- ~S> p? r< V a3r- csims? r is S-' o owO ^S c ad5 U' i 0.^0 0 Q do So % % rr 0 0%J .O , S*. 0_,"O Id & \r r 0 ciP 0 <- c o 0. -- m k" y"h* Li ^Lj CVN & ^ e o CL Hill I H 126 ABD00048837 Ventilation Baghouse Field Data Sheets ABD00048838 Schematic of Sampling Site Ventilation Baghouse To Building Flow I ^ Test Ports Ventilation Baghouse Stack ABD00048839 ENTEC Services, Inc. 2S Commerce Ave. Suite 104-Hueytown, Alabama 35023 Client: Georgia Gulf Job No.: 20148 Source: Ventilation Baghouse Data Input By: L. Beane Wmiaii'i i , WlW--ill>l II HHM1--h* i 1H1 Hi1 ]l> Yii^iiii|i|IMiJ|j|>iiaw'illKi'Mlllllll>iirhiWlMiy>iliaiW6l<'l'lMi INPUT DATA Run Number 12 Date 6-16*00 6-16-00 Time Beqan-Ended 1220-1327 1341-1445 Samplinq Time. Minutes 60 60 Stack Area. Sauare Feet 7.069 7.069 Barometric Pressure, Inches of mercurv 30.10 30.10 Stack Pressure. Inches of mercurv 30.08 30.08 Pitot Tube Correction factor 0.84 0.84 Meter Correction Factor 0.996 0.996 Nozzle Diameter. Inches 0.200 0.200 Peter Volume. Cubic feet 44.882 42.950 Meter Temperature. Dearees F 88.7 94.5 Avq. Orifice Delta P, Inches of Water 1.22 1.10 Volume H20 Collected. MilliUters 33.0 38.0 C02 Concentration, Percent 0.0 0.0 02 Concentration. Percent 20.0 20.0 Avq. Sa. Rt. of Delta P, Inches of Water 1.017 0.981 Stack Temperature, Deqrees F 88.5 98.1 Total particulate collected, qrams iiiin pin 0.0192 'u ,nji'iii TwnSiflMii'iiii[jFiiririTi 0.0400 CALCULATED DAI A mmmsmmsm Standard Meter Volume. Cubic Feet 43.386 41.073 Standard Water Volume, Cubic Feet 1.553 1.789 Moisture Fraction 0.035 0.042 Molecular Weiqht Of Stack Gas 28.427 28.349 Density Of Stack Gas 0.0714 0.0700 Averaqe Stack Gas Velocity. Feet/Second 58.519 56.965 Stack Gas Flow @ Stack Conditions, ACFM Rack Gas Flow @ Standard Conditions. DSCFM 24.820 23.181 24,161 22,013 Isokinetic Samplinq Rate, Percent 101.09 100.78 Particulate concentration < Std.Cond..Grains/Cu.Ft. 0.0068 0.0150 Particulate emissions, lbs per hour 1.35 2.83 3 6-16-00 1507-1610 60 7.069 30.10 30.08 0.84 0.200 42.145 88.3 1.11 30.0 0.0 20.0 0.985 85.5 0.0259 AVERAGE HHHHHi 60 30.10 30.08 RHHHI 43.326 90.5 1.15 33.7 0.0 20.0 0.99 90.7 0.0284 mmx&aimkmm 40.764 1.412 0.033 28.438 0.0718 56.457 23,946 22,512 97.80 0.0098 1.89 41.741 1.585 0.037 28.405 0.0711 57.314 24.309 22,569 99.89 0.0105 2.02 129 ABD00048840 Client: Source: ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Georgia Gulf Ventilation Baghouse Date: Run No.: 6/16/2000 1 Traverse Point M fc 1-2 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 2.10 0.60 0.57 0.89 1.00 1.10 1.50 1.70 1.40 0.66 0.71 0.76 immmmm 1.08 Sa. Rt. Delta P 1.4491 0.7746 0.7550 0.9434 1.0000 1.0488 1.2247 1.3038 1.1832 0.8124 0.8426 0.8718 1.0175 Delta H 2.37 0.68 0.64 1.01 1.13 1.24 1.70 1.92 1.58 0.75 0.80 0.86 1.22 Tm In CF) 87 86 87 88 89 90 90 92 92 92 94 92 89.92 Tm Out rn 87 86 86 86 87 87 87 87 88 89 90 90 88.7 Ts CF) 85 85 85 87 90 92 90 91 91 87 90 89 88.5 130 ABD00048841 foft Q) I 0 M) 4 >0 U- 0 -j 0 O VOc)) p N o C at CO 0 55 g5 0 .oo g5 rcZ SO Q. n s> 4 r 0 r< sS jj- CJ o fd o M .S>ft__ ? ko_ cco =2 -fit <Lx> juf. U.Z o r. CD -- > >82 _ nM 2o t>^' Hf 0 co 0 CM CM O CM Oo O u 2 t @ 4 @-r 1 ano a u.* -r Es CO 0) = ml O too 1o Jj 0. > CL > a nft CL u 3 W(0.\*A Ss E* NO o CO CO co I c/5 (0 Q> _C T3 C0O) tt %CM 15 CcO Ll M V\ --5o00o c T- T- o 5 r% CJ N% M% Q) 03 l. -mfn O) O)O) D) iS C CC O q. *CL*S. Q. I~ E EE E n- 0 I$ c/> OC COA 2^ .Q 3 s 3"co o_ 28 IJ Hi 1 1 Z 0. O> < t_ c a 33 2 O ft u CO Q^ CO 4 1i ilil 15 3 CcDL ft 3 h*> 2 M o) S2 o >co--K--\. 0."" O o` 1o * 0q0 0o0 -V 3 0Q lr n J 0> S8O) fr ts V) * ^ >3 >3 3 a E Io W i4rt vmr LL W .* iHw CO S m* Q. Eo> ffi T <1 7 3T tco& <$$<> <F IE =5 W1 a 9< J| Q> c ^ H S * 0* 5 " 3 3 2 10 ? ! vi r c 00 ^ c o CL *1 W J - 1 Vf! oc CL Field Notes: 131 ABD00048842 Client: Source: ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Georgia Gulf Ventlation Baghouse Date: Run No.: 6/16/2000 2 Traverse Point 1-1 fc______ Li_______ f 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 WSSSSBSBk Delta P 1.40 1.30 0.70 0.81 0.92 0.96 1.50 0.89 0.83 0.77 0.83 0.81 0.98 PARTICULATE FIELD DATA, METHOD 5 f.......................... Sa. Rt. Delta P 1.1832 1.1402 0.8367 0.9000 0.9592 0.9798 1.2247 0.9434 0.9110 0.8775 0.9110 0.9000 Delta H 1.58 1.47 0.79 0.92 1.04 1.08 1.70 1.01 0.94 0.87 0.94 0.92 Tm In fF) 90 90 92 94 97 98 101 103 97 97 96 94 0.9806 1.10 95.75 Tm Out CF) 90 90 90 91 93 94 95 97 96 95 95 93 94.5 Ts CF) 94 93 95 99 102 100 101 105 102 98 97 91 98.1 ABD00048843 ft < 0 <r u. (0 ) _c .c CO TO __ .0 TO C 3 0 3 U:?- OO eZ co ^ % ____ 5: S=k-CicS.2zS& |u- " il 05 ft t3 >r 13 C(0O > 05 c I* < (O Oto N N O C! OOqZ O (/i 03 > >0 |2 * - ?5 1 <1 W .*: S 5 s&s w a. HE n * 0q e* 9- 2 3 V) CO CO O) _o o 3> C" '< 0 "11 c TO re CD w | fi < 0 3 <r 0- T v I Ae # JJ? *8^ _. (X $* < 5J g? g.2^ ir c z a. 0 Tt| & <" tr tft* Ol - C C0 d 1 q 4 *2 3 i * 11 p1 3 4 SjE!r TO ` Q < co^l Q 5 _Ere Q u p> 55 I'* % < % l/l E a. H T .32 ^OrsZ-N Oa' SC 0. O) 2=5 TO Ss. yi Q v0 3* ti I0 I[f 81$ Ev 1/ ~ 0 91 S fl _ * 11 jl c 'ao. 9J l* T V5 sS - *1 ^ v 9 Qoc_ 1 Field Notes: 133 ABD00048844 Client: Source: ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown. Alabama 3S023 Georgia Gulf Ventilation Baghouse Date: Run No.: 6/16/2000 S Traverse Point M k f 1,."23 1-4 1-5 1-6 2-1 2-2 2-3 2-4 2-5 2-6 Delta P 1.30 1.30 0.76 0.84 0.96 0.92 1.70 0.90 0.85 0.81 0.76 0.74 MH 0.99 Sq. Rt. Delta P 1.1402 1.1402 0.8718 0.9165 0.9798 0.9592 1.3038 0.9487 0.9220 0.9000 0.8718 0.8602 0.9845 Delta H 1.47 1.47 0.86 0.95 1.08 1.04 1.92 1.02 0.96 0.92 0.86 0.84 1.11 Tm In rn 89 88 89 90 90 90 91 91 89 89 88 90 89.50 Tm Out TF) 88 88 88 88 87 87 87 86 86 86 86 87 88.3 Ts CF) 84 85 86 86 86 88 88 90 86 83 82 82 85.5 ABD00048845 *o .,_ o '0 ir<3 00 IO CO c03 CCOD 5 9 * oc3 ra c u- J5 2 i ~t 2O to s 03 *tf_c _ro _2 -- Q. o o0 to cu-- >> _\fi CO 3" CaO> CO _> CD C < to to O CM CM O TM 8z sjy 0 *t f* 11 cllg s IMlio %CD 3CCOO CO 2 CL 2 In 3 C Eg m03 r< qTo' IwB* OT4C3SD) w * L c fl q q j </> > oq to </> E *1 8lo: I >9 4 * r r to r V) Oc> / o* .d rM 55 7> u. tO V |3 Sw o. HE < e 9&. t*x* po I* o ?Ph ^H (q*^> 6 cr c* 4 io u_ r< o v> iP 5 oo or C *- r< Jf % . <r * eft g5 i! =z Q. <3 7-1 * 0 If u o|J J* <5? 0 o o o -: c0 oQl eQt d c - n% n% j% 1oc_s rc1a_ uLc>_ olc_s -iCossO ~o. 'a. '5. '5. H E E jEo *, Jtf a 55 03 < SWa5 ^ 2U| o 6 rSs -Q 5 ifib i 0 oc % s Ml c 'ao. H t V . ^ ^ c o Q- Hll Field Notes: 135 ABD00048846 No. 4 Rotary Dryer Field Data Sheets ABD00048847 No. 4 Rotary Dryers Sampling Port Information Stack Diameter: 27*' x 24" Stack Area : 4.50 Square feet Stack Height: Approx. 10 feet Test Port Data: A. Diameter: 4 inches B. Upstream Disturbance <L/D): 0.91 C. Downstream Disturbance (L/D): 3.14 Number of Traverse Points: 25 Minimum Number of Traverse Points Required: 25 SAMPLING POINT NUMBER 1 2 3 4 5 DISTANCE FROM STACK WALL (INCHES) 2.4" 7.2" 12.0" 16.8" 21.6" Overhead View 1 Side View ) 00 O O -------------------- Gas Flow ID Fan ABD00048848 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 PARTICULATE EMISSIONS CALCULATIONS Client: Georgia Gulf Source: No. 4 Rotary Dryer Job No.: 20148 Data Input By: L. Beane Run Number Date Time Beqan-Ended Samolinq Time. Minutes Stack Area, Sauare Feet Barometric Pressure. Inches of mercury Stack Pressure, Inches of mercury Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter. Inches Pieter Volume. Cubic feet Meter Temperature, Deqrees F Avo. Orifice Delta P, Inches of Water Volume H20 Collected. MilliLiters C02 Concentration, Percent 02 Concentration, Percent Avq. Sq. Rt. of Delta P. Inches of Water Stack Temperature. Deqrees F Total particulate collected[ orams 1--jjrrnTiWlliltT ^ Standard Meter Volume, Cubic Feet Standard Water Volume, Cubic Feet Moisture Fraction Molecular Weiqht Of Stack Gas Density Of Stack Gas Averaoe Stack Gas Velocity. Feet/Second Stack Gas Flow <> Stack Conditions, ACFM Rack Gas Flow <S> Standard Conditions, DSCFM Isokinetic Samplinq Rate, Percent Particulate concentration < Std.Cond.,Grains/Cu.Ft. Particulate emissions, lbs per hour 1 6-14-00 1602-1725 62.5 4.500 30.05 29.96 0.84 0.990 0.180 49.425 94.4 2,16 76.0 0.0 20.0 1.454 131.8 0.0118 47.028 3.577 0.071 28.037 0.0650 87.522 23.631 19.613 97.72 0.0039 0.65 2 6-14-00 1745-1857 62.5 4.500 30.05 29.94 0.84 0.990 0.180 53.250 83.9 2.44 81.0 0.0 20.0 1.556 112.8 0.0104 3 6-14-00 62.5 4.500 30.05 29.93 0.84 0.180 52.505 84.0 2.29 76.0 0.0 20.0 1.494 116.5 0.0146 CALCULATED DATA 51.684 3.813 0.069 28.058 0.0672 92.246 24.906 21,388 98.47 0.0031 0.57 50.934 3.577 0.066 28.091 0.0668 88.824 23.982 20.521 101.15 0.0044 0.78 AVERAGE MHH ISMIHHS 62.5 30.05 29.94 51.727 87.4 2.30 77.7 0.0 20.0 1.50 120.3 0.0123 49.882 3.656 0.068 28.062 0.0663 89.530 24.173 20.507 99.11 0.0038 0.66 138 ABD00048849 Client: Source: Georgia Gulf #4 Rotary Dryer 'ZlmZ Traverse Point 1-1 1-2 1-3 I-4 1-5 2-1 2-2 2-3 1 2-4 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-1 5-2 5-3 5-4 5-5 shumi Delta P 0.45 0.58 1.30 2.40 3.10 0.77 1.00 1.50 2.70 3.30 0.93 2.10 3.40 3.10 3.50 1.10 2.30 2.90 2.70 3.10 2.80 1.90 2.40 3.20 3.80 2.25 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown. Alabama 35023 Date: Run No.: PARTICULATE FIELD DATA, So. Rt. Delta P 0.6708 0.7616 1.1402 1.5492 1.7607 0.8775 1.0000 1.2247 1.6432 1.8166 0.9644 1.4491 1.8439 1.7607 1.8708 1.0488 1.5166 1.7029 1.6432 1.7607 1.6733 1.3784 1.5492 1.7889 1.9494 Delta H 0.43 0.55 1.24 2.28 2.98 0.74 0.96 1.44 2.59 3.17 0.89 2.02 3.26 2.98 3.36 1.06 2.21 2.78 2.59 2.98 2.69 1.82 2.30 3.07 3.65 Tm In CF1 91 92 94 95 96 97 98 99 99 99 99 100 101 101 102 102 102 102 102 101 101 100 100 too 100 1.4538 2.16 98.92 ii 6/14/2000 1 Tm Out fF) 90 90 91 91 92 93 93 94 95 95 95 95 96 96 96 97 98 98 97 97 96 95 94 94 93 94.4 TsfF) 125 128 130 133 129 125 122 131 130 131 135 133 135 141 144 139 137 134 131 130 127 129 130 134 131 131.8 ABD00048850 rfCeiD r f * 5 5 re c u. re -3c2 ZS re u- 3 O (A CO c $< Vre) O N NO ^ 8oZ |U)U '00) i- ^ re . T u. 'Sfo1 rt :re= oo oo *0 4 ^^ % %CM ICtO ^ 3 re Wre Ure. Lre. 7V=) co oi It O) c Q. o> O) i2 c jc o a a *~ EEE >ore * >re r--| 5 C%O 3 CO co V) CD <X o _c o rree re Eg re CD o re (75 q: cm t: % "55 A 0<re0 w2 0 Q 0Co Vo) C a $ 4 re L J5 re 3 4 iO re a re 2 N N o re 00 CL D>) < 5/ Jprer*Jr Q <* o*r"t co Sfc Jr3e re > Q. (J re _Q o TS 91 - .2 q5 JJ I o ,, CO ao V 44 * d d 0 00o * 1* > ao^J . j| t| r J" v o o- 0 Orce) M 0< 0 r1 "q. M W n V E c S3ot r o* 'a| to v: r rs 6 S <5 T * % <r ,, 53 <3 a 2 CO 23?O* re 3 2 cor ; a4 !S * ! * 71 * *| a, fft 8jr 2 * & fcW Q. IEr-e J*> - ft <r * 0* * 0" *?* if 8! ir c3 CL Field Notes: 140 ABD00048851 Client: Source: CeorgiaCulf #4 Rotary Dryer till: i^ 11 Traverse Point 5-1 5-2 5-3 5-4 5-S 4-1 4-2 4-3 i 3-1 3-2 3-3 3-4 3-5 2-1 2-2 2-3 2-4 2-5 1-1 1-2 1-3 1-4 1-5 Delta P 1.30 2.20 3.20 4.30 3.80 1.40 2.30 3.00 3.90 3.70 1.00 2.20 3.10 3.20 3.70 1.30 1.80 2.30 2.90 3.50 0.75 0.97 1.80 2.80 3.00 2.54 ENTEC Services, Inc. 25 Commerce Ave.`Suite 104-Huevtown. Alabama 35023 Date: Run No.: 6/14/2000 2 llilliilllll Sa. Rt. Delta P 1.1402 1.4832 1.7889 2.0736 1.9494 1.1832 1.5166 1.7321 1.9748 1.9235 1.0000 1.4832 1.7607 1.7889 1.9235 1.1402 1.3416 1.5166 1.7029 1.8708 0.8660 0.9849 1.3416 1.6733 1.7321 1.5557 Delta H 1.25 2.11 3.07 4.13 3.65 1.34 2.21 2.88 3.74 3.55 0.96 2.11 2.98 3.07 3.55 1.25 1.73 2.21 2.78 3.36 0.72 0.93 1.73 2.69 2.88 2.44 Tm In f F) 86 86 87 87 87 86 86 86 86 85 85 85 84 84 84 85 85 86 86 87 87 86 86 86 86 85.76 Tm Out CF) 86 85 85 85 B4 83 82 82 82 81 80 80 80 80 81 81 81 B2 82 82 81 81 81 82 82 83.9 TsfF) 124 121 120 123 119 115 118 116 114 111 113 109 109 107 109 111 114 109 111 113 109 107 106 106 105 112.8 141 ABD00048852 > foa Q Q v0>0 >. re<Q < o OOcm cOm no z^ 3or"|pA sr ri 00- U- 05 -- -- 5 2^ 3t- 5S3m eZ O.oo gi I r rH I = Ec SZ u- 3 >Ore W- o d > _n * O* >" V) \A - m E i_ o= A a ll O =O a > 0. > s t3f> V> 2> / ST o CD 3 5 - a. re ' 55 CO oo 05 _C o K d 3 -a 4o 3- rl > * O) \A * E oU J *- V * 01 u. W 2* 3O re re. w2 E (t v> i j ;o jsa -$ JA 0 -3 -3 rr &> $ $ V *V d0 <| a Q? 44 $$v d j-ifl fi <1 O' 4 _T (A J t/) 3QS <1 M n,, 0* 0 3W 0^* pc t>c a U.v'k oo .-5 0 0 0 C T- r- :<orr t%- e%g n% v* ^3 L. L. U. W -V=> o) ra 05 o 3 O .S c c c o 5 aaQ^f" 2EEE5 HCO c 2 2Wo CQ re " .2 re u-0(j g 2 N - o2 o o Z Q. 0>5 < r EH % it g 5 re i! =z >re _3 ; O4 2 '3 A r t& Ol 1n A J- s t $3 I0 r c 'o CL c o CL 0 r\ <1 r --o rt s 5 3 a C* n r f - fi - c <5 - ri Sa ^U 1S <q rP qr cFi v? 9 v 0 !? i j C4 rt *5 -WM '/I Date ___ 42. Field Notes: ABD00048853 Client: Source: Georgia Culf Siio*679 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Date: Run No.: 6/14/2000 3 Traverse Point 1-1 1-2 1-3 1-4 1-5 2-1 2-2 2-3 1f 2,s-4 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-1 S-2 5-3 5-4 5-5 -- Delta P 0.71 0.83 1.50 2.60 3.20 1.20 1.70 2.40 2.70 3.30 1.00 2.20 3.20 0.40 3.40 1.30 2.50 3.10 3.70 4.00 1.10 2.20 3.40 4.10 4.00 2.39 So. Rt. Delta P 0.8426 0.9110 1.2247 1.6125 1.7889 1.0954 1.3038 I.S492 1.6432 1.8166 1.0000 1.4832 1.7889 0.6325 t .8439 1.1402 1.5811 1.7607 1.9235 2.0000 1.0488 1.4832 1.8439 2.0248 2.0000 1.4937 Delta H 0.68 0.80 1.44 2.50 3.07 1.1S 1.63 2.30 2.59 3.17 0.96 2.11 3.07 0.38 3.26 1.25 2.40 2.98 3.S5 3.84 1.06 2.11 3.26 3.94 3.84 2.29 Tm InfF) 85 86 86 86 86 86 86 86 86 86 86 85 8S 85 86 86 86 85 86 86 86 86 86 87 86 85.84 Tm out rn 85 83 82 82 82 83 83 82 83 83 82 82 82 82 82 82 82 81 82 82 82 81 81 82 81 84.0 Ts rn 107 109 113 117 115 116 114 115 HI 109 113 118 117 120 119 121 120 117 119 120 121 121 124 120 117 116.5 143 ABD00048854 0(05 * tr Lx V) r-r O) c v> (D 5 g2 a c S d. >& r* 2 5s %____ k. co to > cS ^=C e a) ll ia 1o * to > j A/D ok o o iri * - i* *l * 4 'J 6 fl C 9 'V a> r r *o. S r* rv V) 13 My */) tM5M^ IS tl 1 0 to to _> (0 CO to O (V N O N Oooz o Si oco " > 0* g !i` I JH> </> J2 oo 0- > 1$ C . r> _ U Si'll O n u. <n = o jr>\n ro iS 4 ^ few ~ Q. E r Id J"2 vn = o - 00 r y ty 3? ^ 4) t Field Notes: oE a P c ctf ftp e o Q_ illlH mi m ABD00048855 No. 5 Rotary Dryer Field Data Sheets ABD00048856 No. 5 Rotary Dryers Sampling Port Information Stack Diameter: 27" x 24" Stack Area : 4.50 Square feet Stack Height: Approx. 10 feet Test Port Data: A. Diameter: 4 inches B. Upstream Disturbance (L/D): 0.91 C. Downstream Disturbance (L/D): 3.14 Number of Traverse Points: 25 Minimum Number of Traverse Points Required: 25 SAMPLING POINT NUMBER 1 2 3 4 5 DISTANCE FROM STACK WALL (INCHES) 2.4" 7.2" 12.0" 16.8" 21.6" Overhead View 24" 24" "R" 80" ID Fan 146 ABD00048857 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 Client: Georgia Gulf Source: No. 5 Rotary Dryer Job No.: 20148 Data Input By: L. Beane Barometric Pressure. Inches of mercury Stack Pressure, inches of mercury Pitot Tube Correction factor Meter Correction Factor Jozzle Diameter. Inches Peter Volume. Cubic feet Meter Temperature. Degrees F Avq. Orifice Delta P, Inches of Water Volume H2Q Collected, MilliLiters CQ2 Concentration. Percent 02 Concentration. Percent Avg. Sq. Rt. of Delta P, Inches of Water Stack Temperature. Degrees F 30.04 0.84 0.990 0.185 43.380 93.5 2.06 67.0 0.0 20.0 1.337 153.8 30.06 0.84 0.990 0.185 50.305 97.3 2.39 69.0 0.0 20.0 1.440 150.0 30.03 0.84 0.990 0.185 44.445 97.5 1.95 65.0 0.0 20.0 1.287 152.3 46.043 96.1 2.13 67.0 0.0 20.0 1.35 152.0 Standard Meter Volume. Cubic Feet Standard Water Volume, Cubic Feet Moisture Fraction Molecular Weight Of Stack Cas Density Of Stack Cas Average Stack Cas Velocity. Feet/Second ack Cas Flow <> Stack Conditions. ACFM <ick Cas Flow <> Standard Conditions. DSCFM Isokinetic Sampling Rate, Percent Particulate concentration @ Std.Cond.,Crains/Cu.Ft. Particulate emissions, lbs per hour 41.448 3.154 0.071 28.036 0.0629 81.854 22,101 17.731 90.18 0.0037 0.56 47.769 3.248 0.064 28.112 0.0635 87.860 23,722 19,310 95.44 0.0098 1.62 42.144 3.060 0.068 28.069 0.0631 78.759 21,265 17.153 94.79 0.0019 0.28 43.787 3.154 0.067 28.073 0,0631 82.825 22.363 18,064 93.47 0.0051 0.82 147 ABD00048858 Client: Source: Georgia Gulf No. 5 Rotary Dryer ENTEC Services, inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Date: Run No.: 6/15/2000 I Traverse Point 1-1 1-2 1-3 1-4 1-5 2-1 2-2 2-3 ) 2-4 2-5 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-1 5-2 5-3 5-4 5-5 Delta P 1.10 1.70 2.30 2.40 3.20 1.70 2.00 2.40 3.00 3.10 1.00 1.90 2.50 1.60 1.80 1.70 2.40 3.10 2.30 1.60 0.61 0.70 0.68 1.00 1.10 1.88 So. Rt. Delta P 1.0488 1.3038 1.5166 1.5492 1.7689 1.3038 1.4142 1.5492 1.7321 1.7607 1.0000 1.3784 1.5811 1.2649 1.3416 1.3036 1.5492 1.7607 1.5166 1.2649 0.7810 0.8367 0.8246 1.0000 1.0488 1.3368 Delta H 1.21 1.87 2.53 2.64 3.52 1.87 2.20 2.64 3.30 3.41 1.10 2.09 2.75 1.76 1.98 1.87 2.64 3.41 2.53 1.76 0.67 0.77 0.75 1.10 1.21 2.06 Trnlnm 91 91 92 92 93 94 95 95 95 96 96 96 96 97 99 99 99 99 100 101 101 103 103 104 105 97.28 Tm Out fF) 83 86 86 86 87 87 87 87 87 88 88 88 89 90 9! 91 92 92 93 93 93 93 95 95 95 93.5 Ts f F) 149 150 IS2 1S5 153 157 155 151 153 156 153 153 157 161 163 IS7 15S 156 158 153 151 147 149 150 151 153.8 148 1 1 8 ABD00048859 0 l. V V) (A r 8 k Vr) 04* X 0 ccJo) * CO 0 i rQ 0O3 O re re cC ss V ft 1 4 W *1 M 4 2 o> at 0 i1__ CD J2 Ti 5it0!) =u_ C E H 5 z O0 5^ otf o r CO >> *9 11 IA I* > 0 1so Hj HI Cl. 4 3 E <1(1 J J'3 ii * * Hi C 0 <1 4 1*7 71 7 *7 W C j3i-Br ^ v: 1@ 5! i re ij L > in o ^o 0. > fCOt tfl lo- 31- ii fA E 2re CD ore 55 jCO:O) r0ae "g ^5 ! ii- Z re o o 5000 tn 03 V) _i, C 10 Oo "5 * j5 "re O^ N-- 2o Q. u? $ ((/4I oo lit % J vj 55 0 e=z ffl i5-t n n: w o) a ra raiS _c = o c o 2 o. a a a1- EE EE eX r A fc* 0" 0>3 < J$ re -' >. CL W O I* 9 P J iS 1*1 co % -a JS 3 0 vi o JJ <1* V) Site 4o, s Field Notes: ABD00048860 Client: Source: Georgia Culf No. 5 Rotary Dryer ENTEC Services, Inc. 2S Commerce Ave.-Suite 104-Huevtown. Alabama 35023 Date: Run No.: 6/1 S/2000 2 Traverse Point 1-1 i-2 1-3 1-4 1-5 2-1 2-2 2-3 |M 2-S 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-1 5-2 5-3 5-4 5-5 MMMi Delta P 0.68 0.79 0.99 1.40 2.00 1.90 1.30 2.20 1.90 1.70 1.30 1.70 2.80 3.10 3.40 1.50 1.90 2.30 3.40 3.00 1.90 3.40 3.90 3.30 2.50 2.17 So. Rt. Delta P 0.8246 0.B888 0.9950 1.1832 1.4142 1.3784 1.1402 1.4832 1.3784 1.3038 1.1402 1.3038 1.6733 1.7607 1.8439 1.2247 1.3784 1.5166 1.8439 1.7321 1.3784 1.8439 1.9748 1.8166 1.5811 1.4401 Delta H 0.75 0.87 1.09 1.S4 2.20 2.09 1.43 2.42 2.09 1.87 1.43 1.87 3.08 3.41 3.74 1.65 2.09 2.53 3.74 3.30 2.09 3.74 4.29 3.63 2.75 2.39 Tm In fF) 95 95 96 96 97 97 98 98 99 99 99 100 100 101 102 102 102 102 103 104 104 104 105 105 105 100.32 Tm Out TF) 91 92 92 92 93 93 93 93 93 93 93 94 94 94 94 94 95 95 96 96 97 97 98 98 99 97.3 ts m 137 141 143 151 153 149 151 153 150 149 151 153 1S7 154 151 146 151 156 161 153 147 145 149 151 147 150.0 150 ABD00048861 cv - 5 >ft 1V> U. .* 3re % 3 Q0). U) Ere $ $ 3 7> ^* lr | v -v* ,*Jo) `X S3 .1? ? *i i *4 VO yj * n if 0- ^ pfl <r S V) W I c cr V* cr o- H ?y <a $s3 3 *1 rK q nr 4 *i \3 W to ff ** h S ft ^r 2rt <J VI 4 r- + 0 ci a. 3 <3 < to rt T 0 d>)^ rtV) <o *0 ro Field Noles: ABD00048862 Client: Source: Georgia Gulf No. 5 Rotary Dryer ENTEC Services, tnc. 25 Commerce Ave.-Suite 104-Huevtown. Alabama 35023 Date: Run No.: 6/15/2000 3 MHHHI Traverse Point 1-1 1-2 1-3 1-4 1-5 2-1 2-2 2-3 } 2-4 2-5 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-1 5-2 5-3 5-4 5-5 --IBl Delta P 1.70 2.40 3.20 3.90 3.70 1.60 1.80 1.70 2.20 2.SO 1.30 1.60 2.00 2.40 1.80 1.20 0.97 0.71 0.S3 0.48 0.70 0.79 1.10 1.90 2.10 1.77 So. Rt. Delta P 1.3038 1.5492 1.7889 1.9748 1.9235 1.2649 1.3416 1.3038 1.4832 1.5811 1.1402 1.2649 1.4142 1.5492 1.3416 1,0954 0.9849 0.8426 0.7280 0.6928 0.8367 0.8888 1.0488 1.3784 1.4491 1.2868 Delta H 1.87 2.64 3.52 4.29 4.07 1.76 1.98 1.87 2.42 2.75 1.43 1.76 2.20 2.64 1.98 1.32 1.07 0.78 0.58 0.53 0.77 0.87 1.21 2.09 2.31 1.95 Tm In fF) 94 97 97 97 97 98 98 99 99 100 101 100 101 102 102 102 102 103 103 105 105 106 106 107 107 101.12 Tm Out rn 90 91 91 91 91 92 92 92 93 93 93 93 93 94 95 94 95 95 96 97 97 97 98 98 98 97.5 Ts CF) 147 151 154 159 157 146 150 153 151 149 153 157 160 153 152 147 150 151 153 154 150 147 153 154 156 152.3 152 ABD00048863 q% (4 r S o*r * lj_ i <6 V d o cO r C 4 -trcoo awt --; $ 5 gj J o 9 cZ n2 O ? rt 4 r 0 f J 3 0 jo -2%b. _co gfoeEs u. 0 S > r to t>o <0 to o g r M <3 jg j a. 5 > d J SMo oi Q. > I OCM pj O o O ^ 2 o 5 c3Ot V) V) a -!A? tA * ico*. (0 0c5 T(30 3I 0a3 oTO W Z *r+ cm ol i ! V ! -i to M i? oC so(0 M <id<s 3* _y I? * 22oo oo o *52 s'-*- r O 75 O _ (i g o2 Z 0. -3?- %% *CMCO 'T 3s 7(n: uw; c ow>ob>. ak>. i7Ws= _e c c O s aaaa*" a E 5 E % AJ { J i MM #w 2i** 05 Li i 8 05 I % 0 iii ucc.s _c3o ->Oa "Ui 4 i| o 0 v> t u si ^i Qco q=3: fi S$ E 3 3 5 CD " $3 * 4 5 E V 6 ^ r V)rt I y V) 0 rt r* D V^ 0 R to 23 .*O c5o ^JS - nr -4i w1-0* V) a E nj A 1^ tr 53 o. \r */ HSI 351$ * 0- gr* .noft 1 r <rr ^ f4 <f $ 13 e r 34 n < -i * + * nvnl rt r fi 4 W) r >?) A r - o. r t rt <z iiiiO) 0 2!=ro S<.i f* |<aS in 1h- J*9* , VI V f4 c `o CL O CL a rt jci ni '/ U --T. ^^,73 cr crr p-a w < rt ! v> 0 w ' *t- JC fw*` <r i/i 0 in S to rl yj ^ * << Field Notes: 153 ABD00048864 No. 6 Rotary Dryer Field Data Sheets ABD00048865 No. 6 Rotary Dryers Sampling Port Information Stack Diameter: 27" x 24" Stack Area : 4.50 Square feet Stack Height: Approx. 10 feet Test Port Data: A. Diameter: 4 inches B. Upstream Disturbance (L/D): 0.91 C. Downstream Disturbance (L/D): 3.14 Number of Traverse Points: 25 Minimum Number of Traverse Points Required: 25 Overhead View SAMPLING POINT NUMBER 1 2 3 4 5 DISTANCE FROM STACK WALL (INCHES) 2.4" 7.2" 12.0" 16.8" 21.6" m?1? ID Fan ABD00048866 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 3S023 Client: Georgia Gulf Source: No. 6 Rotary Dryer Job No.: 20148 Data Input By: L. Beane INPUT DATA Run Number Date Time Beaan-Ended Sampling Time, Minutes Stack Area. Sauare Feet Barometric Pressure. Inches of mercury Stack Pressure, inches of mercury Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter, inches Weter Volume. Cubic feet Meter Temperature. Degrees F Ava. Orifice Delta P. Inches of Water Volume H20 Collected. MiliiLiters C02 Concentration. Percent 02 Concentration. Percent Ava. Sa. Rt. of Delta P. Inches of Water Stack Temperature. Degrees F Total particulate collected, grams 1 6-15-00 1600-1719 62.5 4.500 30.13 30.03 0.84 0.993 0.180 48.415 101.5 2.12 66.0 0.0 20.0 1.451 156.4 0.0098 CALCULATED DATA 2 6-15-00 1759-1920 62.5 4.500 30.13 30.03 0.84 0.993 0.180 53.225 93.1 2.22 50.0 0.0 20.0 1.486 158.1 0.0139 Standard Meter Volume, Cubic Feet Standard Water Volume. Cubic Feet Moisture Fraction Molecular Weight Of Stack Cas Density Of Stack Cas Average Stack Cas Velocity, Feet/Second Mack Cas Flow ( Stack Conditions. ACFM Rack Cas Flow @ Standard Conditions. DSCFM isokinetic Sampling Rate. Percent Particulate concentration ( Std.Cond..Crains/Cu.Ft. Particulate emissions, lbs per hour 45.740 3.107 0.064 28.1131 0.063 88.919 24.008 19.320 96.48 0.0033 0.55 51.064 2.354 0.044 28.3242 0.063 90.988 24.567 20,126 103.40 0.0042 0.72 3 6-16-00 0824-0940 62.5 4.500 30.13 30.03 0.84 52.010 95.3 2.24 60.0 0.0 20.0 1.492 157.3 0.0151 49.700 2.824 0.0S4 28.2193 0.063 91.440 24.689 20.047 101.03 0.0047 0.80 AVERAGE 62.5 1 30.13 30.03 51.217 96.6 2.19 58.7 0.0 20.0 1.48 157.3 0.0129 48.835 2.761 0.054 28.2189 0.063 90.449 24.421 19.831 100.30 0.0041 0.69 156 ABD00048867 Client: Source: CeorgiaCulf No. 6 Rotary Dryer ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown. Alabama 3S023 Date: Run No.: 6/15/2000 1 Traverse Point 1-1 1-2 1-3 1-4 1-5 2-1 2-2 2-3 |*____ ,s 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-1 5-2 5-3 5-4 5-5 IIISIls Delta P 1.30 1.40 1.80 2.00 2.10 1.90 2.00 1.90 2.10 2.10 2.40 2.30 2.40 2.60 2.10 2.30 2.10 2.20 2.30 2.10 2.40 2.30 2.30 2.20 2.30 2.12 Sq. Rt. Delta P 1.1402 1.1832 1.3416 1.4142 1.4491 1.3784 1.4142 1.3784 1.4491 1.4491 1.5492 1.S166 1.5492 1.6125 1.4491 1.5166 1.4491 1.4832 1.5166 1.4491 1.5492 1.5166 1.5166 1.4832 1.5166 1.4508 Delta H 1.30 1.40 1.80 2.00 2.10 1.90 2.00 1.90 2.10 2.10 2.40 2.30 2.40 2.60 2.10 2.30 2.10 2.20 2.30 2.10 2.40 2.30 2.30 2.20 2.30 2.12 Tm In fF) 100 100 102 102 104 103 103 103 103 103 102 102 102 102 100 100 104 104 104 102 102 103 104 106 104 102.56 Tm Out fFI 98 98 100 102 101 102 101 100 100 101 101 100 101 100 100 102 10) 101 102 100 100 100 101 100 too 101.5 Ts CF> 149 152 155 160 159 159 155 153 1S5 154 156 158 160 158 159 160 158 158 160 155 150 156 155 157 159 156.4 157 ABD00048868 <0r r o rO 0 o f r\ r f- rJ " e- V mrM j" $^ 0 0 \ * K' > Field Notes: ^ 111 M 111 W 111 H 111 M ABD00048869 Client: Source: ENTEC Services, Inc. 25 Commerce Ave.-Sulte 104-Hoevtown. Alabama 35023 Georgia Culf No. 6 Rotary Dryer wWMmm Oate: Run No.: mBRmMmm Traverse Point l-t 1-2 1-3 1-4 1-5 2-1 2-2 2-3 9 M_________ 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-1 5-2 5-3 5-4 5-S Delta P 2.20 2.30 2.30 2.40 2.50 2.10 2.30 2.40 2.40 2.50 2.50 2.60 2.60 2.30 2.30 2.00 1.90 2.00 2.00 2.10 1.90 2.10 1.70 1.60 2.20 2.22 So. Rt. Delta P 1.4832 1.5166 1.5166 1.5492 1.5811 1.4491 1.5166 1.5492 1.5492 1.5811 1.5611 1.6125 I.6I2S 1.5166 1.5166 1.4142 1.3784 1.4142 1.4142 1.4491 1.3784 1.4491 1.3036 1.3416 1.4832 1.4863 Delta H 2.20 2.30 2.30 2.40 2.50 2.10 2.30 2.40 2.40 2.50 2.50 2.60 2.60 2.30 2.30 2.00 1.90 2.00 2.00 2.10 1.90 2.10 l .70 1.80 2.20 2.22 Tm In f F) 90 92 93 94 96 97 98 98 98 94 96 98 94 97 98 96 90 92 94 90 90 90 92 93 94 94.16 6/15/2000 1 Tm Out rn 88 90 92 92 92 92 93 92 94 92 92 96 94 94 94 94 98 95 90 88 89 88 89 90 92 93.1 Ts rn 145 152 ISO 161 159 150 162 160 160 167 165 166 168 160 161 155 153 155 155 160 158 160 158 157 156 158.1 ABD00048870 160 Field Notes: ABD00048871 Client: Source: Georgia Culf 6 Rotary Dryer 1^--I ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown. Alabama 35023 Date: Run No.: 6/16/2000 3 Traverse Point W 1-2 1-3 1-4 1-5 2-1 2-2 2-3 if ,, 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-1 5-2 S-3 5-4 5-5 lligiiiiiiB Delta P 1.50 1.80 1.80 1.90 2.00 2.00 2.10 2.10 2.20 2.20 2.60 2.60 2.50 2.30 2.40 2.80 2.30 2.30 2.40 2.50 2.60 2.30 2.40 2.30 2.00 2.24 Sq. Rt. Delta P 1.2247 1.3416 1.3416 1.3784 1.4142 1.4142 1.4491 1.4491 1.4832 1.4832 1.6125 1.6125 1.5811 1.5166 1.5492 1.6733 1.5166 1.5166 1.5492 1.5811 1.6125 1.5166 1.5492 1.5166 1.4142 1.4919 Delta H 1.S0 1.80 1.80 1.90 2.00 2.00 2.10 2.10 2.20 2.20 2.60 2.60 2.50 2.30 2.40 2.80 2.30 2.30 2.40 2.50 2.60 2.30 2.40 2.30 2.00 2.24 Tm In f F) 90 92 92 93 94 92 93 94 95 95 9S 98 99 95 97 99 99 100 97 98 98 98 101 103 103 96.40 Tm Out TF1 88 89 90 90 91 88 92 92 ' 93 93 94 95 97 93 95 96 97 98 96 96 96 96 100 100 101 95.3 t$ rn 145 150 151 1 S3 155 160 160 159 158 159 160 159 156 158 160 159 160 158 160 160 160 157 157 160 159 157.3 161 ABD00048872 0 s I 0i fw a u fft t- *i*Jv 0 u. to 1-- r r- 03 c ^ at w ** i(D A o p (J 0 vj r< f<tr t; 0 .e :&_______ ___ *- .2 -ft ^ f ul 2 4) 11. c . 3O to to 0 _>. C s < to O CM CM O ooOz o |Q 0 car !o -- T--cMcri'C m %% % 23- u. _ w *- t=o 2 c C C C O 5 Q. Cl'ClQ.1- 5 EE E E noi'* > 8 > -* Op Hn !/* 11 g l| SsS * I 9 e. > ** So 3 to to */> _o -~ O Et^ o CD ^\ jtf. o 55 O w Cm" oo ^ <r <> w o> o ? fab > ft <*i o =tt.% v>^ cr- C2 *r\ O_ a So g*J ^ ft ^ 0 <0* 0>3 < s z iT cZ 13 a-- O E 3 |sH >> in Vfi ^ *8 * 0 * jq > O' V. fiJ ri U VS vjl c O oi f* *! 4 Ok r <* Ssfco iS > v{ * N Q. E Jo O ** SX O' O' 5QvX3 0 u v N *i vj 'c f* Q <JA Vrt J* ^IVl <r <s- Tr => 3* M> / Vo is ^ > c * > * O' V <y* 6- tl c* jr T^o vfl fJrJ ol r0 ri rvj n| f^vjlfM ft O he Lo ^ 3^ '* \S0 vSl \D oVfi N ft N H T* A$o q ^_ rv r- ' Ha> 'ip <fi *4 -J * o > 3" >> J % -- 21D ^ 2^_ E V) d t^j q <4 if V, t* c will E-fJ ft #4 iHJjJ^Hd^dzj^Jd 1 E=rJ ft e Ho Q. 11 W111 H 111 W111 M 111 i ABD00048873 No. 7 Rotary Dryer Field Data Sheets ABD00048874 No. 7 Rotary Dryers Sampling Port Information Stack Diameter: 27" x 24" Stack Area : 4.50 Square feet Stack Height: Approx. 10 feet Test Port Data: A. Diameter: 4 inches B. Upstream Disturbance(L/D): 0.91 C. Downstream Disturbance(L/D): 3.14 Number of Traverse Points: 25_ Minimum Number of Traverse Points Required: 25 Overhead View SAMPLING POINT NUMBER 1 2 3 4 5 6 DISTANCE FROM STACK WALL (INCHES) 2" 6" 10" 14" 18" 22" Side View oooooo Gas Row ID Fan ABD00048875 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 Client: Georgia Gulf Source: No. 7 Rotary Dryer Job No.: 20148 Data Input By: L. Beane Run Number Date Time Beqan-Ended SamDlinq Time. Minutes Stack Area. Square Feet Barometric Pressure. Inches of mercury Stack Pressure. Inches of mercury Pitot Tube Correction factor Meter Correction Factor Nozzle Diameter. Inches Veter Volume. Cubic feet Meter Temperature. Deqrees F Avq. Orifice Delta P. Inches of Water Volume H20 Collected. Milliliters C02 Concentration. Percent 02 Concentration, Percent Ava. So. Rt. of Delta P. Inches of Water Stack Temperature. Deqrees F Total particulate collected, orams Standard Meter Volume. Cubic Feet Standard Water Volume. Cubic Feet Moisture Fraction Molecular Weiqht Of Stack Gas Density Of Stack Gas Averaae Stack Gas Velocity. Feet/Second yack Gas Flow < Stack Conditions. ACFM Brack Gas Flow @ Standard Conditions. DSCFM Isokinetic Samolino Rate. Percent Particulate concentration < Std.Cond.,Grains/Cu.Ft. Particulate emissions, lbs per hour INPUT DATA 12 6-16-00 6-16-00 1015-1128 1210-1317 60.0 60.0 4.500 4.500 30.13 30.13 30.08 30.08 0.84 0.84 0.990 0.990 0.175 0.176 43.665 46.825 97.5 97.1 2.45 2.71 73.0 72.0 0.0 0.0 20.0 20.0 1.550 1.647 155.8 157.4 0.0328 0.0418 CALCULATED DA'Fa 41.460 3.436 0.077 27.973 0.0626 95.083 25.672 20.427 91.15 0.0122 2.13 44.520 3.389 0.071 28.036 0.0626 101.215 27.328 21.826 90.57 0.0145 2.70 3 1336-1442 60.0 4.500 30.13 30.08 0.84 0.176 51.047 97.9 2.46 68.0 0.0 20.0 1.545 157.0 0.0392 48.438 3.201 0.062 28.131 0.0628 94.758 25.585 20.637 104.21 0.0125 2.20 AVERAGE 60.0 | 30.13 30.08 47.179 97.5 2.54 71.0 0.0 20.0 1.58 156.8 0.0379 44.806 3.342 0.070 28.047 0.0627 97.019 26.195 20.963 95.31 0.0130 2.35 165 ABD00048876 Client: Source: Georgia Culf No. 7 Rotary Dryer ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Date: Run No.: 6/16/2000 1 Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 2-1 fe 2-2 r 23 2-4 2-S 2-6 3-1 3-2 3-3 3-4 3-5 3-6 4-1 4-2 4-3 4-4 4-5 4-6 Delta P 0.77 1.20 1.20 1.S0 1.60 1.10 1.30 1.80 2.70 2.80 2.00 3.00 3.20 3.40 3.50 3.80 3.80 2.70 2.40 2.50 2.70 3.20 3.40 3.60 2.50 So. Rt. Delta P 0.8775 1.0954 1.0954 1.2247 1.2649 1.0488 1.1402 1.3416 1.6432 1.6733 1.7029 1.7321 1.7889 1.8439 1.8708 1.9494 1.9494 1.6432 1.5492 1.5811 1.6432 1.7889 1.8439 1.8974 1.5496 Delta H 0.7S 1.18 1.18 1.47 I.S7 1.08 1.27 1.76 2.65 2.74 2.84 2.94 3.14 3.33 3.43 3.72 3.72 2.65 2.35 2.45 2.65 3.14 3.33 3.53 2.45 Tm In f F) 88 89 90 92 92 94 94 95 96 97 98 98 99 101 102 102 103 102 103 104 106 106 107 107 98.54 Tm Out rn 85 87 89 90 91 92 92 93 93 93 94 96 97 100 101 100 100 101 102 102 103 104 104 105 97.48 TsfR 150 152 151 153 154 156 156 148 150 ISO 153 155 >60 158 159 158 160 1S9 158 160 161 160 159 160 155.83 166 ABD00048877 O rraa * > < 0 0 (A to >> C < U) o cm o ^ OOZ Wo >9 u r pV*> ^6 irir O) g tt w -- *5; 5B gi| ^ U_ J; 9 2 2U CL \ v JX ^ ___ w ro ro goes > = Cu. c= Z U- r o' oO -- >> \r> S* i-t^ o0 @v=s'l 'Si? sn 118 sl too Q. --oOX > 2 3 (0 to 0 a !o CD co |\* Q-a o, ( CO 0 O) c T3 n o: cm TI **= E 3 r > NN ft y n h r-j l*: L vJ 0ra n -x, C `V v \o Ml|*0 n \o \4 ^ c ' >^ O^ 5l? V) *31 ri M Is f1 rP OV} > 0 v <* > 0 N /- * !* r to 2^ ,, 3 O0 Sgt) W v E 0 _ dU O^ 'Q VOJ\C ^ V ^ IT v k*. v> Co V) . VJB N SI NsN X n fo r> 00 V? \jj >o| ^ ^ N rO n Q ti N ^1n<J . CPO- o ^ 0" nl = 0,$ OC 3 T- CM ro M %% % g 3- i_ _ t_ l_ (=0 (A " O) O) cc O) c oc> ioz ; CL`o. `o. CL 2 EE E ^ - Vr c g0 o ra 0_ .O "ro O _ " N N 0 O Z 0. 1 0 0) 0 J 2 , kD 0 5 44 J 2 T* h >j) w> a ^o 0. CO O *v Q , t>* L, O-^ 5C4 CO c_ 3 a % T im e X& 0 2(U o N ^ -? % u. & o ^ >u Sn ^ r5 Un ,_ lo ra ^s|a ,v a vi ?io <y tf IS, r . EV c `o r1 <^l 0. TfHTlHoe CL ro <j n HI III H n M> NN\ 0 O z u_ 167 ABD00048878 Client: Source: Georgia Gulf No. 7 Rotary Dryer ENTEC Services, Inc. 25 Commerce Ave.-Soltc 104-Hueytown, Alabama 35023 Oate: Run No.: 6/16/2000 2 Traverte Point 1-1 1-2 1-3 1-4 1-5 1-6 2-1 1k 2-2 ,, 2-4 2-5 2-6 3-1 3-2 3-3 3-4 35 3-6 4-1 4-2 4-3 4-4 4-5 4-6 MHH Delta P 1.30 1.40 1.50 2.70 2.80 3.10 1.90 2.10 2.50 2.60 2.80 3.00 3.40 3.SO 3.40 3.50 3.70 3.70 2.50 2.70 2.80 3.00 3.10 3.30 2.76 Sq. Rt. Delta P 1.1402 1.1832 1.2247 1.6432 1.6733 1.7607 1.3784 1.4491 1.5811 1.6125 1.6733 1.7321 1.8439 1.8708 1.8439 1.8708 1.9235 1.9235 1.5811 1.6432 1.6733 1.7321 1.7607 1.8166 1.6473 Delta H 1.27 1.37 1.47 2.65 2.74 3.04 1.86 2.06 2.45 2.55 2.74 2.94 3.33 3.43 3.33 3.43 3.63 3.63 2.45 2.65 2.74 2.94 3.04 3.23 2.71 TmlnfF) 85 87 89 90 92 92 94 94 96 97 98 98 101 101 102 101 102 103 103 104 106 106 108 107 98.17 Tm Out fFl 82 86 87 89 90 90 92 93 94 94 95 97 98 97 99 99 100 101 101 102 104 104 105 105 97.1 TsfF) 150 149 152 155 160 161 160 159 157 158 155 156 160 160 IS7 158 160 159 158 158 159 159 157 160 157.4 168 ABD00048879 *O) (0 20 < 0 f* 7 a* Ol (A D) i(s0 *0* 55 ro JS e= 1L CZ S 2 So CL uV h o o v y' r o -2> %________ 0 w ro ro 5 0 cH5 iQ-> {IL= u- J= z C E 3 u3 0O '-n v$ VO > 0I f hi I* VO vs A r V > ** *. *> V. sj \fl o 00 >> -\q 0 rJ 0* H-J 37" CA 0 CA > *CD C <0 (A (0 O 8zcm cm O f'J ft |S^ ( 1 t* 9O w 9 hA 0 0 i 2|0 S oO o oQ jd> Q- > I 3 (A CA (L /> O 0 Er* o 0 m 0 3 CA 00 CL** 00 ! 55 CO % <A 05 c T003 o: CM w* 5 Tu ro c u- ro cr ft 0 cH c*ift 2 to H V) fM to V) r , Cm 3 0 O' Q Q 0 .o fij o Sq is, 2 2- t N N 0) 0 O o0 i? .^ Lf> ;0= --0 c2 1- CM CO TT =te % ?fc % 0 0 0 0 *<=A 0)01010-: c cc c o a Q.Q. Q. *-- E EE E it. i< vS J '%d > ? >1 & <c J aj 0 Q. 55 o 2 0` Ef~ ra^J 5x o <o c/r |(0 k O>) < 0 go >9- Q. O *0 0-- 0.' sU; pA S * 2<i. a. ^ u- 0 E h- <T> O^ u. 3 0 2 &r\ W a. E 0 H I* O yo 8 ?S 5c 50 * 2r N *3-* c> r* *$> v5 ^ V) V v: > VO V) 'N vo liO vo x s O No ^ 1/1 V) \ *N Ci vy * Vi N V V Vi s V > V N Cr-Tv vd (Tkr IvS & ** (/3C0 j ^ r: X\'* r r4 vO r' O) ^ J.E^ 20 0 PN d: v" &V> o >b a3 h> v> SrJ| M|T V* Vi 4J v, b 0 E^ v> % n c An bo v; o. r *o c o CL 1111 H 1111 H n n * Field Notes: ABD00048880 Client: Source: Georgia Gulf No. 7 Rotary Dryer ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Date: Run No.: 6/16/2000 3 Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 2-1 k 2-2 f3 2-4 2-5 2-6 3-1 3-2 3-3 3-4 3-5 3-6 4-1 4-2 4-3 4-4 4-5 4-6 IHMIWI% Delta P 2.60 2.80 2.80 3.40 3.60 2.90 3.30 3.40 3.20 3.60 3.70 3.70 2.50 2.10 2.20 2.30 3.20 3.30 0.95 0.90 0.95 0.98 0.95 0.98 2.51 So. Rt. Delta P 1.6125 1.6733 1.6733 1.8439 1.8974 1.7029 1.8166 1.8439 1.7889 1.8974 1.9235 1.9235 1.5811 1.4491 1.4832 1.5166 1.7889 1.8166 0.9747 0.9487 0.9747 0.9899 0.9747 0.9899 1.5452 Delta H 2.55 2.74 2.74 3.33 3.53 2.84 3.23 3.33 3.14 3.53 3.63 3.63 2.45 2.06 2.16 2.25 3.14 3.23 0.93 0.88 0.93 0.96 0.93 0.96 2.46 Tm In fF) 85 87 88 92 92 93 93 94 96 98 98 100 101 102 102 103 104 105 106 105 106 108 108 104 98.75 Tm Out rn 83 85 86 90 91 91 91 92 95 96 97 98 99 100 100 101 102 103 103 103 104 105 105 107 97.85 Ts fF) 145 147 150 153 155 157 1S8 160 161 160 160 158 160 160 158 160 158 158 160 158 158 156 160 159 157.04 ABD00048881 oO) > 0 < Q rf vT sX vO a- r r mco> (w0 * $ Cs Je3 o5d LU - CL Jl w 2 ^ ro .2 " 10_) =LL LL S e r- *-- > oO 03 -- > 6 o KU lb 1/ V \/ t N Kv K r- r N PS. Cv oc 'q. />] S M 3)3 sC \Q O Ip vo Win Vo -sC v! \ K C C. i o> >J /> W 0 K f* 1>* &* r ^ >> 03 C < Q V(0) 0 CM CM O N O O oz U %t- %CM C*fOc ^ U L L U tn 3 0) J) O O m in 0)010101- *n O ^ a cl a a*- S EE E E CL > 11 o Bo 6w Q. > CA I *o r-s. 13** a. w HE V \r ^ v" Vo tVa; N S^ n, Vo *s *N (30 </> A CL A 1$ o cCoO SO 8<1 CL O u c 'r&e o: cm Z. ** 5, w IT C (A .2 o "re CL 00 ; re S s n 8 2 s CL A0 ,v\,Wrc - O>) < N % g5 IcZ re ^ ><71 Q. o a O /v \o o, sy^ & w Ov Ito O go -- Oo to \X6o a a u n rc n-sj) < V c c o -0 ff; re VNT , v OHoI a Vv,' y V UjW> nC' o*.`J4*c/* v- ^ Xr V; Ko 3 C2 6 \P P* O f V Q us to V V)l^ M l4vO * o0 0^ w S Nl v3 mK'J a r- r1 r 'In ri w *33 Vi O' >. CO *0 -V *0 5 r C8L*.^ Ii so I- m .Hi \/ CM vi r r> c `o CL r* n > \n r- !r 'O oe Q. H n 3* i/j Field Nole ABD00048882 No. 8 Rotary Dryer Field Data Sheets ABD00048883 No. 8 Rotary Dryers Sampling Port information Stack Diameter: 27" x 24" Stack Area : 4.50 Square feet Stack Height: Approx. 10 feet Test Port Data: A. Diameter: 4 inches B. Upstream Disturbance(L/D): 0.91 C. Downstream Disturbance(L/D): 3.14 Number of Traverse Points: 25 Minimum Number of Traverse Points Required: 25 Overhead View 27" SAMPLING POINT NUMBER 1 2 3 4 5 DISTANCE FROM STACK WALL (INCHES) 2.4" 7.2" 12.0" 16.8" 21.6" A ir VS? VV V 24" Side View ) OO 24" "R" 80" O O -------------------- Gas Flow ID Fan ] 173 ABD00048884 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 Client: Georgia Gulf Source: No. 8 Rotary Dryer Job No.: 20148 Data Input By: L. Beane INPUT DATA Run Number Date Time Beqan-Ended Sampling Time. Minutes 1 6-15-00 1855-2005 62.5 2 6-16-00 0825-0930 62.5 Stack Area. Sauare Feet 4.500 4.500 Barometric Pressure, Inches of mercurv 30.13 30.13 Stack Pressure. Inches of mercurv Pitot Tube Correction factor 30.10 0.84 30.11 0.84 Meter Correction Factor Nozzle Diameter, Inches Peter Volume. Cubic feet Meter Temperature, Degrees F Avq. Orifice Delta P. Inches of Water Volume H20 Collected, Milliliters C02 Concentration. Percent 02 Concentration. Percent Avg. Sq. Rt. of Delta P, Inches of Water Stack Temoerature. Degrees F 0.992 0.175 44.305 84.3 1.86 37.0 0.0 20.0 1.401 168.8 0.992 0.175 43.640 82.5 1.81 33.0 0.0 20.0 1.380 160.1 Total particulate collected, grams 0.0095 0.0276 i jp I CALCULATED DATA - ** a** -jkksm* Standard Meter Volume, Cubic Feet 43.111 42.597 Standard Water Volume. Cubic Feet Moisture Fraction Molecular Weight Of Stack Gas Density Of Stack Gas 1.742 0.039 28.381 0.0622 1.553 0.035 28.420 0.0632 Average Stack Gas Velocity. Feet/Second fcack Gas Flow <> Stack Conditions. ACFM Pack Gas Flow < Standard Conditions. DSCFM Isokinetic Sampling Rate, Percent Particulate concentration < Std.Cond..Grains/Cu.Ft. Particulate emissions, lbs per hour 86.215 23.278 18,892 98.38 0.0034 0.55 84.345 22.773 18.821 97.58 0.0100 1.61 3 6-16-00 1000-1103 62.5 4.500 30.13 30.13 0.84 0.175 44.870 88.6 1.98 45.0 0.0 20.0 1.449 169.0 0.0167 43.331 2.118 0.047 28.297 0.0621 89.386 24.134 19.443 96.09 0.0059 0.99 AVERAGE 62.5 30.13 30.11 44.272 85.1 1.88 38.3 0.0 20.0 1.41 166.0 0.0179 43.013 1.804 0.040 28.366 0.0625 86.649 23.395 19.052 97.35 0.0064 1.05 174 ABD00048885 Client: Source: Georgia Gulf No. 8 Rotary Dryer ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown. Alabama 35023 Date: Run No.: 6/15/2000 1 Traverse Point 1-1 1-2 1*3 1-4 1-5 2-1 2-2 2-3 ^ 24 2-5 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-1 5-2 5-3 5-4 5-5 Delta P 1.50 2.70 3.20 3.80 3.80 1.10 2.20 3.30 3.10 3.40 0.80 1.50 2.50 3.60 2.00 0.70 1.10 2.00 2.70 2.80 0.50 0.70 0.80 1.50 1.50 2.11 PARTICULATE FIELD DATA, Sa. Rt. Delta P 1.2247 1.6432 1.7889 1.9494 1.9494 1.0488 1.4832 1.8166 1.7607 1.8439 0.8944 1.2247 1.5811 1.8974 1.4142 0.8367 1.0488 1.4142 1.6432 1.6733 0.7071 0.8367 0.8944 1.2247 1.2247 1.4010 Delta H 1.32 2.38 2.82 3.34 3.34 0.97 1.94 2.90 2.73 2.99 0.70 1.32 2.20 3.17 1.76 0.62 0.97 1.76 2.38 2.46 0.44 0.62 0.70 1.32 1.32 1.86 Tm In TF) 81 81 81 81 81 82 83 85 85 85 85 85 84 84 85 8S 86 85 85 86 86 83 83 83 83 83.72 Tm Out fF) 83 84 84 84 84 85 85 85 85 85 87 86 86 86 86 86 86 85 85 85 8S 84 84 84 83 84.3 TsfF) 165 166 167 168 169 168 169 169 170 170 168 169 169 170 168 168 169 170 170 170 170 170 169 170 170 168.8 175 ABD00048886 so _v0C>>A> cre < (rAe 0 * 0 NoO ON Oo ^Z o In Ia 0r* O(ocA> rr> (rAe X3 1rc7e =cre Z- 2 Q. *0 A O) k_ re re -s 5.S5E=5cZ 0 u. s= _8l r >ore A-- SoO > d .O0e M 0 E AO 113 re 0 ?|6 D- > fw ! s %CO fA rev s\o ^0*Ck' o S0<-2* o a croe re Q_ 3W (OCA) 8<r Ql^ re 0 ip 0> 0 CO 1 \r \a C~ r- f-- -- _ % r0en) - rfC->> v tcr*\ s lO SO)rfi ** %0 ^ gcJ 5h 0 2^i re 0Q. CO" E H0 0 'SC'A Ofjo s QCa d> *< po rfv Qco r--4 -O (a cyC^3 ->D >J> cP V/ \/> \r cCe rv pJfw <*> oM O' t/s V/'V/' o VMls/l V0>3V>fiO c* r A [A *^5 0c) 0c) 0c) 0c) o Q.Q.D.Q.H- 5EEE Lo C* <r vr> <~ C e O O>) < 0|r g -5 0 ;r c z 0 rofyO ><* OCl . *=# O- ""'j; sj> <;r C> 0 0 i oJ 55 xO 0 Qre b,ure<V%j co 0-- 0 SUj 01^ sSc Q-U) c0 --* O' 0 HEVVar Voa %a OJ c J' x> re o>0 a Br uTcc \r 0 Cv -J s no 0 vj 00a Vs ? oi iQ r si ST* fA S' r'- s' ter* 3" re- CijV Ain O- ^ iAlA ca V i/v 10 \A L/" \TrJ' ia S.sh -a r-T*- <si-- O o 5? (/ O- O' V r> O La C-' vr* 0Q)i. Ci Vr Os f* 5 i Vy Nn Vr V* O VTO 1J* K f*" f~ C-' e~J re- o V LP i u wc 'o Q. rJ -- ^ \r -- r*~ HIod -- --JlO L / / / / / Field Notes: ABD00048887 Client: Source: Ceorgia Culf No. 8 Rotary Dryer ENTEC Services, Inc. 25 Commerce Avc.-Suite 104-Hueytown, Alabama 35023 Date: Run No.: 6/16/2000 2 Traverse Point 1*1 1-2 1-3 1-4 1-5 2-1 2-2 2-3 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-i 5-2 5-3 5-4 5-S SMI Delta P 1.10 1.30 2.80 3.60 3.50 1.10 2.00 1.20 3.20 3.50 0.80 1.50 2.20 3.50 3.20 o.so 1.00 2.00 2.80 3.00 0.50 0.45 1.50 2.50 2.80 2.06 So. Rt. Delta P 1.0488 1.1402 1.6733 1.8974 1.8708 . 1.0488 1.4142 1.0954 1.7889 1.8708 0.8944 1.2247 1.4832 1.8708 1.7889 0.7071 1.0000 1.4142 1.6733 1.7321 0.7071 0.6708 1.2247 1.5811 1.6733 1.3798 Delta H 0.97 1.14 2.46 3.17 3.08 0.97 1.76 1.06 2.82 3.08 0.70 1.32 1.94 3.08 2.82 0.44 0.88 1.76 2.46 2.64 0.44 0.40 1.32 2.20 2.46 1.81 Tm in rn 79 80 80 80 82 83 85 83 84 84 84 84 84 85 86 8S 85 8S 8S 85 85 85 85 86 86 83.60 Tm Out rn 83 79 79 79 80 80 80 80 80 80 80 81 81 82 82 82 82 82 82 83 83 83 83 83 83 82.S Ts rn 148 149 155 160 162 164 16 167 168 169 169 169 169 170 170 170 170 170 169 170 170 170 169 170 >69 160.1 177 ABD00048888 O (D cn CD I0 < 0 Q _C>O rce < TO Q 0 OJ N O N 8z H & J5 sD o fj O0 a (M si 6 r r- cn .cco at CD 0) k gs ^ rr *E z g 2 so CL a9 u 0 o- 0 sO 3 SJ 8 LA r-' o -2> % __ _ feui_ ceo g2 ^ = LL c a> ll LL V/> > (0 o 5 JSnJ H<sX o m o o 20 TO va) 0 > >o wo f3 6 I Q. `Uu (^*\ TO CD 3* io i ToO CO c%o cO) XT3O EC CM Z. =** io u to r~ > D) . _C P 'q.M) si * J? oC fsJrJ S3 .O* toS W Cl E f-- V. = P^ 0* 1 -^c~ <BO NO M >j sr1 s)l^ TO -< r- ^ y> v si> Xv |sT if * * C< f< S" o 8Jr ~a net0 l tP< V Va *tp 4A -e 20 u_c< *4 *0 0 \n r r- r^7-N c oo ro D_ T--O O Oo o c <- *- TO o _ NNO z Va cO~' c!^n- C\s' " 3Tfc-C%NJCJtfOc M%l- ^ ^^^*=,, CD cn cn a> S = c c C c o 5 o. a a qI" 5 6 EE rf 4f U Ci > < : cETO x b. ror-* co 3fc ^ - T- > 0) r < o 3 J : J a % xD S^\ c/fc? if* cc % $ c* Kr> *- J* sj> 2 =2 cz ,, j=c* =*? $ <(r o It Li a pH* < 4 u> o v\ i,r n JsJt C0 lof jf c4 rS _3 toi> >rp Q. o b .5 ! /* o Cs Sfi <f aO . Io si d N Ip*^ -' y 5^ Ln v> Va v o Ki lo |co s c|Vr r* 2 - *2 u> S' jrA a2. Ca \.s) S^N or ^rjo V/l *vN A Ci V> K LrjO ft ot 35 c o r~ 5- V\ - C* D. r o CL cJ nrhN- r> r'; La whim Date Field Notes: ABD00048889 Client: Source: Georgia Culf No. 8 Rotary Dryer ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Huevtown, Alabama 35023 Date: Run No.: 6/16/2000 3 Traverse Point l-l 1-2 1-3 1-4 1-5 2-1 2-2 2-3 \ 24 * 3-1 3-2 3-3 3-4 3-5 4-1 4-2 4-3 4-4 4-5 5-1 5-2 5-3 S-4 5-5 IHHMHi Delta P 0.58 0.90 1.50 2.70 2.70 0.70 1.00 2.00 3.10 3.10 0.80 1.10 2.20 3.10 3.50 1.10 110 3.00 3.50 3.80 3.80 2.20 2.70 2.SO 3.50 PART1CULATE FIELD DATA, <ETHOD 6 Sg. Rt. Delta P 0.7616 0.9487 1.2247 1.6432 1.6432 0.8367 1.0000 1.4142 1.7607 1.7607 0.8944 1.0488 1.4832 1.7607 1.8708 1.0488 1.0488 1.7321 1.8708 1.9494 1.9494 1.4832 1.6432 1.5811 1.8708 Delta H 0.51 0.79 1.32 2.38 2.38 0.62 0.88 1.76 2.73 2.73 0.70 0.97 1.94 2.73 3.08 0.97 0.97 2.64 3.08 3.34 3.34 1.94 2.38 2.20 3.08 Tm In rn 84 85 86 86 86 86 87 88 90 91 87 88 90 90 91 90 90 91 92 93 94 94 94 94 94 2.2S 1.4492 1.98 89.64 Tm Out rn 84 84 85 85 86 86 86 87 87 87 88 88 88 88 88 87 87 89 89 90 90 90 90 90 90 88.6 ts rn 165 165 166 167 168 169 170 170 170 169 169 170 170 170 170 168 169 170 170 170 170 170 170 170 170 169.0 179 ABD00048890 o io 0 o fA [sA > 0 trM O0 oo M? xj?*a g* O.'sD E ^0* ** *> *4 L^'^kP Vlki)''fi Sj) \ xQ X8 nO JJl *p on>P o ,0 O> Lnv <-s_r* rJ F -r s' r'nSrJ xfi x& S' C* B zj N saris' J'fcr CS c'lc-J O * (0 3ra .-0*2 >l.r->D & W- xl xi Q. Eo> 0 sflr r* 00 (f 0 :o O O ^ r- c- r- c Tr <P* ofl^: nr T" La >0 -E ^ <*=1 Q< qoqO o'V1? ol >J < i^l 4 "D 0 C0D) s' 0) E* h'c*i c so rnr1 H c< n^. r r f * x Ia In -T/>> <e i_o 'c O 5> i2> W> \AO c< = 9 ? ,Lr </> iO -3-=*- iT c< 4/NlO jAxD dj o rA H -- r CL 'Mr T'M' kA e o Q. H 111 H 111 H I M k Field Noles: ABD00048891 No. 3 Boiler Field Test Data ABD00048892 No. 3 Boiler Sampling Port Information Stack Diameter: 39 diameter Stack Area : 8.296 Square feet Stack Height: Approx. 20 feet Test Port Data: A. Diameter: 1/2 inches B. Upstream Disturbance (L/D):1.85 C. Downstream Disturbance (L/D): 2J) Number of Traverse Points: 12 Minimum Number of Traverse Points Required: 12 SAMPLING POINT NUMBER 1 2 3 4 5 6 7 8 9 10 11 12 DISTANCE FROM STACK WALL (INCHES) 0.82 2.61 4.60 6.90 9.75 13.88 25.12 29.25 32.10 34.30 36.39 38.18 <o til II 6.5' 182 ABD00048893 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Mueytown, Alabama 35023 Client: Georgia Gulf - Aberdeen, Mississippi Job No.: 20148 Source: No. 3 Boiler G. Corley MIM'IIWIII i.i nr Run Number Date Time Began-Ended Sampling Time, Minutes Stack Area, Square Feet Barometric Pressure, Inches of mercurv Stack Pressure, Inches of mercury Pitot Tube Correction factor Meter Correction Factor Meter Volume, Cubic feet eter Temperature, Degrees F wAvg. Orifice Velocity Head, Inches of Water Volume H20 Collected, MilliLiters C02 Concentration. Percent 02 Concentration, Percent Avg. Sq. Rt. of Velocity Head, Inches of Water Stack Temperature, Degrees F Carbon Monoxide, ppm Oxides of Nitrogen, ppm 1 Standard Meter Volume, Cubic Feet Standard Water Volume, Cubic Feet Moisture Fraction Molecular Weight Of Stack Gas Density Of Stack Gas Average Stack Gas Velocity, Feet/Second Stack Gas Flow ( Stack Conditions, ACFM Hbck Gas Flow ( Standard Conditions. DSCFM Carbon Monoxide Emissions, lbs per hour Nitrogen Oxide Emissions, lbs per hour 1 6-2900 1734-1834 60 8.296 2 6-29-00 1842-1942 60 8.296 3 AVERAGE mhh flBHHBH60 8.296 60 30.04 30.02 1.00 30.04 30.02 1.00 30.04 30.04 HW30.02 1.00 30.02 0.996 0.996 0.996 22.560 21.440 21.650 21.883 87.8 90.0 88.9 88.9 2.00 i 2.00 2.00 2.00 41.0 36.0 40.0 39.00 3.28 3.31 3.30 3.30 14.19 14.21 14.28 14.23 0.1268 0.1199 0.1354 0.13 205.2 204.9 205.8 205.29 5.01 6.67 5.54 5.74 19.43 19.71 19.89 19.68 iirifflirrianrri iiWiMaiiT minium i trrrrmi tr r wiriiittDfimBPfi mmmaagBmt CALCULATED DATA 1 wmmxxmamm 21.842 20.675 20.919 21.145 1.930 1.695 1.883 1.836 0.081 0.076 0.083 0.080 28.192 28.257 28.183 28.211 0.0583 0.0584 0.0582 0.058 9.611 9.076 10.270 9.652 4.784 4.517 5,112 4,804 3.499 0.08 3.325 0.10 1 1 3,730 0.09 3,518 0.0878 0.49 0.47 0.53 0.496 183 ABD00048894 No. 3 Boiler Test No. 1 Field Test Data Time 17:34:19 17:35:19 17:36:19 17:37:19 17:38:19 17:39:19 17:40:19 17:41:19 17:42:19 17:43:19 17:44:19 17:45:19 17:46:19 17:47:19 17:48:19 17:49:19 17:50:19 17:51:19 17:52:19 17:53:19 17:54:19 17:55:19 17:56:19 17:57:19 17:58:19 17:59:19 18:00:19 18:01:19 18:02:19 18:03:19 18:04:19 18:05:19 18:06:19 18:07:19 18:08:19 18:09:19 18:10:19 18:11:19 18:12:19 18:13:19 18:14:19 18:15:19 18:16:19 18:17:19 18:18:19 18:19:19 18:20:19 18:21:19 18:22:19 18:23:19 18:24:19 18:25:19 18:26:19 18:27:19 18:28:19 18:29:19 18:30:19 18:31:19 18:32:19 18:33:19 18:34:19 Average ABD00048895 Georgia Gulf Corporation Aberdeen, Mississippi June 29, 2000 No. 3 Boiler Test No. 1 Carbon Dioxide 3.26 3.26 3.23 3.23 3.23 3.24 3.23 3.23 3.23 3.24 3.25 3.25 3.26 3.26 3.23 3.24 3.23 3.23 3.22 3.23 3.25 3.24 3.25 3.25 3.24 3.25 3.25 3.27 3.28 3.29 3.3 3.29 3.29 3.29 3.29 3.28 3.3 3.3 3 28 3.29 3.29 3.31 3.3 3.31 3.29 3.28 3.29 3.29 3.27 3.28 3.29 3.28 3.28 3.28 3.26 3.25 3.25 3.26 3.26 3.27 3.26 Carbon Monoxide 3.45 2.35 9.87 4.36 4.09 5.47 6.41 5.58 4.41 3.21 0 0 0 0 0 0 1.7 1.58 7.16 6.23 5.86 5.06 4.43 4.66 4.62 4.92 3.3 4.69 4.21 4.53 4.66 2.75 1.98 0.35 0.29 1.43 3.88 3.94 4.16 4.29 5.41 2.19 6.86 4.3 13.96 14.59 7.76 11.2 11.72 8.31 9.24 6.93 12.49 5.45 5.12 4.65 5.13 7.65 8.98 7.32 5.56 Oxygen 14.01 14.03 14.03 14.04 14.04 14.03 14.04 14.05 14.03 14.01 14.03 14.02 14.01 14.03 14.05 14.03 14.05 14.05 14.08 14.05 14.04 14.03 14.01 14.02 14.03 13.99 14 13.98 14 13.97 13.94 13.99 13.98 13.98 13.97 13.97 13.97 13.96 13.97 13.98 13.97 13.98 13.94 13.98 13.99 13.98 14 13.98 13.99 13.99 14.01 14.01 14.01 14.02 14.03 14.03 14.02 13.98 13.97 14.01 14.03 3.26 5.03 14.01 Nitrogen Oxide 18.94 18.91 18.94 19.13 19.13 19.1 19.1 19.13 19.13 19.13 19.28 19.28 19.13 19.1 19.13 19.13 19.13 19.13 19.1 19.13 19.13 19.26 19.31 19.26 19.28 19.28 19.48 19.31 19.46 19.49 19.28 19.31 19.46 19.49 19.46 19.49 19.46 19.64 19.64 19.46 19.46 19.46 19.46 19.46 19.46 19.64 19.67 19.61 19.67 19.64 19.64 19.64 19.46 19.46 19.46 19.46 19.46 19.49 19.46 19.46 19.49 19.35 185 Client: Source: ABD00048896 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 Georgia Gulf Aberdeen, Mississppi No. 3 Boiler Date: Run No.: Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 1*7 1-8 1-9 MO Ml M2 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 Delta P 0.02 0.02 0.01 0.02 0.01 0.02 0.02 0.01 0.01 0.01 0.01 0.01 0.01 0.01 0.02 0.02 0.03 0.03 0.02 0.02 0.02 0.02 0.01 0.02 Sq. Rt. Delta P 0.1414 0.1414 0.1000 0.1414 0.1000 0.1414 0.1414 0.1000 0.1000 0.1000 0.1000 0.1000 0.1000 0.1000 0.1414 0.1414 0.1732 0.1732 0.1414 0.1414 0.1414 0.1414 0.1000 0.1414 Delta H 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 AVERAGE 0.1268 2.00 186 ABD00048897 C0cO5 A St CO * CO -- -- 55 Si S i11 - 02. U 2 05 TO %k. _(0__(0 5w tt = C li I--cs Z eu LL. 3O E 3 3o3 > ak.) o\rt iHi J C0O} _C>O. (c0 < CO oCO o8 CO JJ * 2 Jl to CO r( g fl > TO < "*r _ 0 11 oCO 3o a> A 0 o cy> 23 U co ~r" QtLo_. TO CO CO %CO Occo) o VCO ?g to to 2 rQ r* o n 0 J v 4t i {iA > /* <X pi * sz 3ss O CO CO r ? i , yt 3 o j tf|U> "5 r* e <fl r<rt d<r j= 0 <N ** "-X * \* 30 J -r T *g CO o o 15 0 0 o y r TO 23OoT %kT0O.5 E C%TOUCMO.) C%kTCOOO_) cl a. EE %LTacO.> a E <J - cC y N(T 0 $2 -71 TO vi c/5 "to a jTO CO 55 3 q: gi ill2 o. t* <0 /J - 05 <> 05 o| TO 13 4 5 3 % 'qj t s>i) !/ TO 0 A\ 2 a. TO E V) ^<3 c 0o. V s r * to- - 0o. pw <] O 7 V J T 0*TO 2- 'i Field Notes: 187 ABD00048898 No. 3 Boiler Test No. 2 Field Test Data Time 18:42:19 18:43:19 18:44:19 18:45:19 18:46:19 18:47:19 18:48:19 18:49:19 18:50:19 18:51:19 18:52:19 18:53:19 18:54:19 18:55:19 18:56:19 18:57:19 18:58:19 18:59:19 19:00:19 19:01:19 19:02:19 19:03:19 19:04:19 19:05:19 19:06:19 19:07:19 19:08:19 19:09:19 19:10:19 19:11:19 19:12:19 19:13:19 19:14:19 19:15:19 19:16:19 19:17:19 19:18:19 19:19:19 19:20:19 19:21:19 19:22:19 19:23:19 19:24:19 19:25:19 19:26:19 19:27:19 19:28:19 19:29:19 19:30:19 19:31:19 19:32:19 19:33:19 19:34:19 19:35:19 19:36:19 19:37:19 19:38:19 19:39:19 19:40:19 19:41:19 19:42:19 Average ABD00048899 Georgia Gulf Corporation Aberdeen, Mississippi June 29, 2000 No. 3 Boiler Test No. 2 Carbon Dioxide 3.28 3.28 3.29 3.28 3.28 3.28 3.28 3.27 3.27 3.28 3.3 3.28 3.26 3.25 3.24 3.26 3.28 3.29 3.28 3.28 3.29 3.29 3.27 3.26 3.25 3.24 3.24 3.23 3.25 3.25 3.25 3.26 3.26 3.26 3.26 3.28 3.29 3.29 3.27 3.28 3.28 3.27 3.27 3.27 3.29 3.28 3.29 3.28 3.27 3.26 3.26 3.26 3.26 3.27 3.26 3.27 3.28 3.29 3.31 3.29 3.3 3.27 Carbon Monoxide 6.99 6.99 6.14 5.93 13.06 15.6 6.5 7.73 6.8 5.97 6.77 6.75 7.12 7.78 7.54 6.51 6.79 6.75 6.95 6.65 7.45 6.56 0 6.23 5.7 6.62 6.46 6.39 7.27 6.76 7.49 7.84 6.93 7.13 7.24 7 7.88 8.08 5.3 6.27 6.39 0.39 12.23 6.97 6.8 7.67 0.64 4.88 6.92 7.72 8.05 7.59 11.35 4.79 0.11 2.93 6.04 5.34 6.65 2.43 5.71 6.62 Oxygen 13.99 13.97 13.97 13.97 13.98 13.97 13.98 14 13.98 13.99 13.98 14.01 14.01 14.03 14.03 14.02 13.97 13.97 13.97 13.96 13.97 13.98 14 14.02 14.03 14.03 14.05 14.05 14.04 14.03 14.03 14.08 14.02 14.03 14.03 13.99 13.97 14 14.02 14 13.98 14.03 14 14 13.99 14 14.01 14.01 14.01 14.04 14.04 14.03 14.02 14.01 14 14.01 13.99 13.97 13.99 13.97 13.98 14.00 Nitrogen Oxide 19.64 19.64 19.61 19.64 19.83 19.83 19.64 19.83 19.64 19.64 19.64 19.64 19.64 19.46 19.46 19.46 19.49 19.46 19.49 19.46 19.49 19.49 19.31 19.31 19.49 19.46 19.46 19.49 19.49 19.46 19.67 19.64 19.67 19.64 19.64 19.49 19.64 19.67 19.64 19.67 19.49 19.64 19.64 19.61 19.64 19.64 19.64 19.49 19.49 19.46 19.46 19.49 19.49 19.64 19.64 19.64 19.64 19.83 19.86 19.83 19.64 19.59 189 ABD00048900 ABD00048901 I (A 0C5 W* ru o _ 5sgl| 2> %_______ ffi u (D n *; Z2 3 So CL oco * > o., 4 H u> au>s _>, cco < tTJ O CM CM O ^ OOoZ O s 2? i C(D5 Ol. --C JL> N Hi w 2H u^ E o CD CD a 11? Mo ~o r0t Q. > s 0 5^ S" o *) cISo i CO 3fc 05 C 'a CD q: cm 0) Q) . CD =o ^ ft .w-Sooooo 1 ~c v r w C ^w oo ra D_ 5 *re o_ o2 Z Q. 1- eg C*5 M1 % * *fc % 2is l0.) ou.i ok. is_ ^;w Tn 05 05 O) 05 -iSi O = 5 = o s O.CLQ.Q.r- a EE E fj 4 jl 0 d 0 l S\ 5 ^0) cj ! " *a*'-SCD ICO D c,, Q lo l re co IH QC CD C Ll 05 < 0 o > -i Q. o B? "j Vi JO 0 2 cv a- I; i fs) E > hCCcr Ih <j > > 90 I'M c ^ -2 2(A ^ oo is ft T1 0, ^ N Cl r 4 - --*ot-4*o1-1M,1-*i ^ (\l O ^ C i r. cN'-pj J 0 HI Q. s c** S* Vi ft g rj a * i rJ k - oi d cl = ( <_ o. -- <0 fti H - </ - r* 2 to--r ^i il`V! So c 'o CL --r O CL V> -J r *5` V|J) rj c4<r] Ql - ^ Field Notes: 191 ABD00048902 No. 3 Boiler Test No. 3 Field Test Data Time 19:57:19 19:58:19 19:59:19 20:00:19 20:01:19 20:02:19 20:03:19 20:04:19 20:05:19 20:06:19 20:07:19 20:08:19 20:09:19 20:10:19 20:11:19 20:12:19 20:13:19 20:14:19 20:15:19 20:16:19 20:17:19 20:18:19 20:19:19 20:20:19 20:21:19 20:22:19 20:23:19 20:24:19 20:25:19 20:26:19 20:27:19 20:28:19 20:29:19 20:30:19 20:31:19 20:32:19 20:33:19 20:34:19 20:35:19 20:36:19 20:37:19 20:38:19 20:39:19 20:40:19 20:41:19 20:42:19 20:43:19 20:44:19 20:45:19 20:46:19 20:47:19 20:48:19 20:49:19 20:50:19 20:51:19 20:52:19 20:53:19 20:54:19 20:55:19 20:56:19 20:57:19 Average ABD00048903 Georgia Gulf Corporation Aberdeen, Mississippi June 29, 2000 No. 3 Boiler Test No. 3 Carbon Dioxide 3.29 3.27 3.3 3.29 3.31 3.29 3.3 3.27 3.3 3.29 3.28 3.28 3.23 3.27 3.25 3.27 3.28 3.28 3.27 3.27 3.27 3.27 3.27 3.27 3.29 3.28 3.28 3.29 3.27 3.25 3.29 3.28 3.28 3.27 3.28 3.29 3.29 3.28 3.28 3.28 3.29 3.28 3.28 3.3 3.29 3.3 3.29 3.29 3.3 3.27 3.26 3.28 3.25 3.24 3.25 3.25 3.26 3.23 3.26 3.27 3.27 3.28 Carbon Monoxide 4.62 4.92 3.3 4.69 4.21 4.53 4.66 2.75 1.98 0 0.29 1.43 3.88 3.94 4.16 4.29 5.97 6.77 6.75 7.12 7.78 7.54 6.51 6.79 6.75 6.95 6.85 7.45 6.56 0 6.23 5.7 6.82 6.46 6.39 7.27 6.76 7.49 7.84 6.93 7.13 7.24 7 7.88 8.08 5.3 6.27 6.39 0.39 3.23 6.97 6.8 7.67 0.64 4.86 6.92 7.72 8.05 7.59 6.24 4.52 5.54 Oxygen 13.97 14 13.98 13.97 13.94 13.99 13.97 13.98 13.98 13.98 14.01 14.03 14.05 14.03 14.03 14.02 13.98 14.01 14.02 14 14.03 14.01 14.02 14 14 14.01 13.99 14 14.03 14.05 14 14 14 14.02 14.02 14 13.99 14 14.03 13.98 14.01 14 13.99 13.97 13.98 14 14 14 14.01 14.04 14.03 14.03 14.06 14.08 14.05 14.04 14.06 14.06 14.03 14.03 14.02 14.01 Nitrogen Oxide 19.83 19.86 19.86 19.64 19.61 19.86 19.86 19.83 19.83 19.86 19.83 19.83 19.83 19.67 19.64 19.67 19.64 19.67 19.67 19.64 19.67 19.83 19.83 19.64 19.64 19.83 19.86 19.86 19.83 19.67 19.67 19.67 19.64 19.64 19.67 19.64 19.67 19.64 19.67 19.67 19.83 19.86 19.83 19.83 19.83 19.83 19.86 19.83 19.83 19.86 19.67 19.64 19.67 19.67 19.67 19.64 19.64 19.64 19.86 19.86 19.83 19.75 193 Client: Source: ABD00048904 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Georgia Gulf - Aberdeen, Mississppi No. 3 Boiler Date: Run No.: Traverse Point 1-1 1-2 1-3 1-4 1-5 1-6 1-7 1-8 1-9 1-10 1-11 1-12 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 Delta P 0.01 0.01 0.02 0.02 0.02 0.02 0.03 0.03 0.02 0.02 0.02 0.01 0.01 0.01 0.01 0.03 0.02 0.02 0.02 0.01 0.01 0.01 0.01 0.10 Sq. Rt. Delta P 0.1000 0.1000 0.1414 0.1414 0.1414 0.1414 0.1732 0.1732 0.1414 0.1414 0.1414 0.1000 0.1000 0.1000 0.1000 0.1732 0.1414 0.1414 0.1414 0.1000 0.1000 0.1000 0.1000 0.3162 Delta H 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 AVERAGE 0.1354 2.00 194 0 ABD00048905 3E 3TO ^ > % >c0 ^> O 5 (/> f3f ^O nS 0 ;f a. E0 i35 r r! rr a- * 01 C i' r c>' f, i _ r> J 0 rl J c r fr 1j O oc r 9C re 00 cP 90: SoO <J1 j- <r Hu ^0 <M 0) 0) 01 o O) 05 05 Ol ~ o. a. a. o. SEES 4 c5 0 crl '32! * J m<fw J ^ "0 "> -(S0 (0 o ffl _re Q *W iS w 51*0 x St L. 0 it. 2 a) r- E'y>| H <J** Q. o V) 0 0 cL_ OS A^ < 0 " ^ N o> fc . o "S ^ r ri C0 5 *J -M HaO. J r > *ti ~ ..A *\1 r O <j - - ^ Field Notes: 195 ABD00048906 No. 4 Boiler Field Test Data ABD00048907 No. 4 Boiler Sampling Port Information Stack Diameter: 36 diameter Stack Area : 7.069 Square feet Stack Height: Approx. 20 feet Test Port Data: A. Diameter: 1/2 inches B. Upstream Disturbance(L/D): 2.16 C. Downstream Disturbance(L/D): 2J) Number of Traverse Points: 12 Minimum Number of Traverse Points Required: 12 SAMPLING POINT NUMBER 1 2 3 4 5 6 7 8 9 10 11 12 DISTANCE FROM STACK WALL (INCHES) 0.76 2.41 4.25 6.37 9.00 12.82 23.18 27.00 29.63 31.75 33.59 35.24 o 197 ABD00048908 ENTEC Services, Inc. 25 Commerce Ave. Suite 104-Hueytown, Alabama 35023 w POLLUTANT GAS EMISSIONS CALCULATIONS IHlMWHHHIIMIMBMMMMBBrV'illIfnililffWMilMlWiMWIIIIlWiitliMlIirilTinriBtWTini IMMIIIlTIMIPMlIilKllUlfUl--~l ill* Mil IHII llii liIPWI Client: Georgia Gulf - Aberdeen, Mississippi Job No.: 20148 Source: No. 4 Boiler Data Input By: G. Corley 'iri^^riwrtiBiTrtg^ii nn Run Number Date Time BeRan-Ended SamplinR Time, Minutes Stack Area, Square Feet Barometric Pressure, Inches of mercury Stack Pressure, Inches of mercury Pitot Tube Correction factor Meter Correction Factor Meter Volume, Cubic feet eter Temperature, DeRrees F r Avr. Orifice Velocity Head, Inches of Water Volume H20 Collected, MilliLiters C02 Concentration, Percent 02 Concentration, Percent Avr. Sq. Rt. of Velocity Head, Inches of Water Stack Temperature, DeRrees F Carbon Monoxide, ppm Oxides of NitroRen, ppm INPUT DAT^ " 1 6-2900 2128-2228 60 7.069 30.02 30.00 1.00 0.996 21.780 86.4 2.00 54.0 8.51 5.96 0.3631 259.8 0.71 60.63 2 6-29-00 2237-2337 60 7.069 30.02 30.00 1.00 0.996 21.060 84.7 2.00 52.0 7.91 6.90 0.3576 260.5 0.69 55.31 mmmmmmmammesmmmm 3 AVERAGE 2344-0044 60 7.069 30.02 30.00 1.00 60 HHH 30.02 30.00 23.985 84.9 2.00 61.0 8.59 5.77 0.3594 257.6 0.32 61.36 22.275 85.3 2.00 55.67 8.34 6.21 0.3600 259.32 0.57 59.10 Standard Meter Volume, Cubic Feet Standard Water Volume. Cubic Feet Moisture Fraction Molecular WeiRht Of Stack Gas Density Of Stack Gas AveraRe Stack Gas Velocity, Feet/Second Stack Gas Flow @ Stack Conditions, ACFM Hack Gas Flow @ Standard Conditions, DSCFM Carbon Monoxide Emissions, lbs per hour NitroRen Oxide Emissions, lbs per hour CALCULATED DATA mmmBmsmnn imsammssmsmzmwinmuwBTOTitrawgiMigr 21.127 20.492 23.330 21.650 2.542 2.448 2.871 2.620 0.107 0.107 0.110 0.108 28.354 28.310 28.333 28.333 0.0541 0.0540 0.0543 0.054 28.554 28.158 28.231 28.314 12,111 11,943 11,974 12,009 7,948 7,835 7,862 7,882 0.02 0.02 0.01 0.0197 3.45 3.11 3.46 3.339 198 ABD00048909 No. 4 Boiler Test No. 1 Field Test Data Time 21:28:19 21:29:19 21:30:19 21:31:19 21:32:19 21:33:19 21:34:19 21:35:19 21:36:19 21:37:19 21:38:19 21:39:19 21:40:19 21:41:19 21:42:19 21:43:19 21:44:19 21:45:19 21:46:19 21:47:19 21:48:19 21:49:19 21:50:19 21:51:19 21:52:19 21:53:19 21:54:19 21:55:19 21:56:19 21:57:19 21:58:19 21:59:19 22:00:19 22:01:19 22:02:19 22:03:19 22:04:19 22:05:19 22:06:19 22:07:19 22:08:19 22:09:19 22:10:19 22:11:19 22:12:19 22:13:19 22:14:19 22:15:19 22:16:19 22:17:19 22:18:19 22:19:19 22:20:19 22:21:19 22:22:19 22:23:19 22:24:19 22:25:19 22:26:19 22:27:19 22:28:19 Average ABD00048910 Georgia Gulf Corporation Aberdeen, Mississippi June 29, 2000 No. 4 Boiler Test No. 1 Carbon Dioxide 8.6 8.61 8.61 8.6 8.6 8.21 7.91 8.22 8.53 8.63 8.63 8.55 8.37 8.18 8.12 8.04 7.96 7.91 7.92 7.92 7.91 7.92 8.17 8.36 8.59 8.84 8.94 9 9.07 9.09 9.11 9.13 9.17 9.18 9.19 9.21 9.24 9.24 9.28 9.28 9.05 8.65 8.41 8.31 8.29 8.27 8.27 8.27 6.28 8.28 8.29 8.23 7.37 7.4 7.87 7.73 7.47 7.4 7.33 7.31 7.3 Carbon Monoxide 10.48 4.98 2.73 0.22 0.11 0.14 0.09 0 0 0 0.06 0.08 0.13 0.17 0.16 0.09 0.17 0.2 0.15 0.09 0.16 1.18 4.01 4.79 3.66 1.08 0.16 0.09 0.1 0.17 0.2 0.18 0.2 0.28 0.31 0.3 0.22 0.19 0.25 0.19 0.22 0.13 0.02 0.03 0.17 0.27 0.25 0.27 0.26 0.58 1.27 1.15 1 0.91 0.94 0.91 0.83 0.89 0.73 0.71 0.64 Oxvnen 5.48 5.49 5.49 5.51 5.72 6.39 6.56 5.92 5.55 5.47 5.53 5.71 6.03 6.22 6.35 6.46 6.56 6.59 6.58 6.58 6.6 6.51 6.03 5.79 5.34 5.06 4.9 4.81 4.72 4.68 4.64 4.6 4.55 4.55 4.51 4 45 4 43 4.4 4.36 4.44 5.06 5.58 5.9 5.96 5.99 6.04 6.04 6.05 6.07 6.04 6.03 6.8 7.74 7.13 6.58 7.2 7.47 7.57 7.67 7.73 7.71 8.39 0.82 5.87 Nitrogen Oxide 61.59 62.14 62.14 62.14 62.29 62.29 62.14 54.72 49.09 52.8 59.13 61.94 62.14 60.89 57.02 53.33 51.88 49.95 49.25 49.09 48.9 48.75 48.36 48.25 48.21 56.51 60.54 65.82 69.36 71.46 73.08 73.74 74.1 74.81 74.81 75.17 75.35 76.4 77.64 78.33 79.17 79.22 74.5 65.86 60.01 56.85 55.63 55.42 55.42 54.39 54.93 55.09 55.42 52.97 43.1 43.42 51.21 52.44 49.64 48.21 47.64 59.94 Client: Source: ABD00048911 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Georgia Gulf Aberdeen, Mississppi No. 4 Boiler Date: Run No.: 6-29-00 1 Traverse Point 1-1 1-2 1-3 1*4 1-5 1-6 1-7 1-8 1-9 1-10 1-11 1-12 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-8 2-9 2-10 2-11 2-12 Delta P 0.14 0.15 0.15 0.16 0.17 0.16 0.16 0.14 0.13 0.13 0.12 0.11 0.13 0.13 0.13 0.14 0.14 0.13 0.12 0.11 0.11 0.11 0.11 0.10 Sq. Rt. Delta P 0.3742 0.3873 0.3873 0.4000 0.4123 0.4000 0.4000 0.3742 0.3606 0.3606 0.3464 0.3317 0.3606 0.3606 0.3606 0.3742 0.3742 0.3606 0.3464 0.3317 0.3317 0.3317 0.3317 0.3162 Delta H 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 Tm In (F) 86 87 89 90 90 Tm Out (F) 84 84 84 85 85 HlflHI Itllifilllisl Ts (F) 260 261 261 261 262 262 260 260 260 258 258 259 259 260 259 260 260 260 260 260 260 259 258 258 wmkmmmmmm. AVERAGE 0.3631 2.00 86 4 259.8 201 ABD00048912 3 ! v) Q>) --T < CO O) c _to *(50 *0) $ CcO 5CO SS o2 E c s >*^f.c_r_e___re -- 5 cs5 ^ 0 =U- E =z 3 O L- Q ^ t3 .I'M o r> re > ore > o H _c>o> tco < (0 CO O MNON 8z /OQ 0 il ^ o O 0 0 " 9 1C T CO 0 Jr _l CL To o CL > 3 <4 o0 E o TO m CO to ^ oc too TO " ? 0 3^ to VI C GO cn *fc 0c3 *6 CO S JP * V % r* 0" to 2o0o00 c T- CM C5 'T % 3fc % % o k- L. w b -C=O w 03 03 03 03 iS 75 c c c c o 5 a a a a>" ^ E E Cr d 0 < 3? 3 0 *-2! w TO U_ $ N-- o Z L _TO ,, 2d yTO <V CO s \; 3 K 25 5 > oi Cl ' O V^l ? cl a lo J 5 <f O0 O' x0 <J a> V V'J <- 03 | = ^ TO FM A c o CL HO Q. VJ rJ - r ^l(V <>. or 0 - - H J r O 414 Field Noles: 202 ABD00048913 No. 4 Boiler Test No. 2 Field Test Data Time 22:37:19 22:38:19 22:39:19 22:40:19 22:41:19 22:42:19 22:43:19 22:44:19 22:45:19 22:46:19 22:47:19 22:48:19 22:49:19 22:50:19 22:51:19 22:52:19 22:53:19 22:54:19 22:55:19 22:56:19 22:57:19 22:58:19 22:59:19 23:00:19 23:01:19 23:02:19 23:03:19 23:04:19 23:05:19 23:06:19 23:07:19 23:08:19 23:09:19 23:10:19 23:11:19 23:12:19 23:13:19 23:14:19 23:15:19 23:16:19 23:17:19 23:18:19 23:19:19 23:20:19 23:21:19 23:22:19 23:23:19 23:24:19 23:25:19 23:26:19 23:27:19 23:28:19 23:29:19 23:30:19 23:31:19 23:32:19 23:33:19 23:34:19 23:35:19 23:36:19 23:37:19 Average ABD00048914 Georgia Gulf Corporation Aberdeen, Mississippi June 29, 2000 No. 4 Boiler Test No. 2 Carbon Dioxide 7.29 7.28 7.28 7.3 7.16 7.07 7.01 6.99 6.97 6.94 6.93 6.96 6.99 7.03 7.12 7.19 7.27 7.35 7.41 7.48 7.53 7.56 7.58 7.67 7.68 7.72 7.72 7.73 7.8 7.77 7.83 7.85 7.86 7.84 7.79 7.8 7.79 7.8 7.75 7.76 7.76 7.8 7.93 8.03 6.09 8.18 8.24 8.36 8.39 8.43 8.47 8.56 8.62 8.66 8.72 8.77 8.8 8.69 8.94 9.02 9.09 7.80 Carbon Monoxide 0.58 0.48 0.54 0.63 0.59 0.57 0.58 0.58 0.53 0.57 0.59 0.54 0.61 0.58 0.65 0.78 0.48 0.36 0.44 0.74 0.82 0.81 0.76 0.9 0.79 0.67 0.68 0.54 0.62 0.52 0.51 4.17 7.69 5.69 2.2 0.79 1.14 1.38 0.44 0.25 0.24 0.32 0.25 0.26 0.29 0.27 0.33 0.3 0.32 0.36 0.29 0.3 0.28 0.26 0.26 0.31 0.29 0.24 0.3 0.3 0.82 0.81 Oxvaen 7.75 7.74 7.74 7.82 8 06 6.18 8.28 8.29 8.35 8.39 8.36 8.37 8.22 6.15 8.03 7.86 7.71 7.59 7.48 7.4 7.29 7.24 7.07 7 7 6.94 6.92 6.84 6.82 6.8 6.77 6.71 6.73 6.72 6.79 6.64 6.78 6.9 6.91 6.9 6.69 6.73 6.59 6.42 6.26 6.15 6.05 5.91 5.85 5.79 5.7 5.54 5.47 5.41 5.31 5.21 5.15 4.99 4.94 4.77 4.77 6.85 Nitrogen Oxide 46.62 46.29 46.29 46.29 46.44 46.44 46.47 46.1 45.76 45.17 44.66 44.33 43.79 43.64 43.6 43.79 44.18 44.66 45.39 49.44 49.99 50.85 51.88 52.24 53.29 53.82 53.82 53.86 54.02 54.19 54.39 54.72 55.05 55.76 56.13 56.47 56.68 56.68 55.97 55.8 55.63 55.59 55.26 56.47 57.57 57.91 58.25 58.77 63.2 64.6 65.29 65.13 66.52 67.93 68.13 68.3 68.68 69.31 69.87 73.56 74.32 54.68 Client: Source: ABD00048915 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Georgia Gulf Aberdeen, Mississppi No. 4 Boiler Date: Run No.: 6-29-00 2 VOLUMETRIC FLOW FIELD DATA, METHOD 1-4 ABD00048916 E > < re > c) Co -(Cft * CD _ --; 51 J1 |E 05 5 i_ %_______ - CcD :--2=. c 2 05 I = 5 5. si 2o uZ o o -v co /. >^ ore o-- > o h- 05 (ft _> CD C < (ft (0 O CMNQN 8z 8 I E re -i ij dZ > IE .2 ao. >o 2 fi o0 i* CD m 0 0 p f* v eft j. ^ 0. f* o CD (75 s CO % (ft O) c Tr3e a: cn z. c .. _ *V li re o jo re iS S Q. E j- HvS JJ r f t ^ =M n^ t* 1 1 in * cMd Jj f' r* t*' 4 J nJ r> l> si re .2 J > J 004 N. w l C (ft OO re " SCcD Oo OTo- o 4.) "r f-NMt O % Ofc *fc ^ La k* ^ ka (/) = 05 05 0) 05 = TS| 0=5 0=5 .05 .O) --oS e; Q. D. Q. Q. H* 2 EE E E re O_ 2 N-- o za Cre-- H J o re u co 0 0 i oc cn |f i 0 'J o: 5"Z| co % gs ESZ 0>3 | L. \ * v* o .2 E fv f/ H M f4 r*l n j: 0 < ci| Q. < a> % 2 re ^X V lw 0 V c o o. n) r-k 5 o 0- ^ J > <v,0 -- fj fV ^ ^ ^^ 0r ^'7- t V/i vj j- *.<r i z-- c) Field Notes: 206 ABD00048917 No. 4 Boiler Test No. 3 Field Test Data Time 23:44:19 23:45:19 23:46:19 23:47:19 23:48:19 23:49:19 23:50:19 23:51:19 23:52:19 23:53:19 23:54:19 23:55:19 23:56:19 23:57:19 23:58:19 23:59:19 0:00:19 0:01:19 0:02:19 0:03:19 0:04:19 0:05:19 0:06:19 0:07:19 0:06:19 0:09:19 0:10:19 0:11:19 0:12:19 0:13:19 0:14:19 0:15:19 0:16:19 0:17:19 0:18:19 0:19:19 0:20:19 0:21:19 0:22:19 0:23:19 0:24:19 0:25:19 0:26:19 0:27:19 0:28:19 0:29:19 0:30:19 0:31:19 0:32:19 0:33:19 0:34:19 0:35:19 0:36:19 0:37:19 0:38:19 0:39:19 0:40:19 0:41:19 0:42:19 0:43:19 0:44:19 Average ABD00048918 Georgia Gulf Corporation Aberdeen, Mississippi June 29, 2000 No. 4 Boiler Test No. 3 Carbon Dioxide 9 8.85 8.65 8.36 7.85 7.67 7.88 8.13 8.33 8.47 6.49 8.51 8.53 8.54 8.55 8.55 8.52 8.5 8.43 8.12 7.95 7.93 7.86 7.79 7.72 7.69 7.64 7.61 7.57 7.52 7.46 7.35 7.32 7.31 7.32 7.31 7.3 7.41 7.68 8.18 8.6 8.84 9.02 9.18 9.27 9.33 9.35 9.37 9.39 9.4 94 9.4 9.4 9.39 9.4 9.48 9.57 9.65 9.72 9.83 9.91 8.47 Carbon ^onnxide 1.48 0.51 0.37 0.35 0.32 0.31 0.42 0.44 0.47 0.57 0.73 0.62 0.46 0.35 0.24 0.33 0.32 0.33 0.42 0.38 0.39 0.36 0.34 0.3 0.27 0.27 0.28 0.25 0.25 0.25 0.27 0.28 0.27 0.27 0.24 0.24 0.27 0.28 0.28 0.26 0.3 0.28 0.32 0.27 0.28 0.28 0.3 0.27 0.28 0.27 0.27 0.28 0.39 1.77 2.75 1.35 0.83 0.74 0.56 0.53 0.28 0.45 Oxygen 4.95 5.26 5.61 6.14 7.01 6.66 6.53 6.16 5.87 5.73 5.7 5.67 5.64 5.65 5.63 5.65 5.67 5.71 5.94 6.47 6.55 6.66 6.76 6.9 7.01 7.04 7.15 7.19 7.28 7.36 7.52 7.69 7.71 7.7 7.72 7.73 7.7 7.31 6.72 5.95 5.36 5.01 4.75 4.49 4.36 4.27 4.24 4.22 4.21 4.18 4.18 4.19 4.19 4.19 4.11 3.94 3.82 3.67 3.51 3.35 3.24 6.72 Nitrogen Opjde 75.71 76.4 76.03 72.86 69.36 64.24 55.26 48.36 49.44 52.6 56.3 56.94 59.66 59.85 60.01 60.01 60.16 60.35 60.39 60.54 60.2 53.7 49.44 48.36 47.49 46.25 45.21 44 42.92 42.21 42.03 40.8 401 38.53 38.53 38.33 38.16 38.16 37.99 37.99 42.56 51.56 58.77 65.25 70.9 74.27 77.45 79.41 79.93 80.45 80.5 80.59 60.64 80.83 81.17 81.31 81.69 82.03 82.71 88.57 90.65 60.62 Client: Source: ABD00048919 ENTEC Services, Inc. 25 Commerce Ave.-Suite 104-Hueytown, Alabama 35023 Georgia Gulf Aberdeen, Mississppi No. 4 Boiler Date: Run No.: 6-29-00 3 VOLUMETRIC FLOW FIELD DATA, METHOD 1-4 209 ABD00048920 ccn w ** CD ffl -- -- 51^ = 5 _g |G= = 2 2O Cl O) at * 5 Jj ce co 0 Li s Do CO co _> CO c < cCoO o CM CM O OO O o tn >o V .1 r LL \/ co o := o o o j =3 H o oH co CO >> o 2 -eg O co llo co -2 h. O G. > CoO _o 0*> CL > Io- 23CCOO 24 CL * 00 1 Q, mCO CO CO Co I(oE0 " ra O_ N -7 O2 Z Q. 00 o iy 5 v` CO tn n rT oC JS I V) c%o <Cc0] :o co CM % iV V 0 0? * () c* Sr $ f' V 'T* ft 2= iilz D O> > - ft IS I'M c __ 11 ^ 5^ LL CO 3 ^O **5H* iS s Q. IE- JJ N/ Lo _ K p( > " > \ 1_ fc ft < < Ct po-j- r* vY . .'fs cJ r< ft yu Jr4 tr ^ ^ Field Notes: 210 ABD00048921 Appendix C Laboratory Analysis ABD00048922 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, Silo #675 Job No.: 20148 City/State Aberdeen, Mississippi Analyst: Tim Draheim Barometric Pressure,in hg Analytical Balance ID 30.10 Lab Amb. Temp, F _73 Rel Humidity in Lab, % OHAUS__________________ Date Run Identification Filters 1 Filter ID # 106 Initial Weight, grams - Date/Time 7/10/00 3.7677 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams 3.7679 0.0002 Wash Bottle ID# Acetone Wash F6 Volume of Acetone Used, ml Initial Weight, grams - Date/Time 7/10/00 100 72.7642 Final Weight, grams - Date/Time 7/10/00 72.7709 Total Weight of Acetone Wash, grams 0.0067 Wash Bottle ID# Acetone Blank 1 Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 74.0301 74.0303 Total Weight of Acetone blank, grams 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0071 2 109 3.5898 3.5899 0.0001 F7 100 72.7865 72.7935 0.0070 1 74.0301 74.0303 0.0002 0.0002 0.0073 48 July 10, 2000 3 110 3.7707 3.7710 0.0003 FI 3 100 71.8990 71.9074 0.0084 1 74.0301 74.0303 0.0002 0.0002 0.0089 212 ABD00048923 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, Silo #676 Job No.: 20148 City/State Aberdeen, MississippiAnalyst: Tim Draheim Barometric Pressure.in hg Analytical Balance ID 30.10 OHAUS Lab Amb. Temp, F 73 Rel Humidity in Lab, % 48 Date July 10, 2000 Run Identification Filter ID # Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Filters 1 119 3.7869 3.7871 Total Weight of Particulate on Filter, grams 0.0002 Wash Bottle ID # Volume of Acetone Used, ml Acetone Wash F15 100 Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone Wash, grams 73.3161 73.3255 0.0094 Wash Bottle ID# Acetone Blank 1 Initial Weight, grams - Date/Time 7/10/00 74.0301 Final Weight, grams - Date/Time 7/10/00 74.0303 Total Weight of Acetone blank, grams 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0098 2 113 3.7650 3.7653 0.0003 F19 100 73.6339 73.6439 0.0100 1 74.0301 74.0303 0.0002 0.0002 0.0105 3 118 3.7866 3.7873 0.0007 F20 100 71.2368 71.2423 0.0055 1 74.0301 74.0303 0.0002 0.0002 0.0064 213 ABD00048924 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, Silo #677 Job No.: 20148 City/State Aberdeen, Mississippi Analyst: Tim Draheim Barometric Pressure,in hg Analytical Balance ID 30.10 OHAUS Lab Amb. Temp, F 73 Rel Humidity in Lab, % _48_____ Date July 10, 2000 Run Identification Filters 1 Filter ID# 104 Initial Weight, grams - Date/Time 7/10/00 3.7847 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams 3.7852 0.0005 Wash Bottle ID # Acetone Wash Sill Volume of Acetone Used, ml 100 Initial Weight, grams - Date/Time 7/10/00 81.0765 Final Weight, grams - Date/Time 7/10/00 81.0932 Total Weight of Acetone Wash, grams 0.0167 Wash Bottle ID# Initial Weight, grams - Date/Time 7/10/00 Acetone Blank 1 74.0301 Final Weight, grams - Date/Time 7/10/00 74.0303 Total Weight of Acetone blank, grams 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0174 2 105 3.7107 3.7110 0.0003 S110 100 75.8125 75.8240 0.0115 1 74.0301 74.0303 0.0002 0.0002 0.0120 3 530 3.6624 3.6627 0.0003 F5 100 71.5987 71.6134 0.0147 1 ,74.0301 74.0303 0.0002 0.0002 0.0152 214 ABD00048925 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, Silo #678 Job No.: 20148 City/State Aberdeen, Mississippi Barometric Pressure,In hg Analytical Balance ID 30,10 Lab Amb. Temp, F 73 OHAUS__________________ Analyst: Tim Draheim Rel Humidity in Lab, % Date 48 July 10,2000 Run Identification Filters 1 2 Filter ID # 116 117 Initial Weight, grams - Date/Time 7/10/00 3.7639 3.8012 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams 3.7640 0.0001 3.8014 0.0002 Wash Bottle ID # Acetone Wash SI 05 SI 06 Volume of Acetone Used, ml 100 100 , Initial Weight, grams - Date/Time 7/10/00 77.8309 79.9284 Final Weight, grams - Date/Time 7/10/00 77.8367 79.9344 Total Weight of Acetone Wash, grams 0.0058 0.0060 Wash Bottle ID # Acetone Blank 1 1 Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 74.0301 74.0303 74.0301 74.0303 Total Weight of Acetone blank, grams 0.0002 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of rrom Unannlf Particulate Illllllllllllllllllllllll 0.0002 0.0002 0.0061 0.0064 3 123 3.7530 3.7533 0.0003 SI 08 100 79.1973 79.2063 0.0090 1 74.0301 74.0303 0.0002 0.0002 0.0095 215 ABD00048926 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, Silo #679 Job No.: 20148 City/State Aberdeen, MississippiAnalyst: Tim Draheim Barometric Pressure,in hg Analytical Balance ID 30.10 Lab Amb. Temp, F 73 OHAUS__________________ Rel Humidity in Lab, % Date 48 July 10,2000 Run Identification Filters 1 Filter ID# 107 Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 3.8034 3.8035 Total Weight of Particulate on Filter, grams 0.0001 Wash Bottle ID # Acetone Wash FI Volume of Acetone Used, ml 100 Initial Weight, grams - Date/Time 7/10/00 75.5733 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone Wash, grams 75.6012 0.0279 Wash Bottle ID# Acetone Blank 1 Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone blank, grams 74.0301 74.0303 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0282 2 108 3.7725 3.7726 0.0001 F2 100 74.5833 74.6017 0.0184 1 74.0301 74.0303 0.0002 0.0002 0.0187 3 111 3.5840 3.5842 0.0002 F4 100 74.2170 74.2428 0.0258 1 74.0301 74.0303 0.0002 0.0002 0.0262 216 ABD00048927 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, Silo #680 Job No.: 20148 City/State Aberdeen, Mississippi Analyst: Tim Draheim Barometric Pressure,in hg Analytical Balance ID 30.10 OHAUS Lab Amb. Temp, F 73 Rel Humidity in Lab, % 48 Date July 10,2000 Run Identification Filters 1 Filter ID # 112 Initial Weight, grams - Date/Time 7/10/00 3.7848 Final Weight, grams - Date/Time 7/10/00 3.7848 Total Weight of Particulate on Filter, grams 0.0003 Wash Bottle ID # Acetone Wash F15 Volume of Acetone Used, ml 100 Initial Weight, grams - Date/Time 7/10/00 73.3176 Final Weight, grams - Date/Time 7/10/00 73.3273 Total Weight of Acetone Wash, grams 0.0097 Wash Bottle ID # Acetone Blank 1 Initial Weight, grams - Date/Time 7/10/00 74.0301 Final Weight, grams - Date/Time 7/10/00 74.0303 Total Weight of Acetone blank, grams 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0102 2 114 3.6650 3.6654 0.0004 F19 100 73.6360 73.6399 0.0039 1 74.0301 74.0303 0.0002 0.0002 0.0045 3 115 3.6389 3.6391 0.0002 F20 100 71.2383 71.2420 0.0037 1 74.0301 74.0303 0.0002 0.0002 0.0041 217 ABD00048928 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, Silo #687 Job No.: 20148 City/State Aberdeen, Mississippi Analyst: Tim Draheim Barometric Pressure.in hg Analytical Balance ID 30.10 OHAUS Lab Amb. Temp, F 73 Rel Humidity in Lab, % 48 Date July 10, 2000 Run Identification Filter ID # Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams Filters 1 529 3.8010 3.8015 0.0005 Wash Bottle ID # Volume of Acetone Used, mi Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone Wash, grams Acetone Wash F5 100 71.5991 71.6081 0.0090 Wash Bottle ID # Acetone Blank 1 Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone blank, grams 74.0301 74.0303 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0097 2 124 3.7587 3.7589 0.0002 F17 100 74.5457 74.5525 0.0068 1 74.0301 74.0303 0.0002 0.0002 0.0072 3 125 3.7454 3.7459 0.0005 FI 3 100 74.4008 74.4092 0.0084 1 74.0301 74.0303 0.0002 0.0002 0.0091 218 ABD00048929 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, Silo #688 Job No.: 20148 City/State Aberdeen, Mississippi Analyst: Tim Draheim Barometric Pressure,in hg Analytical Balance ID 30.10Lab Amb. Temp, F 73 OHAUS__________________ Rel Humidity in Lab, % Date 48 July 10,2000 Run identification Filter ID # Filters 1 120 Initial Weight, grams - Date/Time 7/10/00 3.7625 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams 3.7630 0.0005 Wash Bottle ID # Acetone Wash F10 Volume of Acetone Used, ml Initial Weight, grams - Date/Time 7/10/00 100 71.2480 Final Weight, grams - Date/Time 7/10/00 71.2558 Total Weight of Acetone Wash, grams 0.0078 Wash Bottle ID# Acetone Blank 1 Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 74.0301 74.0303 Total Weight of Acetone blank, grams 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0085 2 121 3.7464 3.7467 0.0003 F11 100 71.4565 71.4686 0.0121 1 74.0301 74.0303 0.0002 0.0002 0.0126 3 122 3.7667 3.7671 0.0004 F12 100 71.4998 71.5135 0.0137 1 74.0301 74.0303 0.0002 0.0002 0.0143 219 ABD00048930 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, #10 Cyclone Dryer Job No.: 20148 City/State Aberdeen, Mississippi Analyst: Tim Draheim Barometric Pressure.in hg Analytical Balance ID 30.10 Lab Amb. Temp, F 73 OHAUS__________________ Rel Humidity in Lab, % Date 48 July 10,2000 Run Identification Filters 1 Filter ID# Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 503 3.7582 3.7606 Total Weight of Particulate on Filter, grams 0.0024 Wash Bottle ID # Acetone Wash F13 Volume of Acetone Used, ml 100 Initial Weight, grams - Date/Time 7/10/00 74.3974 Final Weight, grams - Date/Time 7/10/00 74.4099 Total Weight of Acetone Wash, grams 0.0125 Wash Bottle ID # Acetone Blank 1 Initial Weight, grams - Date/Time 7/10/00 74.0301 Final Weight, grams - Date/Time 7/10/00 74.0303 Total Weight of Acetone blank, grams 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0151 2 505 3.7980 3.8021 0.0041 Sill 100 81.0781 81.1390 0.0609 1 74.0301 74.0303 0.0002 0.0002 0.0652 3 504 3.7664 3.7714 0.0050 SI 08 100 79.1979 79.2132 0.0153 1 74.0301 74.0303 0.0002 0.0002 0.0205 220 ABD00048931 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, #11 Cyclone Dryer Job No.: 20148 City/State Aberdeen, Mississippi Analyst: Tim Draheim Barometric Pressure,in hg Analytical Balance ID 30.10 OHAUS Lab Amb. Temp, F 73 Rel Humidity in Lab, % 48 Date July 10, 2000 Run Identification Filters 1 Filter ID# Initial Weight, grams - Date/Time 7/10/00 116 3.7681 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particuiate on Filter, grams 3.7695 0.0014 Wash Bottle ID# Acetone Wash SI 05 Volume of Acetone Used, ml 100 Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone Wash, grams 77.0775 77.9333 0.0158 Wash Bottle ID # Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone blank, grams Acetone Blank 1 74.0301 74.0303 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0174 2 117 3.7437 3.7452 0.0015 S110 100 75.9403 75.9596 0.0193 1 74.0301 74.0303 0.0002 0.0002 0.0210 3 502 3.7817 3.7847 0.0030 SI 06 100 79.9298 79.9440 0.0142 1 74.0301 74.0303 0.0002 0.0002 0.0174 221 ABD00048932 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, Fluid Bed Dryer Job No.: 20148 City/State Aberdeen, MississippiAnalyst: Tim Draheim Barometric Pressure,in hg Analytical Balance ID 30.10 Lab Amb. Temp, F 73 OHAUS___________________ Rel Humidity in Lab, % Date 48 July 10,2000 Run Identification Fitter ID# Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams Filters 1 507 3.8116 3.8129 0.0013 Wash Bottle ID # Volume of Acetone Used, ml l Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone Wash, grams Acetone Wash F5 100 71.5982 71.6161 0.0179 Wash Bottle ID# Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone blank, grams Acetone Blank 1 74.0301 74.0303 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0194 2 508 3.7748 3.7752 0.0004 F6 100 72.7658 72.7950 0.0292 1 74.0301 74.0303 0.0002 0.0002 0.0298 3 509 3.7884 3.7889 0.0005 F7 100 72.7886 72.7930 0.0044 1 74.0301 74.0303 0.0002 0.0002 0.0051 222 ABD00048933 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, Ventilation Baghouse Job No.: 20148 City/State Aberdeen, MississippiAnalyst: Tim Draheim Barometric Pressure,in hg Analytical Balance ID 30.10 Lab Amb. Temp, F 73 OHAUS__________________ Rel Humidity in Lab, % 48 Date July 10,2000 Run Identification Filter ID # Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams Filters 1 521 3.7620 3.7664 0.0044 Wash Bottle ID# Volume of Acetone Used, ml Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Acetone Wash F8 100 72.0490 72.0636 Total Weight of Acetone Wash, grams 0.0146 Wash Bottle ID # Initial Weight, grams - Date/Time 7/10/00 Acetone Blank 1 74.0301 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone blank, grams 74.0303 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0192 2 523 3.7790 3.7826 0.0036 F9 100 74.0290 74.0652 0.0362 1 74.0301 74.0303 0.0002 0.0002 0.0400 3 524 3.6290 3.6312 0.0022 F10 100 72.6876 72.7095 0.0235 1 74.0301 74.0303 0.0002 0.0002 0.0259 223 ABD00048934 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, #4 Rotary Dryer Job No.: 20148 City/State Aberdeen, Mississippi Analyst: Tim Draheim Barometric Pressure.in hg Analytical Balance ID 30.10 OHAUS Lab Amb. Temp, F 73 Rel Humidity in Lab, % 48 Date July 10, 2000 Run Identification Filter ID # Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams Filters 1 500 3.7107 3.7136 0.0029 Wash Bottle ID # Volume of Acetone Used, ml Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone Wash, grams Acetone Wash F7 100 72.7664 72.7751 0.0087 Wash Bottle ID # Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone blank, grams Acetone Blank 1 74.0301 74.0303 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0118 2 501 3.7670 3.7704 0.0034 F8 100 74.1224 74.1294 0.0068 1 74.0301 74.0303 0.0002 0.0002 0.0104 3 506 3.6226 3.6266 0.0040 F9 100 74.0328 74.0432 0.0104 1 74.0301 74.0303 0.0002 0.0002 0.0146 224 ABD00048935 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, #5 Rotary Dryer Job No.: 20148 City/State Aberdeen, Mississippi_________________ Analyst: Tim Draheim Barometric Pressure,in hg Analytical Balance ID 30.10 Lab Amb. Temp, F 73 OHAUS__________________ Rel Humidity in Lab, % Date 48 July 10,2000 Run Identification Filter ID# Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams Filters 1 510 3.5890 3.5898 0.0008 2 511 3.7527 3.7532 0.0005 3 512 3.7693 3.7694 0.0001 ;T;-;T;-;T;XX:;X;I;*; Wash Bottle ID# :;>T: ;X;^ : ^ f; ; :->:-:l- T*: -.-M-1-. Volume of Acetone Used, ml Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone Wash, grams FI 100 75.5700 75.5790 0.0090 Wash Bottle ID# Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Acetone Blank 1 74.0301 74.0303 Total Weight of Acetone blank, grams 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of i-ront riaii Particulate 0.0002 0.0100 F2 100 74.5787 74.6084 0.0297 1 74.0301 74.0303 0.0002 0.0002 0.0304 F4 100 74.2130 74.2179 0.0049 1 74.0301 74.0303 0.0002 0.0002 0.0052 225 ABD00048936 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, #6 Rotary Dryer Job No.: 20148 City/State Aberdeen, MississippiAnalyst: Barometric Pressure,in hg Analytical Balance ID 30,10 Lab Amb. Temp, F 73 OHAUS___________________ Tim Draheim Rel Humidity in Lab, % 48 Date July 10,2000 Run Identification Fitter ID# Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams Filters 1 513 3.6913 3.6992 0.0079 Wash Bottle ID # Volume of Acetone Used, ml Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone Wash, grams Acetone Wash F11 100 73.0473 73.0490 0.0017 Wash Bottle ID # Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone blank, grams Acetone Blank 1 74.0301 74.0303 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0096 2 514 3.7374 3.7428 0.0054 F12 100 73.6318 73.6401 0.0083 1 74.0301 74.0303 0.0002 0.0002 0.0139 3 517 3.7890 3.7926 0.0036 F15 100 73.3205 73.3318 0.0113 1 74.0301 74.0303 0.0002 iiiiiwiaii 0.0002 0.0151 226 ABD00048937 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, #7 Rotary Dryer Job No.: 20148 City/State Aberdeen, Mississippi Analyst: Tim Draheim Barometric Pressure,in hg Analytical Balance ID 30.10 Lab Amb. Temp, F 73 OHAUS__________________ Rel Humidity in Lab, % Date 48 July 10,2000 Run Identification Filters 1 Filter ID # 518 Initial Weight, grams - Date/Time 7/10/00 3.7530 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams 3.7553 0.0023 Wash Bottle ID# Volume of Acetone Used, ml . Initial Weight, grams - Date/Time 7/10/00 Acetone Wash F17 100 74.5449 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone Wash, grams 74.5752 0.0303 Wash Bottle ID # Acetone Blank 1 Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 74.0301 74.0303 Total Weight of Acetone blank, grams 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0328 2 520 3.7800 3.7865 0.0065 F18 100 74.1343 74.1694 0.0351 1 74.0301 74.0303 0.0002 0.0002 0.0418 3 522 3.6500 3.6567 0.0067 F19 100 73.6369 73.6692 0.0323 1 74.0301 74.0303 0.0002 0.0002 0.0392 227 ABD00048938 Laboratory Data Particulate Matter Gravimetric Analysis Client: Georgia Gulf, #8 Rotary Dryer Job No.: 20148 City/State Aberdeen, MississippiAnalyst: Barometric Pressure,in hg Analytical Balance ID 30.10 Lab Amb. Temp, F 73 OHAUS Run Identification Filter ID# Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Particulate on Filter, grams Filters 1 515 3.6819 3.6835 0.0016 Wash Bottle ID # Volume of Acetone Used, ml Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone Wash, grams Acetone Wash F3 100 73.4373 73.4450 0.0077 Wash Bottle ID# Initial Weight, grams - Date/Time 7/10/00 Final Weight, grams - Date/Time 7/10/00 Total Weight of Acetone blank, grams Acetone Blank 1 74.0301 74.0303 0.0002 Total Weight of Residue in Acetone Wash, grams (ml used) * (acetone blank, g/ml) Total Weight of Particulate Matter Collected grams Total Weight of Front Half Particulate 0.0002 0.0095 Tim Draheim Rel Humidity in Lab, % 48 Date July 10, 2000 2 516 3.6490 3.6558 0.0068 F14 100 76.0553 76.0759 0.0206 1 74.0301 74.0303 0.0002 3 519 3.5790 3.5839 0.0049 F20 100 75.2408 75.2524 0.0116 1 74.0301 74.0303 0.0002 0.0002 0.0276 0.0002 0.0167 228 ABD00048939 No. 3 Boiler Instrument Calibration Instrumentation Calibration ABD00048940 Client- Georgia Gulf - Aberdeen, Mississippi No. 3 Boiler Test No. 1 Job No.: Date: 20148 June 29,2000 Run NOx CO 02 C02 Average Zero System Average Upscale System Calibration Response (ppm) Calibration Response (ppm) 0.13 25.06 0.17 14.62 0.07 10.19 0.04 9.76 Upscale Gas (ppm) 25.20 14.89 10.30 9.89 Uncorrected Average Corrected Average Concentration indicated by Concentration indicated by Analyzer (ppm) Analyzer (ppm) 19.35 1943 5.03 5.01 14.01 14.19 3.26 3.28 | RunS NOx CO 02 C02 Test No. 2 Corrected EfftuBfttGdeGOntvfrtfation.tity has* ppfn Average Zero System Average Upscale System Calibration Response (ppm) Calibrabon Response (ppm) Upscale Gas (ppm) Uncorrected Average Corrected Average Concentration indicated by Concentration indicated by Analyzer (ppm) Analyzer (ppm) 0.11 25.02 25.20 19.59 19.71 0.15 14.59 14.89 6.62 6.67 0.07 10.17 10.30 14.00 14.21 0.02 9.73 9.89 3.27 3.31 RunS NOx CO 02 | C02 Test No. 3 Corrected EftluontGas Concentration. dry basis ppm Average Zero System Average Upscale System Calibration Response (ppm) Calibrabon Response (ppm) Upscale Gas (ppm) Uncorrected Average Corrected Average Concentration indicated by Concentration indicated by Analyzer (ppm) Analyzer (ppm) 0.11 24.99 25.20 19.75 1989 0.16 14.63 14.89 5.54 5.54 0.06 10.12 10.30 14.01 14.28 0.03 9.76 9.89 3.28 3.30 230 ABD00048941 Analyzer Calibration Data Source: Geogia Gulf - No. 3 Boiler Test Personnel: G. Corley Test No.: Date: 1-3 6/29/00 Gas ID: NOx Span: 46.61 Zero Gas Mid-Ranqe Gas High Range Gas Cylinder Value (ppm) 0.00 25.20 46.61 Analyzer Calibration Response (ppm) 0.05 25.14 46.45 Absolute Difference (ppm) 0.1 -0.1 -0.2 Difference % of Span 0.11 -0.13 -0.34 Gas ID: 02 Span: 20.90 Zero Gas Mid-Range Gas High Range Gas Cylinder Value (%) 0.00 10.30 20.90 Analyzer Calibration Response (%) 0.06 10.28 20.83 Absolute Difference (%) 0.1 0.0 -0.1 Difference % of Span 0.29 -0.10 -0.33 Gas ID: C02 Span: 20.13 Zero Gas Mid-Range Gas High Range Gas Cylinder Value (%> 0.00 9.89 20.13 Analyzer Calibration Response (%) 0.00 9.77 20.04 Absolute Difference (%) 0.0 -0.1 -0.1 Difference % of Span 0.00 -0.60 -0.45 Gas ID: CO Span: 90.92 Zero Gas Low-Range Gas Mid-Range Gas High Range Gas Cylinder Value (ppm) 0.00 14.89 49.01 90.92 Analyzer Calibration Response (ppm) 0.21 14.93 49.21 91.07 Absolute Difference (ppm) 0.21 0.04 0.20 0.15 Difference % of Span 0.23 0.04 0.22 0.16 231 ABD00048942 . Test No. 1 System Calibration Data Source: Geogia Gulf - No. 3 Boiler Test Personnel: L. Bean Test No.: Date: 1 6/29/00 Gas ID: NOx Span: 46.61 Zero Gas Mid-Range Gas Analyzer Calibration Response 0.05 25.14 Initial Values System System Calibration Cal. Bias Response % of Span 0.12 0.2 25.05 -0.2 Final Values System System Calibration Cal. Bias Response % of Span 0.14 0.2 25.06 -0.2 Drift % of Span 0.04 0.02 Gas ID: 02 Span: 20.90 Zero Gas Mid-Range Gas Analyzer Calibration Response 0.06 10.28 Initial Values System System Calibration Cal. Bias Response % of Span 0.07 0.0 10.20 -0.4 Final Values System System Calibration Cal. Bias Response % of Span 0.07 0.0 10.18 -0.5 Drift % of Span 0.00 -0.10 Gas ID: C02 Span: 20.13 Zero Gas Mid-Range Gas Analyzer Calibration Response 0.00 9.77 Initial Values System System Calibration Cal. Bias Response % of Span 0.02 0.1 9.75 -0.1 Final Values System System Calibration Cal. Bias Response % of Span 0.05 0.2 9.76 0.0 Drift % of Span 0.15 0.05 Gas ID: CO Span: 90.92 Zero Gas Low-Range Gas Analyzer Calibration Response 0.21 14.93 Initial Values System System Calibration Cal. Bias Response % of Span 0.17 -0.04 14.65 -0.31 Final Values System System Calibration Cal. Bias Response % of Span 0.16 -0.05 14.58 -0.38 Drift % of Span -0.01 -0.08 232 ABD00048943 Test No. 2 System Calibration Data Source: Geogia Gulf - No. 3 Boiler Test Personnel: L. Bean Test No.: Date: 2 6/29/00 Gas ID: NOx Span: 46.61 Zero Gas Mid-Ranqe Gas Analyzer Calibration Response 0.05 25.14 Initial Values System System Calibration Cal. Bias Response % of Span 0.12 0.2 25.05 -0.2 Final Values System System Calibration Cal. Bias Response % of Span 0.10 0.1 24.98 -0.3 Drift % of Span -0.04 -0.15 Gas ID: 02 Span: 20.90 Zero Gas Mid-Ranqe Gas Analyzer Calibration Response 0.06 10.28 Initial Values System System Calibration Cal. Bias Response % of Span 0.07 0.0 10.20 -0.4 Final Values System System Calibration Cal. Bias Response % of Span 0.07 0.0 10.14 -0.7 Drift % of Span 0.00 -0.29 Gas ID: C02 Span: 20.13 Zero Gas Mid-Ranqe Gas Analyzer Calibration Response 0.00 9.77 Initial Values System System Calibration Cal. Bias Response % of Span 0.02 0.1 9.75 -0.1 Final Values System System Calibration Cal. Bias Response % of Span 0.01 0.0 9.71 -0.3 Drift % of Span -0.05 -0.20 Gas ID: CO Span: 90.92 Zero Gas Low-Ranqe Gas Analyzer Calibration Response 0.21 14.93 Initial Values System System Calibration Cal. Bias Response % of Span 0.17 -0.04 14.65 -0.31 Final Values System System Calibration Cal. Bias Response % of Span 0.12 -0.10 14.52 -0.45 Drift % of Span -0.05 -0.14 233 ABD00048944 Test No. 3 System Calibration Data Source: Geogia Gulf - No. 3 Boiler Test Personnel: L. Bean Test No.: Date: 3 6/29/00 Gas ID: NOx Span: 46.61 Zero Gas Mid-Ranqe Gas Analyzer Calibration Response 0.05 25.14 Initial Values System System Calibration Cal. Bias Response % of Span 0.12 0.2 25.05 -0.2 Final Values System System Calibration Cal. Bias Response % of Span 0.10 0.1 24.93 -0.5 Drift % of Span -0.04 -0.26 Gas ID: 02 Span: 20.90 Zero Gas Mid-Range Gas Analyzer Calibration Response 0.06 10.28 Initial Values System System Calibration Cal. Bias Response % of Span 0.07 0.0 10.20 -0.4 Final Values System System Calibration Cal. Bias Response % of Span 0.04 -0.1 10.03 -1.2 Drift % of Span -0.14 -0.81 Gas ID: C02 Span: 20.13 Zero Gas Mid-Range Gas Analyzer Calibration Response 0.00 9.77 initial Values System System Calibration Cal. Bias Response % of Span 0.02 0.1 9.75 -0.1 Final Values System System Calibration Cal. Bias Response % of Span 0.03 0.1 9.76 0.0 Drift % of Span 0.05 0.05 Gas ID: CO Span: 90.92 Zero Gas Low-Range Gas Analyzer Calibration Response 0.21 14.93 Initial Values System System Calibration Cal. Bias Response % of Span 0.17 -0.04 14.65 -0.31 Final Values System System Calibration Cal. Bias Response % of Span 0.15 -0.07 14.61 -0.35 Drift % of Span -0.02 -0.04 234 ABD00048945 No. 4 Boiler Instrument Calibration Instrumentation Calibration ABD00048946 Client: RunO NOx CO 02 C02 Georgia Gulf - Aberdeen, Mississippi No. 4 Boiler Job No.: Date: 20148 June 29,2000 Test No. 1 Corrected Effluent Gas Concentration, dry basis* ppm Average Zero System Average Upscale System Calibration Response (ppm) Calibration Response (ppm) Upscale Gas (ppm) Unconected Average Corrected Average Concentration Indicated by Concentration Indicated by Analyzer (ppm) Analyzer (ppm) 0.06 46.10 46.61 59.94 60.63 0.13 14.54 14.89 0.82 0.71 004 10.12 10.30 5.87 5.96 0.03 9.74 9.89 8.39 8.51 ^ Run# NOx CO 02 002 Test No. 2 Corrected EffiueMOo* Concentration, dry basis. ppm Average Zero System Average Upscale System Calibration Response (ppm) Calibration Response (ppm) Upscale Gas (ppm) Uncorrected Average Corrected Average Concentration indicated by Concentration indicated by Analyzer (ppm) Analyzer (ppm) 007 46.09 46.61 54.68 55.31 0.14 1454 14.89 0.81 0.69 006 10.20 10.30 6.85 6.90 0.03 9.74 9.89 7.80 7.91 tf Rund NOx CO 02 C02 Test No. 3 Corrected Effluent Qu Concentration, dry Oasis, ppm Average Zero System Average Upscale System Calibration Response (ppm) Calibration Response (ppm) Upscale Gas (ppm) Uncorrected Average Corrected Average Concentration indicated by Concentration indicated by Analyzer (ppm) Anaiyzer (ppm) 0.09 46.07 46.61 60.62 61.36 0.14 14.56 14.89 045 0.32 0.07 10.15 10.30 5.72 5.77 0.03 9.75 9.89 8.47 6.59 236 ABD00048947 Analyzer Calibration Data Source: Geogia Gulf - No. 4 Boiler Test Personnel: G. Corley Test No.: Date: 1-3 ' 6/29/00 Gas ID: NOx Span: 46.61 Zero Gas Mid-Ranoe Gas High Range Gas Cylinder Value (PPm) 0.00 25.20 46.61 Analyzer Calibration Response (PPm) 0.05 25.14 46.45 Absolute Difference (PPm) 0.1 -0.1 -0.2 Difference % of Span 0.11 -0.13 -0.34 Gas ID: 02 Span: 20.90 Zero Gas Mid-Range Gas High Range Gas Cylinder Value (%) 0.00 10.30 20.90 Analyzer Calibration Response (%) 0.06 10.28 20.83 Absolute Difference (%) 0.1 0.0 -0.1 Difference % of Span 0.29 -0.10 -0.33 Gas ID: C02 Span: 20.13 Zero Gas Mid-Range Gas High Range Gas Cylinder Value (%) 0.00 9.89 20.13 Analyzer Calibration Response <%) 0.00 9.77 20.04 Absolute Difference (%) 0.0 -0.1 -0.1 Difference % of Span 0.00 -0.60 -0.45 Gas ID: CO Span: 90.92 Zero Gas Low-Range Gas Mid-Range Gas High Range Gas Cylinder Value (ppm) 0.00 14.89 49.01 90.92 Analyzer Calibration Response (ppm) 0.21 14.93 49.21 91.07 Absolute Difference (ppm) 0.21 0.04 0.20 0.15 Difference % of Span 0.23 0.04 0.22 0.16 237 ABD00048948 Test No. 1 System Calibration Data Source: Geogia Gulf > No. 4 Boiler Test Personnel: L. Bean Test No.: Date: 1 6/29/00 Gas ID: NOx Span: 46.61 Zero Gas Hiqh-Ranqe Gas Analyzer Calibration Response 0.05 46.45 Initial Values System System Calibration Cal. Bias Response % of Span 0.12 0.2 46.14 -0.7 Final Values System System Calibration Cal. Bias Response % of Span 0.03 0.0 46.06 -0.8 Drift % of Span -0.19 -0.17 Gas ID: 02 Span: 20.90 Zero Gas Mid-Range Gas Analyzer Calibration Response 0.06 10.28 Initial Values System System Calibration Cal. Bias Response % of Span 0.07 0.0 10.20 -0.4 Final Values System System Calibration Cal. Bias Response % of Span 0.01 -0.2 10.04 -1.1 Drift % of Span -0.29 -0.77 Gas ID: C02 Span: 20.13 Zero Gas Mid-Range Gas Analyzer Calibration Response 0.00 9.77 Initial Values System System Calibration Cal. Bias Response % of Span 0.02 0.1 9.75 -0.1 Final Values System System Calibration Cal. Bias Response % of Span 0.03 0.1 9.72 -0.2 Drift % of Span 0.05 -0.15 Gas ID: CO Span: 90.92 Zero Gas Low-Range Gas Analyzer Calibration Response 0.21 14.93 Initial Values System System Calibration Cal. Bias Response % of Span 0.17 -0.04 14.65 -0.31 Final Values System System Calibration Cal. Bias Response % of Span 0.09 -0.13 14.43 -0.55 Drift % of Span -0.09 -0.24 238 ABD00048949 Test No. 2 System Calibration Data Source: Geogia Gulf - No. 4 Boiler Test Personnel: l. Bean Test No.: Date: 2 6/29/00 Gas ID: NOx Span: 46.61 Zero Gas Hiqh-Ranqe Gas Analyzer Calibration Response 0.05 46.45 Initial Values System System Calibration Cal. Bias Response. % of Span 0.12 0.2 46.14 -0.7 Final Values System System Calibration Cal. Bias Response % of Span 0.02 -0.1 46.04 -0.9 Drift % of Span -0.21 -0.21 Gas ID: 02 Span: 20.90 Zero Gas Mid-Ranqe Gas Analyzer Calibration Response 0.06 10.28 Initial Values System System Calibration Cal. Bias Response % of Span 0.07 0.0 10.20 -0.4 Final Values System System Calibration Cal. Bias Response % of Span 0.04 -0.1 10.19 -0.4 Drift % of Span -0.14 -0.05 Gas ID: C02 Span: 20.13 Zero Gas Mid-Ranqe Gas Analyzer Calibration Response 0.00 9.77 Initial Values System System Calibration Cal. Bias Response % of Span 0.02 0.1 9.75 -0.1 Final Values System System Calibration Cal. Bias Response % of Span 0.04 0.2 9.73 -0.2 Drift % of Span 0.10 -0.10 Gas ID: CO Span: 90.92 Zero Gas Low-Ranqe Gas Analyzer Calibration Response 0.21 14.93 Initial Values System System Calibration Cal. Bias Response % of Span 0.17 -0.04 14.65 -0.31 Final Values System System Calibration Cal. Bias Response % of Span 0.10 -0.12 14.43 -0.55 Drift % of Span -0.08 -0.24 239 ABD00048950 Test No. 3 System Calibration Data Source: Geogia Gulf - No. 4 Boiler Test Personnel: L. Bean Test No.: Date: .. 3 6/29/00 Gas ID: NOx Span: 46.61 Zero Gas Hiqh-Ranae Gas Analyzer Calibration Response 0.05 46.45 Initial Values System System Calibration Cal. Bias Response % of Span 0.12 0.2 46.14 -0.7 Final Values System System Calibration Cal. Bias Response % of Span 0.05 0.0 46.00 -1.0 Drift % of Span -0.15 -0.30 Gas ID: 02 Span: 20.90 Zero Gas Mid-Range Gas Analyzer Calibration Response 0.06 10.28 Initial Values System System Calibration Cal. Bias Response % of Span 0.07 0.0 10.20 -0.4 Final Values System System Calibration Cal. Bias Response % of Span 0.06 0.0 10.10 -0.9 Drift % of Span -0.05 -0.48 Gas ID: C02 Span: 20.13 Zero Gas Mid-Range Gas Analyzer Calibration Response 0.00 9.77 Initial Values System System Calibration Cal. Bias Response % of Span 0.02 0.1 9.75 -0.1 Final Values System System Calibration Cal. Bias Response % of Span 0.03 0.1 9.74 -0.1 Drift % of Span 0.05 -0.05 Gas ID: CO Span: 90.92 Zero Gas Low-Range Gas Analyzer Calibration Response 0.21 14.93 Initial Values System System Calibration Cal. Bias Response % of Span 0.17 -0.04 14.65 -0.31 Final Values System System Calibration Cal. Bias Response % of Span 0.11 -0.11 14.47 -0.51 Drift % of Span -0.07 -0.20 240 ABD00048951 Calibration Gas Protocol Certificates ABD00048952 IBSpecialty Gases 5480 Hamilton Blvd. Th^BAL 36582 P.O^B90969 Mobile, AL 36619 Phone: (334) 653-2500 FAX: (334) 653-2530 Certificate of Analysis: E.P.A. Protocol Gas Mixture Cylinder No : Cylinder Pressure: Certification Date CC14785 2000PS1G 4/25/00 Order No. Expiration Date: Laboratory: 388470 4/25/02 ASG-MOBiLE Reference Standard Information: Type NTRM81684 Component NITRIC OXIDE Instrumentation: Cvl. Number CC66785 Concentration 96.9PPM Instrument/Model/Serial No. ECOPhysics/CLD700EL/72411 Analytical Principle Chemiluminescence Analytical Methodology does not require correction for analytical interferences. Certified Concentrations: Component MTR\C OXIDE MO> NITROGEN Analytical Results: Concentration 46.61 PPM 46.61 PPM Balance Accuracy Procedure G1 1st Component: 1 st Analysis Date: R 96.80 S 47.00 2 0.000 NITRIC OXIDE 4/18/00 S 2 R 46.70 0.000 96.90 2 R S 0.000 96.90 46.B0 Cone Cone Cone AVG: 46.75 47.00 46.80 67.52 2nd Analysis Date: 4/25/00 R 96.70 S 46.20 7 0.000 S 46.30 2 0.000 R 96.90 2 0.000 R 96.90 S 46.50 Cone Cone Cone AVG: 46.30 46.30 46.50 46.37 Certification performed in accordance with "EPA Traceability Protocol (Sept. 1997)" using the assay procedures listed. Do not use cylinder below 150 psig. Dp '-BmI ciu t- H mj c-Iju Approved for Release Page 1 242 ABD00048953 ESpecialty Gases 5480 Hamilton Blvd. Tn^^AL 36562 P.O^Br90969 Mobile, AL 36619 Phone: (334) 653-2500 FAX: (334) 653-2530 Certificate of Analysis: E.P.A. Protocol Gas Mixture Cylinder No: Cylinder Pressure: Certification Date CC96317 2000PSIG 4/25/00 Order No. Expiration Date: Laboratory: 388470 4/25/02 ASG-MOBILE Reference Standard Information: Type NTRM81684 Component NITRIC OXIDE Instrumentation: Cvi. Number CC66785 Concentration 96.9PPM Instrument/Model/Serial No. ECOPhysics/CLD700EL/72411 Analytical Principle Chemiluminescence Analytical Methodology does not require correction for analytical interferences. Certified Concentrations: Component NITRIC UXYIiLnr; NO> NITROGEN Analytical Results: Concentration 24.73 PPM 25,20 PPM Balance Accuracy Procedure 1st Component: iNlTRlC OXIDE 1 st Analysis Date: 4/18/00 R' 97.10 S 24.90 Z 0.000 S 24.80 Z 0.000 R 96.70 Z 0.000 R 96.80 S 24.80 Cone 24,85 Cone 24.85 Cone AVG: 24.83 24.B4 2nd Analysis.Date:. . 4/25/00 ..... R 97.00 S 24.80 Z 0.000 S 24.50 Z 0.000 R 96.70 Z 0.000 R 96.70 S 24.50 Cone Cone 24.55 Cone AVG: 24.77 24.55 24.62 Certification performed in accordance with "EPA Traceability Protocol (Sept. 1997)" using the assay procedures listed. Do not use cylinder beiow 150 psig. Approved for Release Page 1 243 ABD00048954 BSpecialty Gases Mobile, AL 36619 Phone: (334) 653-2500 FAX: (334) 6532530 Certificate of Analysis: E.P.A. Protocol Gas Mixture Cylinder No: Cylinder Pressure: Certification Date CC51538 2000 psig 7/7/99 Order No. Expiration Date: Laboratory: Reference Standard information: 340910 7/6/02 Ab'G-MQBILE Type NTRMS1675 NTRM82659 Component CARBON DIOXIDE OXYGEN Cvl. Number CC34949 CC45577 Concentration 14.08% 20.11% Instrumentation: Instrument/Model/Serial No. SIEMENS ULTRAMAT 5E K3-684 SIEMENS OXYMAT 5E KE-904 Analytical Principle NDIR PARAMAGNETIC Analytical Methodology does not require correction for analytical interferences. Certified Concentrations: Component CARBON DIOXIDE OXYGEN NITROGEN Cones ntration ao i$%. 4.958 % BALANCE Accuracy Procedure 3 Analytical Results: 1st Component: CARBON. DIOXIDE ' 1st Analysis Date: R 14.08 S 20.12 2 0.000 7/6/99 S 2 R 20.14 0.000 14.08 Z R S 0.000 14.08 20.12 Cone Cone Cone AVG: 20.14 % 20.12 % 20.12 % 20.13 % 2nd Component:: w 1st Analysis Date: R 20.10 S 4.960 2 0.000 7/6/99 S Z R 4.960 0.000 20.12 Z 0.000 R 20.12 S 4.955 Cone Cone Cone AVG: 4.962 % 4,956 % 4.953 % 4.956 % Certification performed in accordance with "EPA Traceability Protocol (Sept. 1997)" using the assay procedures listed. . Do not use cylinder below 150 psig. . \ . ' A\- r. , t \> I p i , TY* UJ-'-.'Y.LT . n . hi p l\A-L'/Lll--- Approved tof Kelease ** Page 1 of 1 ABD00048955 RPCI CHICflSU f-a>C;l~r/r..`''-fPD-i^-ro rial i. u J.W--.* .. ------------------------- -- ....--------- --- ------------------------- T*.- ' -------------------------------- i.| .1 v. .;) r-------------------------------------- TTTT'yr--------'I .t*rr Gl/26/2000 14:21 2056646309 <D tooo AS g dz oc u; ..irji: 2 o n <n cfctii W2^ I [9c CD n SCO |I 9O 4AM Is fc zoo o a CM mm mi ABD00048956 ___ EA FIELD SERVICES O <0 PAGE 01 Q. CL < 5 5 AU P E -I Is *i 21 * ji 2* -o -ia fi 51 II l tf-s 246 01/26/2000 14:21 09 CO W >! < CD < 2 < O OO ill oK ct < CL o iou. hUJ O <\i .i.T.A. 5s o>` 2056646309 V- < ' Ssf C/5 CJ r' ABD00048957 EA FIELD SERVICES PAGE 02 ,1, \ \ l. 247 - N I S TRib Caibrellon Standard hae bean certified per (he September, 1693 EPATroceabflty Protocol, Document EPA-flOOfRBa'224, using PtoMfciia G l. All values certified to bo *f Traceeita. Donoluea IMi cyRnritr below 1.0 Menapaaoal la ., 150p*Jg ABD00048958 248 ABD00048959 Appendix D Equipment Calibration E e >33Oa CL U '6 o15 V0)) t- o lit * 8 I O 5 to ABD00048960 I9 -5 I 0 O<N =X OX a *I 8 1l (O U) o II 2 E 5 li 588 1*3 w a) to >2 5 *1 <d m o cd ^^ dss N~*- (aN"> h* <n> r-Kv P gu > d ui i P> KOu fM CM -- *- -- p UJ Calibrated By:. Wade Drew & <5 ABD00048961 ENTEC S lic e s , Inc. EPA Method 5 Meter Box Calibration Pre-Test Calibration Orifice Method C alibrated Bwada Orew s> o uj > oo o UJ y isf * I 9 S 82 ^rs. <trN> (2) Cl CJ r r 1E O h* 2<N 2M 8 g^ ^R: 2<N 8CN *- 55S 251 ABD00048962 ENTEC S m rces, Inc. EPA Method 5 Meter Box Calibration Pre-Test Calibration Orifice Method Calibrated By:Tlin D ro lie lm a> t LO 20 (9 .o 11 7a5 i8 OZ $? -a2 I= o in -- -- 88 8 Mlo> --_ in 8 2 b| - s (D - n =-Bs1i O^CM 6*<N- O-- '-- B i- I fl s u 5J gO > 2 "31 is. o p> m 5 ri rs o> ni rs E==! |--CM --CM SDOrs 111 J III5 5 3 UJ 252 ABD00048963 o c o w in =1 fa 2g <m o LU CL UJ b_<L) "S LU <aft -- ~ o X0: TO5 1I 8 n .c CD H o (SI CO UJ a I1 o j> 5 (0 fN (6 |?3X >I fN <N 8 > X u) in (n co I 1 a gd n* e 1 8 8 5 . 5 ll zo > J 3 o > n m m if- !5S --6 s--' o(Di O) P~ jan w - - - Ia 5 fil LU LU 2OS 3 UJ O o Sn --N in co tn to to ^ (--N uo a-> cn d - 2 o eo 3 o> Soo Calibrated By:. Wade Drew 253 < ABD00048964 o oo -oCo oo in E .Q T5 O g CD UJ uj it! tZ Ui o1 O J- ti 0) o 3fN Ofl> TT 3 2 111 6 = >Sre 8X 8 88 I oE J5 S $ -- ~M -<0 o 2 P o LLI Ia ^51 -- --N (^O ^ u5a - !! Calibrated By:Tlm Orahelm 254 ABD00048965 THERMOCOUPLE CALIBRATION Client: Georgia Gulf Source: Multiple Sources Date: Tech: 5-12-00 Lynn Beane Thermocouple Identification Meter Box In (Console E-l 0) Meter Box Out (Console E-l 0) Cold Ambient Hot fMHMBMBll Cold Ambient Hot Reference Thermometer Temperature 42 74 251 50 70 251 Thermocouple % Potententiometer Temperature Temperature Difference 42 0.00 74 0.00 250 0.14 49 0.20 70 0.00 251 0.00 Heater Box (HB-01) Cold Ambient Hot 47 70 259 48 -0.20 70 0.00 258 0.14 1 ||j Stack Gas Probe ESP-3C Impinger Exit (HB-01) Cold 53 54 -0.19 Ambient 74 75 -0.19 Hot 275 276 -0.14 PliiPPBI wmwmMWmwk WMSiM9MSM, Cold 53 53 0.00 Ambient 70 71 -0.19 Hot 229 230 INNMMNi 1mnmppmp MiBllkfBi -0.15 % Difference=[{(Ref. Thermometer+460) (Thermocouple+460)}/(Ref. Thermometer+460)] x 100 < 1.5% 255 ABD00048966 THERMOCOUPLE CALIBRATION Client: Georgia Gulf Source: Multiple Sources Date: Tech: 5-12-00 Lynn Beane Thermocouple Identification Meter Box In (Console E-10) Cold Ambient Hot Meter Box Out (Console E-l 0) :^Cold* ^ Ambient Hot Heater Box (HB-01) Cold Ambient Hot Stack Gas Probe ESP-3 D Cold Ambient Hot Reference Thermometer Temperature 42 74 251 50 70 251 51 71 250 53 74 275 Thermocouple % Potententiometer Temperature Temperature Difference 42 0.00 74 0.00 250 0.14 11111-- WwimwimmA 49 0.20 70 0.00 251 0.00 WWWMWMMWM 51 0.00 70 0.19 251 -0.14 1 54 -0.19 75 -0.19 276 -0.14 Impinger Exit (HB-02) Cold Ambient Hot fMfwimimiwsmmsm. 53 70 229 53 0.00 71 -0.19 230 -0.15 iHiillSSiiySIIKiliiH % Difference=[{(Ref. Thermometer+460) - (Thermocouple+460)}/(Ref. Thermometer+460)] x 100 < 1.596 ABD00048967 THERMOCOUPLE CALIBRATION Client: Georgia Gulf Source: Multiple Sources Date: Tech: 6-06-00 Lynn Beane Thermocouple Identification Meter Box In (Console E-l 1) Meter Box Out (Console E-l 1) Heater Box (HB-02) Stack Gas Probe ESP-3A Impinger Exit (HB-03) Reference Thermocouple % MHHHBIm Thermometer Potententiometer Temperature Temperature Temperature Difference Cold 45 45 0.00 Ambient 72 73 -0.19 Hot 251 251 0.00 'WSKM^^ISIK& MBM Cold 51 51 0.00 Ambient 71 70 0.19 Hot kllillllBSIIl Cold 249 45 250 -0.14 WMMMMMifflMMb smfMPBraM 45 0.00 Ambient 73 73 0.00 Hot 253 252 0.14 MMBHBtwi WWW---- wmmmmmmmm M----I Cold 55 54 0.19 Ambient 73 72 0.19 Hot 253 254 -0.14 llllllllllllllllii MMBMl Cold 47 48 -0.20 Ambient 71 71 0.00 Hot 231 231 0.00 % Difference=[{(Ref. Thermometer+460) - (Thermocouple+460)}/(Ref. Thermometer+460)] x 100 < 1.5% 257 ABD00048968 THERMOCOUPLE CALIBRATION Client: Georgia Gulf Source: Multiple Sources Date: Tech: 6-09-00 Bradley Hall Reference Thermocouple % Thermocouple Thermometer Potententiometer Temperature Identification Temperature Temperature Difference Meter Box Cold 48 48 0.00 In (Console E-12) Ambient Hot 72 251 72 0.00 252 -0.14 IMW-- Meter Box Out Cold Ambient (Console E-12) Hot rnmmmm Heater Box Cold 51 73 248 51 50 73 248 wmimmmmMiMB, 51 0.20 0.00 0.00 0.00 (HB-04) Ambient 74 73 0.19 Stack Gas Probe ESP-6A Hot 237 fwmMwmdMii. Pi^PPPlill1 Cold 55 Ambient 72 Hot 749 Wmmmmmm 237 54 73 749 0.00 i--i 0.19 -0.19 0.00 MMHMH Impinger Exit Cold 50 50 0.00 (HB-04) Ambient 70 71 -0.19 Hot WMMPMMWM- 230 231 -0.14 d'WN^^WMWHWNMWMzWKMMW' llljllllll! % Difference=[{(Ref. Thermometer+460) - (Thermocouple+460)}/(Ref. Thermometer+460)) x 100 < 1.5% ABD00048969 THERMOCOUPLE CALIBRATION Client: Georgia Gulf Source: Multiple Sources Date: Tech: 5-09-00 Tim Draheim Thermocouple Identification Meter Box In (Console E-l 3) Meter Box Out (Console E-l 3) Cold Ambient Hot Cold Ambient Hot Reference Thermocouple % Thermometer Potententiometer Temperature Temperature Temperature Difference 43 44 -0.20 70 71 -0.19 253 253 0.00 1WBMHMBWM wmammm -- 48 48 0.00 71 71 0.00 250 251 -0.14 WMWiMSMMM Heater Box (HB-02) Cold Ambient Hot Hlppiii 50 72 245 51 -0.20 72 0.00 245 0.00 Stack Gas Probe ESP-7A Impinger Exit (HB-03) Cold Ambient Hot Cold Ambient Hot 50 50 0.00 71 73 -0.38 251 252 -0.14 i--11 HHHHIIS 55 55 0.00 70 71 -0.19 229 230 -0.15 wmmmmm HBHHHBMI % Difference=[{(Ref. Thermometer+460) - (Thermocouple+460)}/(Ref. Thermometer+460)] x 100 < 1.5% 259 ABD00048970 THERMOCOUPLE CALIBRATION Client: Georgia Gulf Source: Multiple Sources Date: Tech: 5-12-00 Lynn Beane WlfMMMfm, Reference Thermocouple % Thermocouple Thermometer Potententiometer Temperature Identification Temperature Temperature Difference Meter Box Cold 41 42 -0.20 In Ambient 71 72 -0.19 (Console E-l 4) Hot 247 i--i^j -- 247 0.00 Meter Box Cold 47 48 -0.20 Out Ambient 73 73 0.00 (Console E-l 4) Hot 251 251 0.00 Heater Box Cold wmmlmimmjmm lliippppppii 47 47 0.00 (HB-03) Ambient 72 73 -0.19 Hot 240 241 -0.14 Stack Gas Probe ESP-3B Cold Ambient Hot Impinger Exit . (HB-03) wfMwMwmwMMM, Cold Ambient Hot 51 75 280 51 74 219 ill H 50 0.20 75 0.00 281 -0.14 50 0.20 74 0.00 220 -0.15 iMiiPfPIp `WimmBMm % Difference=[{(Ref. Thermometer+460) - (Thermocouple+460)}/(Ref. Thermometer+460)) x 100 < 1.5% ABD00048971 Pitot Tube Calibration Project: Georgia Gulf Date: 4-03-00 Pitot Tube ID: ESP-6A Calibrated By: WD Run No. 1 2 3 delta Pstd in. H20 0.43 0.43 0.44 "A" Side Calibration delta P(s) in. H20 0.60 0.60 CP(s> 0.84 0.84 0.60 Cp (Side A) 0.85 0.84 Deviation Cp(s) - Cp (A) 0.003 0.003 0.006 Run No. 1 2 3 delta Pstd in. H20 0.43 0.43 0.43 "B" Side Calibration delta P(s} in. H20 0.60 CP(s) 0.84 0.60 0.60 Cp (Side B) 0.84 0.84 0.84 Average Pitot Tube Cp 0.84 Deviation Cp,s)' Cp (B) 0.000 0.000 0.000 261 ABD00048972 Pitot Tube Calibration Project: Georgia Gulf Date: 3-13-00 Pitot Tube ID: ESP-7A Calibrated By: GC Run No. 1 2 3 delta P^ in. H20 0.43 0.43 0.43 "A" Side Calibration delta P(8) in. H20 0.60 0.60 0.60 Cp (Side A) CP(s) 0.84 0.84 0.84 0.84 Deviation Cp(s) - Cp (A) 0.000 0.000 0.000 Run No. 1 2 3 delta Pstd in. H20 0.42 0.43 0.42 "B" Side Calibration delta P(s) in. H20 0.60 0.60 CP(s) 0.83 0.84 0.59 Cp (Side b) 0.84 0.83 Average Pitot Tube Cp 0.84 Deviation Cp,sl - Cp (B) 0.006 0.004 0.001 262 ABD00048973 Pitot Tube Calibration Project: Georgia Gulf Date: 3-13-00 Pitot Tube ID: ESP-3B Calibrated By: TD Run No. 1 2 3 delta Pstd in. H20 0.43 0.43 0.42 "A" Side Calibration delta P(s) in. H20 0.60 0.60 0.59 Cp (Side A) CPfs) 0.84 0.84 0.84 0.84 Deviation Cp(S) - Cp (A) 0.001 0.001 0.002 Run No. 1 2 3 delta P^ in. H20 0.43 0.44 0.44 "BM Side Calibration delta P(s) in. H20 0.60 0.60 0.60 Cp (Side B) CP(s) 0.84 0.85 0.85 0.84 Average Pitot Tube Cp 0.84 Deviation Cp(s) Cp (B) 0.006 0.003 0.003 263 ABD00048974 Pitot Tube Calibration Project: Georgia Guff Date: 3-13-00 Pitot Tube ID: ESP-3A Calibrated By: GC Run No. 1 2 3 delta Pstd in. H20 0.43 0.43 0.43 "A" Side Calibration delta P(8) in. H20 0.60 0.60 0.60 Cp (Side A) Cp,s> 0.84 0.84 0.84 0.84 Deviation CP(s)" Cp (A) 0.000 0.000 0.000 Run No. 1 2 3 delta Pstd in. H20 0.43 0.43 0.43 "B" Side Calibration delta P(s) in. H20 0.59 0.60 0.60 Cp (Side B) CPw 0.85 0.84 0.84 0.84 Average Pitot Tube Cp 0.84 Deviation Cpfs) Cp (B) 0.005 0.002 0.002 264 ABD00048975 Pitot Tube Calibration Project: Georgia Gulf Date: 4-02-00 Pitot Tube ID: ESP-3D Calibrated By: TD Run No. 1 2 3 delta Pstd in. H20 0.43 0.43 0.43 "A" Side Calibration delta P(s) in. H20 0.60 0.60 0.59 Cp (Side A) CP(s) 0.84 0.84 0.85 0.84 Deviation Cp(S)- Cp (A) 0.002 0.002 0.005 Run No. 1 2 3 delta Pstd in. H20 0.44 0.44 0.44 "B" Side Calibration delta P(s) in. H20 0.60 CPfs) 0.85 0.60 0.60 Cp (Side B) 0.85 0.85 0.85 Average Pitot Tube Cp 0.844 Deviation Cp(s, * Cp (B) 0.000 0.000 0.000 265 ABD00048976 Pitot Tube Calibration Project: Georgia Gulf Date: 4-03-00 Pitot Tube ID: ESP-3C Calibrated By: TD Run No. 1 2 3 delta Pstd in. H20 0.43 0.43 0.43 MA" Side Calibration delta P(s) in. H20 0.60 0.59 0.60 Cp (Side A) CP(S) 0.84 0.85 0.84 0.84 Deviation Cp(8) - Cp (A) 0.002 0.005 0.002 Run No. 1 2 3 delta Pstd in. H20 0.43 0.43 0.43 "B" Side Calibration delta P(s) in. H20 0.59 CP(s) 0.85 0.60 0.84 0.60 0.84 Cp (Side B) 0.84 Average Pitot Tube Cp 0.84 Deviation Cp(S) ` Cp (B) 0.005 0.002 0.002 266 ABD00048977 O 9 N. ' If) to Ig CL O II .j. e |g <3 ui S1 2 CO 88 zO x RR 11 UJ CO 0) O i muKi a il fl E 11 hi UJ y sS G2 8 SK* (6 -- => yK*.j sc rJ< ^ w cm => y 267 Date: 07/10/00 Pb: 30.12 in. Hg Box No.: E ll Calibrated By: DLB CTr0OM5t-)- CL00OM05 ooCoO> oo 3 c0o0 CO CCOO o TO c u_ --C I0T3) 0CO0 OO) _ <CD0 lT CD -- S' $O 0) 3 iCnO (CDO nCO o 3 CD 2 Q. E 0) cCoO m00 oCOo c in 00 co CO h00 C/5 $ a~ NCO lCOO (0D0 5 Cra/5 c II LO *= s Is CO ooo N00. oC0M0 0hCO5- 0 E3 Q o TO C ~ o. O <C0D m00 LTqOT ooo cooo rCO > (0 0 5, . c Ll_ __^ d 3 ^ o CO 05 L00O05 00 Lro-Oo 00 C/5 5 c d 3C3, o PO oo o oo o E % X 01TM oin mo om w ?= c iss Ei '5 O E 75 I OfS X ooCO ooCO ooCO Bd ^ o ABD00048978 CO lo 0055 o CT> > < Lo L Oc) dCO oCO + X m o O 3O*co I0L OCO 75 V) oc + o(N X C u." 5a> E 3C E E 75 E CO CToO/5> 75 5 75 75 TO OQ. .Q 735 E Q. E3 0. WT*o3 3 2Q. E 0k>_5 < II 1Eoo-> o-- 3 2Q. E O) 2> < ii E K5 CD co E ? X TO ;o, a CL II E u5. CO CO E 75 X + Qo_ It TaE03.5 co w3vC/>5 Q. > 0C5 II E 1 X TO o CE0oL5 E ? C a 7icf5 "E EOD) c $ 7c5 5 ii >- Average MCF (1.00 + or - 0.02) = 0.99453 268 ABD00048979 ir> g "8 5 0 I <3 I s< me s! j o /? so -~g E3 . . 3<0 S> IS ao .a no 98 Si 2W I0o) s III O SOS 5i N8 80 8 cc O cr UJ HUJ W < .3j- CD >O' na UJ K S S| 5I I| 5g => I S3 O ui ~ iI 5l $ ss <fnD* IND u 6s3^ 1fgs1t1' e>e a 3S 1511 S5 269 Date: 07/10/00 Pb: 30.14 in. Hg Box No.: E13 Calibrated By: DLB Tc0CoDf)r 0CoCCO>0DD TC0CO0DDT) oo to o3 CO If) ^ 00 00 00 (0 c u_ -- ^ CD CO TTOO C CO OO 00 <0 CD O $Q ~03) CCOM CO CCOO 3TM Si TO -- Q. E -- CM CO CO <D C 00 OO CO CCD Tf -<fr If) ii_ 00 00 CO a) TO t- t* t* $ C 00 OO CO 5TO iCCiD CCOD >-N d O g COCDOO oTi 18 CCTtOD- etndT- 0 0) E3 Q o TO C x-s *3= ^ ID 5 OCoD oCt*O UOCOO) CCTODf > CCOD O iT_O TO s TcO iZ 3 sO) ICcDMo e oo CD ICrD-O OO HCTOO TO .2 5c d o3, o P Oo o oo o E 1O xX TO c Q) aj ao> "O E ITO 5E- TO "53 TO ooo ^ ooo ooo If) If) If) ABD00048980 CICCofODD) o a> CD CD TO > < Average MCF (1.00 + or - 0.02) = 0.99530 270 ABD00048981 2Q LLI H c o 26 X o CD >v CD T033 re 3 ChO. re .q O E I o Q> <0 o Q. O) X o o N- O d r- co o 0-)* CO Q 00 CM CM 00 in CO CO O) o> o CO o o o> o - o re o3 ^ in CO CO CO CTJ c -- lO CO N C 00 CO CO to _ CO iTO -- 8 <0 =N if) 3 CO CO CO 3 CO CuO. Q. E a> JU co m co C CO CO 00 re 75 re CCMO CCOO iono 5 iZ 7Hr5e 5 re 'E C1--O 0C0M 0C0O o in in re <2 -J *7 00 00 o o> in CM a> il S <re0 S s T}- CO CO r- m in m O re * a Eof 3 O oom s oo o> 00 in it s? m co m m in > troe O re 2 In =: 3 s o sj- m st 't CO r e oo CT) eet CO H_ re g 5c ooo ooo odd E ? i -I*i0n 0m 0io re re "H3 11" 11 O 5x (N X ~C5O C o oo ooo CO CO CO Ta3> w sf CO tT o> CT) 0) ore> 0) > < LL CT> O C CO re to + X re 3 o o o re.c o c Li. 0 re O re 75 CO 76 c + (0 re re re 3 re CEE E to To m re O) re O M X c w re re E To re 1 (O re o $ re o o S' CO 76 0u). S CO CO a 3 3 T" 1 5 76 E o re 76 re re t5 a. E a. EX X re re Q_ re re re o re 2 To re o> re re re O) *o re re T3 re > t+ re > .Q X) re k_ 3 to to fi a re > 76 O) re c n E 3 < < a CL ? E ii n n II I Q. E CT> 3 o E s E E CT) re s T3 re Q_ 1- h* . D. T3 E CT> *o % 76 C fr -Q i 75 c (3 e' 1; E CT) t re c re 5 76 c U-- 75 5 n >- Average MCF (1.00 + or - 0.02) = 0.99434 271 ABD00048982 Appendix E Test Calculations ABD00048983 TEST CALCULATIONS I. Determination of Moisture in Stack Gases a. Volume of Water Vapor Collected (Cubic Feet): Vwstd = 0.04707 * (Vic) b. Dry Gas Volume Through Meter (Cubic Feet): Vmstd = 17.64 * Vm * Y * {(Pbar + (H/13.6)) / Tm} c. Moisture Content (Percent): Bws = Vwstd / { Vwstd + Vmstd } * 100 d. Wet Molecular Weight : (Ms) Ms = { Md * (1-Bws) } + { 18.0 * Bws } II. Actual Stack Gas Volume Sampled (Cubic Feet): Vma = { Vmstd * Ts * Pstd } / { (1-Bws) * Tstd * Ps } III. Determination of Stack Gas Velocity & Volumetric Flow Rate a. Stack Gas Velocity (Feet per Second): Vs = Kp * Cp * (SqR P) * { SqR (Ts / (Ps * Ms) ) b. Stack Volumetric Flow Rate (Cubic Feet per Minute): 1. Dry Standard Conditions (Qs) Qs = 60 * (1-Bws) * Vs * As * (Tstd/Ts) * (Ps/Pstd) 2. Actual Conditions (Qa) Qa = Vs * As * 60 IV. Determination of Particulate Concentration (Grainloading) a. Dry Standard Conditions: (cs) cs = 0.01543 * (Mn / Vmstd) b. Actual Conditions: (csl) csl = 0.01543 * ( Mn / Vma) V. Emission Rate (Pounds per Hour) E = 60 * Qs * cs / 7000 VI. Determination of Acceptability of Sampling Results: (I) I = ( 0.0945 * Ts * Vmstd ) / { 0 * Vs * Ps * An * ( 1 - Bws ) } 273 ABD00048984 As An ACF ACFM Bws cs csl Ca Cp delta H dp delta P dscf E E/Btu F Kp Ma Maw Mf Mn Pa Pbar Pm Ps Pstd Qa Qs Tm Ts Tstd O Va Vaw Vf Vi Vic Vm Vma Vmstd Vs Vwstd Wa Wf Wi Y NOMENCLATURE Cross-sectional area of stack, square feet Cross-sectional area of nozzle, square feet Actual cubic feet of gas at stack conditions Actual cubic feet of gas per minute at stack conditions Proportion by volume of water vapor in gas stream Particulate concentration in stack gas, gr/dscf Particulate concentration in stack gas, gr/ACF Acetone blank residue concentration, mg/g Pitot tube coefficient Pressure drop across orifice meter, inches water Nozzle diameter, inches Velocity head of stack gas, inches water Cubic feet of dry gas corrected to standard conditions Particulate emission rate, pounds/hour Particulate Emission Rate, pounds/mmBtu F-factor, 9640 dscf/MMBTU's of heat input Constant (85.49) Mass of residue of acetone after evaporation, mg Mass of residue of acetone blank, mg Particulate matter collected on filter, mg Total particulate matter collected, mg Percent of isokinetic sampling Density of acetone, mg/ml Barometric pressure, inches mercury Barometric pressure of dry gas meter, in. mercury Absolute stack gas pressure, inches mercury Barometric pressure, standard conditions, 29.92 "Hg Volumetric flow rate, actual conditions, ACF/min Volumetric flow rate, dry standard conditions, dscf/min Absolute average dry gas meter temperature, degree R Absolute average stack gas temperature, degree R Absolute temperature at standard conditions, 528 R Total sampling time, minutes Volume of acetone blank, ml Volume of acetone used in wash, ml Final volume of impinger contents, ml Initial volume of impinger contents, ml Total volume collected in impingers and silica gel, ml Volume of gas sampled through gas meter, cubic feet Stack gas volume sampled, ACF Volume of gas sampled through gas meter, cubic feet Average stack gas velocity, feet/sec Volume of water vapor in gas sampled, standard cubic feet Weight of residue in acetone wash, mg Final weight of filter or probe wash beaker, g Initial weight of filter or probe wash beaker, g Dry gas meter calibration factor 274