Document 9J4Q1J1rJr4N6w2RN3jq1D5E3

Interoffice Communication To M. L. Ashby From V. M. Fisher Date December 2, 1983 subject Incinerator Bypass Reduction Design No. 194-900-983-VMF FINAL ISSUE y This attached class "A" design provides for installing new pressure trans mitters for the Direct Chlorination Vent Header and Wet Vent Header bypass controllers (PRC-901 and PRC-902) on the HC1 Absorbers, C-901 and C-901B. These new pressure transmitters should reduce the incinerator bypasses to the atmosphere by allowing the maximum pressure in the absorbers before bypassing. Also included are provisions for installing Annubar Flow Sensors in the Wet Vent and the Direct Chlorination headers. Adding these flow sensors will allow monitoring the vent flow, which currently cannot be done. The HC1 Absorbers, having 3 psig design pressures, limit the operating pressure of the incinerator units. To protect both HC1 Absorbers from over pressing the Wet Vent Header and Direct Chlorination Header bypass control valves (PCV-902 and PCV-901) open whenever the pressure in either header reaches 80" H?0. However, the existing pressure transmitters for the con trollers of these bypass valves are located upstream of where both headers split to each incinerator train. At this location, the pressure readings are not indicative of the actual pressure on the absorbers. The new trans mitters should permit higher operating pressures (without exceeding the design pressures) before bypassing because the actual absorber pressures will control the bypass valves. With the new pressure transmitters, a different set point for the bypass con trollers is required. The Combustion Air Blowers (BL-901 and BL-901B), having a maximum discharge pressure of 79" H^O, also limit the operating pressure of the incinerator units. To avoid "dead-heading" the blowers and to provide overpressuring protection for the absorbers, the bypass control valves will open when absorber's pressure is 52" H20. One change from the review design is the installation of new pressure trans mitters. on the absorbers rather than the relocation of the existing trans mitters. The existing transmitters will remain to provide pressure indica tions for the Wet Vent and Direct Chlorination Vent headers. Keeping these indications will be advantageous to operators as well as provide information needed for optimizing the incinerator's operations. This design is part of an overall plan to reduce incinerator bypasses. The overall plan will be outlined in a future letter. CCR 000018478 This project is included in the 1983 Capital Budget as two projects in ' "Miscellaneous Projects Under $15,000". By copy of the final design to y J. R. Holcomb, separate definitive cost estimates are requested for the pressure transmitters and flow sensors for each train. If there are any questions or comments, please contact me. 1 M. Fisher Process Engineer Approved D. L. Davis, Sr. Process Eng br cc: RAC-JWW-RB-MLA(4)-MCM-JRH(4)-SRA-PLF-DLD-SJR-PE PFF - Ponca City CCR 000018479 DISCUSSION The National Enforcement Investigation Center (an EPA division) final report, evaluating their January 1981 VCM Plant inspection, concluded that incinerator bypasses contributed to the plant's excess vinyl chloride emissions. Although these bypasses were not classified as EPA violations, factors causing these bypasses were identified to determine how the number of bypasses can be reduced. The VCM Plant has experienced 62 incinerator bypasses from January 1981 to September 1983. The bypass causes can be grouped into the following five categories. Causes Number % Power Failures Mechanical Failures Flame Outs High Vent Pressures Combustion Air Blower High Amperage Shutdown Total 1 9 22 27 3 62 2 14 35 44 5 100 Both mechanical and power failures are uncontrollable. Flame out bypasses occur when the incinerator firebox flame scanners lose sight of the flame. Sudden vent surges or high vent volumes produce two conditions which usually cause flame outs: 1) Incomplete combustion, resulting in black smoke in the firebox, blocking the scanners' view of the flame. 2) The firebox flame being momentarily blown out, causing the scanners to register an extinguished flame. To limit these flame out bypasses, restriction orifices can be placed in the lines having sudden vent surges. During the May 1982 turnaround, a restriction orifice was placed in the vent line of the Flake Caustic Dryers, S-207 A&B, to reduce the vinyl surges during purging and recharging of the vessels. High pressure bypasses occur at the Wet Vent Header Knockout Vessel, T-501, and the Direct Chlorination Vent Header Knockout Vessel, S-500. Whenever either vent header exceeds 80" HpO, the bypass control valves open directing the vents to the atmosphere via C-500. The pressure transmitters (PT-901 and PT-902) relaying pressure indications to the Direct Chlorination Vent Header and Wet Vent Header bypass controllers (PRC-901 and PRC-902), are upstream of the vent header's split to the primary and secondary incinerator trains. The bypass controllers pressure transmitters are approximately 80 feet from both incinerator trains' entrances, so the actual pressure at the absorbers is lower. Pressure drops are taken through 000019'*80 OCR the line and equipment (i.e. the Flame Arrestors, S-911 and S-911B; the Incinerator Fireboxes, 1-901 and 1-901Bi and the Waste Heat Boilers, H-902 and H-902B). Installing new pressure transmitters on the absorbers should allow higher vent and operating pressures without bypassing and exceeding the absorbers' design pressure. An automatic shutdown of the Combustion Air Blowers (BL-901 or BL-901B) will result in vent bypasses. These shutdowns or "trips" happen whenever the blowers' motor require.more than 292 amps. This will occur whenever the backpressure on the blowers either exceeds the design rating (i.e. 79" H2O) or is too low. When designing the Incinerator units, the blowers were sized for the maximum pressure drop through each train. To compensate for the lower static pressure, the blower's output capacity and power requirement increase sometimes reaching the shutdown point. Before modernizing the Oxychlorination Unit, a butterfly valve on the blower's discharge line was kept half closed increasing the system pressure drop and maintaining a reasonable operating range on the inlet damper system. After Starting up the modernized Oxychlorination Unit, there has not been a need to keep the butterfly valve partially closed. The budget design, (Reference: "Incinerator Bypass Reduction" June 1, 1982 by M. J. Allen) specified installing a differential pressure controller on the discharge lines of the blowers. These controllers were to maintain a 1.2" H2O pressure drop through the butterfly valves during the operation of either blower. Instead another alternative, installing a variable frequency controller on the blowers' motors, is being examined. Variable frequency controllers would convert the existing fixed speed motors to controlled adjustable speed machines. The variable frequency controllers alternative should result in a 28% annual energy savings. This is based on the blowers' present electrical operating cost versus the predicted electrical operating cost with the variable speed controllers. (The variable speed controllers provide a horsepower savings with flow reduction.) Adapting the existing motors will cost approximately $62,000. This is $52,200 over the $9800 in the 1983 Capital Budget for installing the differential pressure controllers. A preliminary economic analysis of this alternative showed a 41% "incremental" rate of return for the additional $52,200 outlay. Provisions for installing these adjustable frequency controllers are not addressed in this particular design, but will be addressed in a future design. CCR 000018481 DESIGN BASIS The HC1 Absorbers (C-901 and C-901B) limit the operating pressures of both the primary and secondary incinerator trains, both having design pressures of 3 psig or 83.1" H^O. To allow operating at higher vent pressures without bypassing and exceeding the absorbers' design pressures, new pressure trans mitters (PT-1 and PT-1B) for the Wet Vent Header pressure controller (PIC-902), and Direct Chlorination Vent pressure controller (PIC-901) will be installed on the absorbers. In adding the new pressure transmitters, the effects on the Combustion Air Blowers (BL-901 and BL-901B) must be considered. These blowers have a maximum discharge pressure of 79" H20 which limits the operating pressure range of both incinerator units. If^the operating pressure in the firebox reaches 67" H2O the blowers will "dead-head" causing a motor overload and a subsequent shutdown. This is assuming that a 12" H20 pressure drop is taken through the air fence and air plenum as specified in the incinerator design. To avoid shutting down the blowers and to provide overpressuring protection for the absorbers, whenever the pressure at PT-1 or PT-1B exceeds 52" H20 the Wet Vent and Direct Chlorination Vent bypass valves (PCV-902 and PCV-901) will open. (Note: the calculated setpoint of 52" H20 is based on the maximum firebox operating pressure, 67" H20 minus the designed pressure drop across the waste heat boiler, 15".H20.) ^Since the response speed of the bypass control loops with the new transmitters and the actual pressure drops across equipment in the incinerator trains are not known, a set pressure lower than 52" H20 should be used initially. With experience, an optimum set point will be chosen. Another important consideration in adding the new pressure transmitters is the possibility of blowing the rupture disks on T-501 and S-500 was examined. The rupture disk on S-500 (RD-901) is set for 11 psi while the rupture disk on T-501 (RD-902) is set for 15 psi. Pressure drop calculations show that for the incinerator trains at design rates (i.e.. Direct Chlorination Vent rate of 65,000 SCFH and Wet Vent rate of 47,080 SCFH), the maximum pressure drop through the equipment and lines between the knockout vessels, and the relocated pressure transmitters should be 103" H20 maximum. Equipment P, "H?Q Flame Arrestor (S-911 and S-911B) Incinerator (1-901 and 1-901B) Waste Heat Boiler (H-902 and H-902B) Piping From S-911 to T-501 Piping From S-911 to S-500 Piping From 1-901 to S-911 Total 6 12 - 40 15 6 29 7 75(min) - 103(max) Therefore, when a bypass occurs the maximum pressure at the knockout drums should be approximately 6 psig (52 + 103" H20), which is below the rupture disks set pressures. CCR 000018482 Since the new pressure transmitters on both absorbers will be relaying signals to the existing Wet Vent Header pressure controller and Direct Chlorination Vent Header pressure controller, a high signal selector module will be added to both controllers. In addition to the new pressure transmitters, Annubar Flow Sensors will be installed in the Wet Vent header and the Direct Chlorination Vent header. These annubars will be inserted near the existing pressure transmitters (PT-901 and PT-902). Installing these annubars will allow the monitoring of vent flows, which cannot be measured now. To size these annubars the following rates were used. Direct Chlorination Vent Wet Vent 90,000 SCFH 56,000 SCFH The existing vent header pressure transmitters will remain to provide pressure indications for the Direct Chlorination Vent header and the Wet vent header. 000018^83 CCR t ENVIRONMENTAL IMPACT STATEMENT This project should reduce the number of incinerator bypasses due to high vent pressures. ENERGY IMPACT STATEMENT This project will tiave no effect on the plant's energy consumption. The energy checklist is not applicable to this project, and therefore was not completed. SAFETY & HEALTH IMPACT STATEMENT This project will have no effect on plant safety. The safety checklist was completed and included with the Review Issue. CCR 000018484 WORK LIST Refer to Drawing No. VCM-194-1 1) Connect high signal selector module, HS-902, with the existing pressure controller for the Wet Vent header, PIC-902. 2) Connect high signal selector module, HS-901, with the existing pressure controller for the Direct Chlorination Vent header, PIC-901. 3) Disconnect input from Direct Chlorination Vent header pressure transmitter, (PT-901) to Direct Chlorination Vent Header pressure controller, (PIC-901). 4) Disconnect input from Wet Vent Header pressure transmitter (PT-902) to Wet Vent Header pressure controller (PIC-902). 5) Install 2" flanged coupling on Wet Vent Header. See manufacturer's instructions with FE-2 specification sheet. Locate the coupling so that once the annubar is installed it is 3 pipe diameters (30") downstream of 90 elbow and 7 pipe diameters (70") upstream of the existing Wet Vent Header pressure transmitter (PT-902). 6) Install Annubar Flow Sensor, FE-2 on the Wet Vent Header at 2" flanged coupling mentioned in step 5. Refer to the manufacturer's installation instructions with FE-2 specification sheet. 7) Install DP transmitter, FT-2 and connect to Annubar Flow Sensor. 8) Install flow recorder, FR-2, in the incinerator control room. 9) Run electrical connections from DP transmitter, FT-2, to flow recorder, FR-2. 10) Install Annubar Flow Sensor, FE-1, on the Direct Chlorination Vent header line upstream of the branch off to the primary and secondary incinerator trains. Locate Annubar 3 pipe diameters (24") downstream of 90 elbow and 7 pipe diameters (56") upstream of Direct Chlorination Header pressure transmitter (PT-901). Refer to the manufacturer's installation instructions with FE-1 specification sheet. 11) Install DP transmitter, FT-1 and connect to Annubar Flow Sensor. 12) Install flow recorder, FR-1, in the incinerator control room. 13) Run electrical connections from DP transmitter, FT-1, to flow recorderFR-1. Steps 14, 15 and 16 are for the primary incinerator train, however, these steps should be duplicated for the secondary incinerator train. CCR 000018485 14) Install new pressure transmitter PT-1 on the HC1 Absorber, C-901. Refer to Drawing No. VCM-194-2. Insert the pressure transmitter in the vacant 2" 150# nozzle located to the north of TE-908 and the existing 0-60" HoO pressure gauge. Run electrical connections from PT-1 to the high signal selector modules HS-902 and HS-901 on both the Wet vent header pressure controller, PIC-902, and the Direct Chlorination vent header pressure controller, PIC-901, respectively. Install a 2" plug valve with a 2" x i" reducing flange and 3/4" bleed valve upstream of PT-1. Use specification Q40-1 (Kynar) pipe upstream of PT-1. 15) Install pressure recorder, PR-1, in the incinerator control room. 16) Connect input from PT-1 to PR-1. 17) Remove existing pressure gauge for S-500 from 2" valve and install pressure gauge, PG-1, with diaphragm seal and i meter valve, upstream of Direct Chlorination Bypass valve. 18) Install pressure gauge for T-501, PG-2, with diaphragm seal and V' meter valve on existing 2" valve upstream of Wet Vent Bypass valve. CCR 000018486 (conoco) Engineering Center Ponca City. Oklahoma Specification Sheet PLANT _Z-C 1/CM PLAK1T project n-jrjuei?Ard(L SPECIFICATION SHEET PROJECT NO. A.F.E. NO______________________ REQ. NO^ , -- DATE ^/ / /&3 APP OBY MADE BY YMF* BY-pass ge-doct/o/J ITEM NO. Fe8--- / SERVICE AtsJklUGAtL puov*/ gy.^/TA/7- p/e.&C.r C+{LojWAVOfJ H-EAQE&* TYPE : JSTTL 7.5" - ANMUBAIL. F4Q - TAP MQO&1-._______________________________ LitiE Size Aao- schedule : 8* 40 Lt*Je ma-re&jAl- \ srfgL A+MU6A& MAtTZjjU of <l*u*r/?JAL7-/at4 \ S!6eS$ ELEMENT ANO SoZeW'tCt* . CALCU LAf/oM DATA APPU C.AT/OU D/P__Pr <^hft-o/2_i/JA rinsJ A&AE>t?(2- tTLO/O ! tL)4Co.ftdA ?-*=& tfYpe>CA#.&QtJ'S. CO. Ca* /J* C/J*. PTLOW FATE ; t.SoQ SCFM S/say)___/ 5g jYCEm CM /*/j p(LES5U&-& \ 4^~ * rf-irO (k/o4maC)______ 7*5 _____________ TEMP / tec pr {fi/o&MM-)_______ i47'F (max)_________________ MErE/Z. TYPE O/R CEL.L.____________________________________________________ PaPd \ <4*7 PS/A ___________L________________________________________ pe-MsrrY: Mouse ulf WTj 30.54-^ OtO^L%TB QtiP&e/tflfi&TWf* V FACTOIZ. , Cr/Cif ta KS5"________________________________________________ Q/F> gA^c^e g ? Ho______________________________________________ _______________ A/e>rgs AT-r-jj-c.//AfE^+JTS SPEC NOREV SHEET__ / ____OF____$-____ 4-e CCR 000018^37 4-441-S E- - WALL I e i IV FEMALE NPT BRONZE GATE VALV._ *7 ! DRILL ONE 1 06" OIA HOLE AND PROVIDE Vi" MIN WELD BEAD ALIGN TO PIPE AXXIISi \r'c1'/" NPT r T cCS WELO COUPLING l I 1%" NPT CS CLOSE NIPPLE WITH SPECIAL 1 065" ID l i CUSTOMER ____ '~"C> OCr C-++&A4 tCstC-TS ------------------ 4 50- ------------------- ^ ^______ -------- (DE7 60") -------- LOCATION _____ ______________ FULLY INSERTED POSITION PROJECT........................ TAG NO. F-&-- / OPERATING TEMPERATURE. SPECIFY (o.OL________________ FLOW MEDIUM. SPECIFY <~Q ! *JAtTBP /-tYptl* C& PI PEI D -- D'________ >*'__________________ ^ 98^810 *3 WALL - E ________________________________ DIMENSIONS CALCULATED F -- CAGE NIPPLE ASSY BY OIETERICH STANDARD G - OVERALL PROBE WITHDRAWN_________ 1) MAXIMUM PRESSURE RATING FOR STANDARD "FLO-TAP" IS 70 PSIG 2) STANDARD PACKING GLAND IS RATED Tft 450F MAX 3) CAUTION SAFETY LINK MUST BE INSTALLED TO MINIMIZE CHAIN SLACK FOLLOWING PROBE INSERTION. 4) NOMINAL INSERTION FORCE 50-60 LB. AT RATED PRESSURE > Olatedch Standard Corporation Subsidiary ol Corporation Boa 9000 Boulder, Colorado B0306 USA ANNUBAR MODEL FTL 75 APPR OVAL LATEST REVISION A - 7 OR MORE PIPE DIAMETERS ARE RECOMMENDED FOR UPSTREAM SIDE AFTER VALVES ELBOWS. ETC 'B-3 TO 4 PIPE DIAMETERS ARE RECOMMENDED FOR DOWNSTREAM SIDE 'C --PERMANENT RUSTPROOF METAL TAGS SHOWING MIN., NORM A MAX. DESIGNEO FLOWS METER READINGS FOR DESIGNED FLOW TAG NO LINE SIZE. SERIAL NO A METERED FLUID Diawn by ------- Dale ?-7-a Checked by Loiter Date Oaie Drawn J 7& Scale A/TS 01200 ANNUBAR Flow Sensors Flo-Tap ANNUBAR Installation & Operating Instructions 1 Dieterich Standard Corp Subsidiary of Corporation /=**- 1 Dl fzecr cHLOZiUAT/ou . ; *****-> - 1 Contents Section Page FTL-73 and FTL-75........................ For lines to 70 p$ig....................... Equipment required...................... Installation procedure.................. Insertion procedure...................... Retraction procedure................... 1-4 1 2 2*3 3-4 4 FTM-7S and FTH-75..................... For lines to 1000 psig................... For lines to 2000 psig.................. Equipment required..................... Installation procedure.................. Insertion procedure...................... Retraction procedure................... 4-7 5 5 5 5-6 7 7 FTM-85............................................... 8-11 Equipment required..................... 8 Installation procedure.................... 8-10 FTL-73 and FTL-75 FTL-73 FTL-73 and FTL-75: tor lines to 70 psig -- - Models FTL-73 and FTL-75_Flo-Taps (Submittal Drawings E-201 and E-202) are designed for installation under pressure in lines where the static pres sure does not exceed 70 psig and where the temperature does not ex ceed 800F. Maximum temperature during the "hot-tapping'' process is limited to the rating of the drilling ma chine (250F for Mueller D-5). All items required for installation are provided except for drilling and weld ing facilities. These instructions are intended for installation without sys tem shutdown in weldable pipe. For installation in other types of pipe, con sult the factory. & CCR 0Q0018A89 1 Equipment required Installation procedure FTL-73 and FTL-75 Equipment required 1. Welding equipment 2. Pressure (hot-tap) drilling machine. Mueller D-5 or equivalent. 3. M/16"drill bit, Mueller 33530. 4. Drill holder. Mueller 33555. 5. Adapter nipple. Mueller 36195. (Items 2 thru 5 are available from Mueller Co.. Decatur. Illinois. In most cases, the public service company in your city is available to do the hottapping ' job. or the equipment may be rented or purchased locally.) Pressure drill machine and tooling 1. Verify that the line pressure and temperature are within the rated limits of the Flo-Tap ANNUBAR. (70 psig static pressure maximum. 800 F maximum temperature with asbestos packing). Temperature is limited dur ing installation to maximum rating of drilling machine. 2. Grind off paint or other coatings from the pipe in the area where the Flo-Tap is to be installed. (Except for steam applications, Flo-Tap may be installed at any angle around the pipe. Consult Catalog E-100 for recom mended minimum straight pipe lengths for best accuracy, and E-79 for further information on location for liquid and gas installation.) 5. Install the close nipple (supplied with Flo-Tap) into the weld coupling. (The close nipple is specially ma chined to 1.065" ID for ANNUBAR guide support.) 6. Install the Flo-Tap unit isolating valve on the close nipple. Verify that the valve is in the fully open position. 7. Install drill bit and adapter into the pressure drilling machine. Then at tach the machine to the Flo-Tap unit isolating valve. 3. Tack weld the 1-1/4" weld coupling (supplied with the Flo-Tap) to the pipe. The coupling must be aligned per pendicular to the pipe axis and square to its plane. 4. Complete welding. A/V-*- CCR 000018490 Insertion procedure FTL-73 and FTL-75 8. Drill through the pipe wall in accord ance with the instructions supplied with the drilling machine. 9. Withdraw the drill bit through the Flo-Tap unit isolating valve. Close the unit valve and remove the drilling ma chine. Check for leakage at valve and connections. 10. Install the Flo-Tap cage nipple (supplied with the Flo-Tap) by thread ing it into the unit isolating valve. Then install the 1-1/2" x 1" reducer (sup plied with Flo-Tap) on the cage nipple. 11. Insert Flo-Tap ANNUBAR into the cage nipple and tighten the stuffing box nut into the reducer. Hand tighten the compression nut. 12. Install the instrument valves (sup plied with Flo-Tap) and verify that both valves are fully closed. 13. While maintaining hand pressure on the Flo-Tap ANNURAR. check all connections for leakage by cracking open the unit isolating valve. If there is no apparent leakage, proceed to the insertion. Flo-Tap installed 1. Verity that both instrument valves are fully closed. While firmly holding the probe, open the unit isolating valve fully. 2. Manually push the Flo-Tap probe into the line until it contacts the oppo site pipe wall. Approximately 50 to 60 pounds of force will be required when performing insertion under full rated line pressure of 70 psig. It may be necessary to loosen the gland slightly for ease of insertion. Fully inserted 3. White manually holding the Flo-Tap probe in the inserted position, turn the probe until the flow arrow on the Flo-Tap head is aligned in the direc tion of flow and tighten the compres sion nut. 4. Still holding the Flo-Tap probe, at tach the safety chain link so that it passes through the third link from the end on both ends of the chain sup plied as part of the assembly. CAUTION The Flo-Tap prpbe must be manually held in the inserted position until the compression nut has been tightened and the safety link has been properly installed. CCft 00001849J Retraction procedure FTL-73 and FTL-75 5. Inspect the packing gland for evi dence of leakage. Tighten the com pression nut as required to stop leak age and to retain the probe in the in serted position. 6. Connectinstrumentlines to the FloTap instrument valves and to the ap propriate meter, recorder, transmitter or controller. 7. Open the Flo-Tap instrument valves. Then purge or bleed the connecting lines and readout equipment as re quired. 1. Fully close the Flo-Tap instrument valves. Then, if required, depressurize and disconnect the instrument lines. 2. While manually holding the probe In the inserted position, remove the safety link from the Flo-Tap chain. Continue holding the probe and care fully loosen the compression nut until line pressure begins to force the probe out of the pipe. Allow the probe to move slowly until it is stopped by the' Flo-Tap chain. CAUTION The probe must be manually restrain ed to prevent sudden movement caused by line pressure. Failure to manually restrain the probe during retraction could result in personal in jury. 3. After the probe is fully retracted, the Flo-Tap unit isolating valve may be closed to isolate the probe from the lines. 4. The Flo-Tap probe may now be fully removed if desired by separating the packing gland from the reducer and lifting out the probe. i 4 CCR 000018492 [ (conoco) Engineering Center Ponca City, Oklahoma Specification Sheet PLANT ITEM NO. senviue LC VCH T^LA^jt~ re --z ArJAJtJ&A/Z- f^LDl*/ PROJECT 71AJ C-j fr-/ (=MF=AJ7~ PO (Z SPECIFICATION SHEET PROJECT NO- A.F.E. NO REO. NO. ^__ i_____ OATE Sp/e_B___ MADE BY 7m APP O BY &(ZAi~d{2 3YPA&S [&DUC"nOf'J YJ PT V^f^'T H-&AIP&B-- TYPB : AMP "7.r - FlAaJ <> &P Ho C>BU Y--?='UAt^<S>& E>t M (<W \ C, " /r&TAC (ZEQ'> Ot>\ b op pip* y/All. to rue PA<^? O f- ) \r/ftT 4i4r/A/6 <=1&. ^ s' ~~ c,r /o aj ; 4" is'o^RP p^/W " M4tp/al f4 A-srsrLLoY "o " S'LeMe+J-r A*Jo urt& si-z-e ak/o sc^eu^e ; I0U Fu/ZA-^-i CALC.UL AT iOhJ DATA ~c.o. = /o Af*PUtCATi&b4 iV^r \/+JT" rt&AO&e. PLUtD ; CULOgt*JA'n=-D HyDg^>CA6o*JS . hiCUt fr/ATtt ploiv : 3 32 scFm (max) -- 92 scf=^ ('/-*/*/') re-es-svee : AO " (/JoenAC) 70 V..0 6wax) T^A-r F* ~pr ; 12 0 (mA*} t Z<3 *? f^tAx) Me-r-e^e. 7-y^e d/p c.euu Ba^o pzess /4.7 ps/a DM5/rv MoLGcuLJifZ-irfr. sob : kT F'AC.roe.-. '-P/c.v =1.13 >lp : O3" f2 orefAn+j^-r&p Note's ; ^Ff=" A 7^r">4 c~UA1aj T3 4-441-S SpFC WO FV SHEET__ ^___ OF . ^ _____ 4-81 CCR 000018493 n r\ / 'n /=* - 2 War' l/^A/7" Type ANF Drawing ` . 75 . /ANNUBAR ' C4900 (75) .-3. ANNUBAR Type. , 75 are available with optional C07 (V ,4. female NPT) or COS (socket-weld) couplings mounted on a flange on 2-1/8" centers. Unless otherwise 5. specified, these ANNUBARS are de signed for a 5" dimension from pip wall to face of mating mounting flange. This 5" dimension must be maintained when installing the mounting hardware. If mating hardware has not been in stalled, proceed as follows: 6. perpendicular to the pipe axis and square to its plane. Finish weld ing coupling. Size a short nipple to obtain the 5" or specified distance from pipe wall to face of mating flange. Weld nipple to weld coupling, making sure that it is perpendic ular to the pipe. Although the ANNUBAR is sized to a specified dimension, it is wise to avoid installation problems by checking dimensions at this time. Insert ANNUBAR through the nipple -until it bottoms at the opposite pipe wall (or into the opposite side plug, in the case of Type 76). Note dimension from outer pipe wall to inside face of ANNUBAR flange. Remove ANNUBAR. The dimension should agree with the 5" or speci fied dimension. Align mating flange to installed nipple, again making sure the 5" or specified dimension is main tained. Make sure also that the mating flange will align with the ANNUBAR flange such that the flow arrow will point directly down stream. Then weld mating flange to pipe nipple. Install flange gaskets and slide ANNUBAR into the pipe. Complete installation by bolting the 'y. ANNUBAR flange to mating flange. ; 1. Drill or burn a 1-1/16" diameter hole in the pipe wall'. 2. Tack weld a IV socketz.weld cou pling to pipe and align so it is CCR 000018495 (conoco) Engineering Center Ponca City, Oklahoma Differential Pressure Transmitters SPECIFICATION DATA SHEET PROJECT NO. f34-3ee>--93-Vw=\ A.F.E. NO____ REQ. NO..--------- y-------- DATE c8/331/ f/Q833 APP'D BY MAOE GY v/.M.F' PLANT \JCH PlArs/T LAJCS CHAgiS. LA. pan.prr tSjCl *J&l?AT`Ol5: BY-PASS ggOUCT~IQ*J 1 ITEM NO & TAG _FT- 2~ FT - / < 2 SERVICE W&T Duzecr cpLoZajAn LU 3 He-ad eg Vej t LU 4 MANUFACTURER PnSS/HOUAjr POSeM&UAlT 5 MODEL NO. //St OR //>/, OR ALPMAUHF t/J 6 FLUID VJer venr gasgs CULoG-iKtAno^ V&4rCAS<, o 7 STATE VAPQP az o 8 PRESSURE."H2.O oper(max 9 TEMPERATURE. F OPER|MAX u 10 SPECIFIC GRAVITY ra OPER. T4P. A!firs. / 40 70 12 O /2.C> /.7/9 o 11 SEAL LIQUID PLUG&OLUAS a 12 SEAL UQUIO SP. GR. v> 13 1 VApofZ, 4S* 75 0>G / 4-7 /./ 70 fcucex* cv3& I 14 TYPE -- ELECTRONIC-PNEUMATIC &LCrZOM!C. eLPCTg?KltC,, 15 SENSOR TYPE 16 Output signal 17 POWER SUPPLY REOUIREO 18 ADJUSTABLE SPAN LIMITS. HjO 19 CALIBRATED RANGE. HjO 20 ADJUSTABLE SUPPRESSION RANGE STRAtrt <9A&<Se 4--20 mA DC. Yes o- 5 0-0.3 stgai* GXcOoe 4--fOmA T>C. _________ Ye%__________ o -- S' _________G -- 2 H 21 CALIBRATED SUPPRESSION RANGE Q 22 1 MINIMUM ACCURACY 1 o 23 MINIMUM REPEATABILITY (/) UI 24 800Y STATIC PRESS. RATING 25 PROCESS CONNECTION -_ 26 1 ELECTRICAL CLASSIFICATION 27 TYP& of secv*c.e exp Poof puoH exp. ptcooffUOVY 28 1 29 30 U--JI 31 BODY < CE 32 : ELEMENT U-i 33 IP/Zecesn fCA*sGes < S- 34 1 35 AIR FILTER-REGULATOR UJ 36 AIR SUPPLY GAUGE UASTBLLOY C* /.oV " C.M HASreLLcY "C m 3Hr ss 3/U */& SS - . . .r / O 37 | OUTPUT GAUGE tuni 38 | MOUNTING BRACKET O u < 39 | 40 1 o-/o sazr \Zee. Tl clAC. o -- to soptt retncAt- 41 Overrange protection equal to static press rating 42 CONNECTIONS: AIR--1/4' NPT. CONDUIT--1/2* 43 SEE SACK OP SPECIFICATION SHEET FOR LINE DEFINITIONS 44 45 I 46 47 I 48 I 49 I 50 51 1-442 QUOTATION WHJ. NOT BE CONSIDERED IP MANUFACTURER OOES NOT COMPLETE FORM BY FURNISHING INFORMATION FOR BLANK SPACES. SPEC NO. REV_____ SHEET___ 3_____ OF _ 7^- 5-82 CCR 000018496 Cconoco) Engineering Center Ponca City, Oklahoma Pressure Transmitters SPECIFICATION DATA-SHEET PROJECT NO. I<?4 -9 -a3-VA A.F.E. NO_______________________ flEQ. NO. -___ ^________________ a 4/a*DATE APP'D BY MADE BY _ &ITEM NO. TAG < 2 SERVICE LU 3 UJ 4 MANUFACTURER 5 MODEL NO. (/) 6 FLUID o 7 STATE a O8 PRESSURE. OPER MAX z -P*o 9 TEMPERATURE, OPER MAX o @10 SPECIFIC GRAVITY OPER. T.&P. o 11 SEAL LIQUID cc 12 SEAL LIQUID SP. OR. (0 13 PT-- t r.- <*oi UCt- A6Soe.&ett RCtseMo u*j r" oe. eQutuAL*&H t veur GAses Vapcxl 80 ZS5 Boa PT -- 1 B hcl absorbed C*L GGUiVAUFNT tfeur GA&G& vapog 4>o ZSS 80 soo - 14 TYPE --ELECTRONIC-PNEUMATIC 15 ELEMENT TYPE 16 OUTPUT SIGNAL 17 POWER SUPPLY REQUIRED 18 ADJUSTABLE SPAN LIMITS, P9F "19 CALIBRATED RANGE, Q _itn 20 ADJUSTABLE SUPPRESSION RANGE < 21 CALIBRATED SUPPRESSION RANGE. PSI Q 22 MINIMUM ACCURACY Za 23 MINIMUM REPEATABILITY tn 24 BODY STATIC PRESS. RATING a 25 OVERRANGE PRESS. LIMIT * 1 &Lec-nen+j/c OiApajPAts/W NO* Q -- lOO o -- &o SU&CTfZOhitC d/ab^zagH -4 - Zo mA Ifo? O -- too o -- 80 " 26 PROCESS CONNECTION 27 ELECTRICAL CLASSIFICATION 28 y<Lo/e>*J PCUfP' FtojzcP 29 30 tn 31 BODY <UEJ 32 ELEMENT 33 5s 34 35 i-lASr&i-COY 'C hfAsr-eccor c hfAGT&LL-OY C- LtASTeLLOr c (U0J 36 AIR FILTER-REGULATOR 37 AIR SUPPLY GAUGE o 38 OUTPUT GAUGE UJtn 39 MOUNTING BRACKET oo< 40 41 42 CONNECTIONS; AIR--1/4" NPT. CONDUIT--1/2" 43 SEE BACK OF SPECIFICATION SHEET FOR LINE DEFINITIONS i :_____________ 44 B07~U ~45 puese* TGArtSrt trresz^ *4a\/G A A/trX.OGB*J tn 46 47 Z 48 49 --> CCR 000018497 50 51 52 QUOTATION WU. NOT BE CONSIDERED IF MANUFACTURER DOES NOT COMPLETE FORM BY FURNISHING INFORMATION FOR BLANK SPACES. SPEC NO. . SHEET__ REV. _ OF.*? 6-82 4-451-S (conoco) Engineering Center Ponca City, Oklahoma Indicators, Recorders, Controllers (Receiver Instruments) plant V<im PlAkj-t La<&CHacls. La. proifot \K\c.ihit=eATiQe- SPECIFICATIONJ^A SHEET PROJECT NO. t A.F.E. NO mrmREQ. NO DATE APP'D BY. WADE BY by-pass ggo^crio^ 1 ITEM NO. < 2 SERVICE 111 3 (11 o 4 MANUFACTURER 5 MODEL NO. 6 INSTRUMENT FUNCTION 7 INSTRUMENT MOUNTING 8 ELECTRICAL CLASSIFICATION < 9 POWER SUPPLY & o 10 INPUT SIGNAL Z O 11 ACCURACY u5 12 REPEATABILITY Ui a 13 LOCAT/O+J 14 15 f'rz-/ c/)\ FK- 2 <') PlgEC.T CULOZtHATTc h Wgt V&'+jt T tAGAOGfZ H&A Rswee -ZZl KEOOdDeeJlNCHCArne FLUSt-1 fZecoZo&U / av ocAraZ. P'cOSH PiC- &>( DitLecr cmloZ . ve*tr &Y-PA. E%lSTiN& INDICATOR <Zo+tT& ol u SS. . no i/ -4- ZOmA . //o\/ 4-- 2. Or-* A P>Ar4e?t. Paaj&L cc 16 NO. OF PENS OR POINTERS Ui o 17 SCALE RANGE c o 18 CHART SIZE ANO TYPE l> 111 19 CHART RANGE a 20 CHART NUMBER o 21 CHART FACTOR < o 22 CHART ORIVE a 23 | z 24 | 25 CONTROL MODE (SEE LINE 44) 2. O--iO / 4" Sr& to o - to Y / so SC PW Z-eP^ FH-l O -- ZO\T~ 4* srjZfP 0--10 V 93 '* 26 CONTROLLER ACTION Ui 27 SCALE RANGE .j o 28 SET POINT ADJ.: MAN.--REMOTE a H- 29 AUTO--MAN SWITCH ANO AOJ. o 30 OUTPUT SIGNAL o 31 32 33 ALARM FUNCTION sto 34 QUANTITY ANO FORM c<c 35 CONTACT RATING < 36 37 VU)i 38 I 39 | o 40 <U/>I 41 u o< 42 43 R.AaJG PCUCa F*>P A-ZOtnA ~TYPG AC-/37 lZAsiee RuJCj FOfZ 4 - 2Op*A TYPfr AC.-<37 44 1 CONTROL MODES: P - PROPORTIONAL (GAIN). - INTEGRAL (RESET). D - DERIVATIVE (RATE), BIAS. GAP. RAnQ. BATCH 45 | PECOROER INK SUPPLY: CAPILLARY WITH 6 MONTHS MIN. SUPPLY. AJAL. SeuSCTbt mgdolG t&-3o( FISH&Z KM !3&f 46 1 CO 47 | 48 1 z 49 s so SI * / ZDetL 4 FK.-Z. _.rvr\T OCR 98 52 4-439-S QUOTATION WU NOT BE CONSfOEREP IF MANUFACTURER DCS NOT CC*^lTE FORM 0Y FURMSMINO WDRMA7X3N FOR BLANK SPACES 7-62 SPEC NOSHEET. (conoco) Engineering Center Ponca City, Oklahoma Indicators, Recorders, Controllers (Receiver Instruments) SPECIFICATION DATA SHEET project no. A.F.E. NO......................................... .............. .................. REQ. NO. -f_______________ HATF p/Bl/PS APP'D BY MADE BY _ VMP? PLANT \JCH PUNT LJXeeUA&J&U. PROJECT / MQMggA7T)g g/-- PAS*> fZGDU CTtO 11 ITEM NO. < 2 SERVICE UzuJi O 3 4 MANUFACTURER 5 MOOEL NO. 6 INSTRUMENT FUNCTION 7 INSTRUMENT MOUNTING _j B ELECTRICAL CLASSIFICATION <h 9 POWER SUPPLY O 10 INPUT SIGNAL zo 11 ACCURACY </> 12 REPEATABILITY o 13 nc -- wer v'ewt" BY- PfirSS EXISTING <Ho/^'nCOLLE=(_ 1 I PZ-1& C-QOi RP/tESU&E. 2-poib F^essutze. /=7 SURPL Rr> -- op / RfrCOPOB /p_ EypLOS/Ot-/ P'~>r>r>tr / iov 4- -- 12.0 TMA f=t smb fa. 22 i (zeoofa&e-fe R/ USM fzyp>/ FPonA t i Ov' 4-2.0TM A / 14 15 aUacJ ouUcJ dor 16 NO. OF PENS OR POINTERS 17 SCALE RANGE IB CHART SIZE ANO TYPE 19 CHART RANGE 20 CHLRT NUMBER 21 CHART FACTOR < 22 CHART DRIVE a 23 24 | ~rv/o O -- ! OO u f-JGA f? 4V Stp>p r> - loo L/a/PAZ / o" Mi. G FzCTC> tr. pp~i. O-iOO LtMEAR -r" STA/A - l OO U/KiEAe to" M* o A L tCTZSfr. 25 CONTROL MOOE (SEE LINE 44) 26 CONTROLLER ACTION UI 27 SCALE RANGE O 2B SET POINT AOJ.: MAN.--REMOTE E- 29 AUTO--MAN. SWITCH AND AOJ. O 30 OUTPUT SIGNAL u 31 32 33 ALARM FUNCTION <zA 34 QUANTITY AND FORM tr 35 CONTACT RATING < 36 37 ... . M 36 U 39 o 40 t/i UJ 41 o o 42 < 43 I H/&M SIGNAL. SetPCTdd MODULE ME- SOZ. MlSHEZ- KM &Ol 44 ) CONTROL MODES: P - PROPORTIONAL (GAIN). 1 INTEGRAL (RESET!. 0 - DERIVATIVE (RATE). BIAS. GAP. RATIO. BATCH 45 | RECORDER INK SUPPLY: CAPILLARY WITH 6 MONTHS MIN. SUPPLY. 46 | i/> 47 | - 48 1 z 49 1 50 CCR ouuv 51 52 4-439-S QUOTATION WU. NOT BE CONSIDERED IF MANUFACTURER DOES NOT CGABRETE FORM BY FURMSHINQ INFORMATION FOR BLAM< SPACES SPEC NO_____ SHEET __^2_ 7-A2 REV.___ OF. 7 PI AMT LC vert M A TE R IA LS D ESIG N D E TA ILS _<l 11E1 z UJ u> lij tiO >b UJZ a ITEM NO. 2 SERVICE 3 4 MANUFACTURER 5 MODEL NO. 6 FLUID 7 FLUID STATE 0 PRESSURE.'%COPER MAX 9 TEMPERATURE. *F OPER \ MAX 10 11 I DIRECT READING OR RECEIVER 12 1 MOUNTING 13 1 STEM LOCATION 14 CONNECTION 15 DIAL OIAMETER 16 1 OIAL SCALE 1 7 t TUBE RANGE 18 1 ACCURACY 19 (RING STYLE 20 1 21 1 22 ! BOURDON TUBE 23 1 SOCKET 24 1 MOVEMENT 25 1 CASE 26 lLENS 27 1 28 l 29 1 TYPE: SCR D OR FLG'D 30 I PROCESS CONN. SIZE AND RATING 31 | GAUGE CCNN. SIZE 32 1 LIOUIO FILL FLUID D IA P H R A G M S E A L 33 1 BOTTOM HOUSING MATL 34 1 TOP HOUSING MATL 35 1 DIAPHRAGM MATL 36 i DIAPHRAGM FLUSH CONN. Engineering Center Ponca City, Oklahoma Pressure Gauges and Diaphragm Seals SPECIFICATION DATA SHEET PROJECT NO. A.F.E. NO DATE^^/jg3 APP'D BY *** mMADE BY J/MF_ PROJECT IMClht&AT6Z 'ASS' /Z&DUCT/QAJ Pr-- t fm2=:c.7- R&- 2. UsaD&Z v) Averse (oee CXJlY) CHL0/l4tJAT&> HY#OCMto*J 4/VX>ftCAS*lS VAPO&. Ss //> VAPO& eo /OS' LX> JA7 ______ LT* /ZO * O -- ZOGfiH*rO O -- ZOO "MtJ? 1 RL&'O /" ISO hJPT FLt/0EoW&6 HASKELL* "C* 3/4> SS i/frcAf 1 / ISO tZF /xFr FlucLol. UASrSLUPY "C " 3/6 ss STANDARD FEATURES 37 1 T(Pe Set Ytf--ASfifeaerrr 38 ELEMENT TYPE: BOURDON TUBE 39 GAUGE TYPE: SOUD FRONT W/BLQWOUT DISC 40 OWL; PLASTIC FINISH--WHITE W BLACK MARKINGS 41 i POINTER ADJUSTABLE 42 | SIPHON: MATL 43 1 PtGTAtL' MATL 44 1 PRESSURE SNUBBER TYPE 302. YH-AGUc&cer C C ESSO R IES 45 1 FLUSH MOUNTING RING 46 1 < ' A7 | 48 1 1 49 * ; so 1 I 51 I 1 r1 QUOTATION WILL NOT BE CONSIDERED IF MANUFACTURER OOES NOT COMPLETE FORM BY FURNISHING INFORMATION FOR BLANK SPACES. S-S2 REV. -- ____ OF__ 7 4-440-S NOTES CCR 0000X8500 t>vVdj Mo. VCM I 34-2- TO H5-3ot (4S-902 P?ESsl/^ TONSMirree. nstallAtiom HOTS *4 * PT--f TO BS /M&TA'LC& GaJ SpAfg& 2."a/<>ZZL 0XC-90U Rr^tBro &e t*JsrALU=& 0<v SPAP& ZSMOZZLB OAT C-$G/8f VMF" whiles ZCa/C/A/&#A7-B& Hypass ~7?epttc.n **4 ie&- 900-333 - VM1= CCR 000018501 _ CCR 000018502 R. A. Conrad * (conoco) Date J /tsr /<-, w CCR 000018503 ?