Document zQ3zQEmQY3Z4mpG4VZJ5OmQwz

4*.fVt, rXc 1 1* Authority Petrochemical Department__L. for Expenditure Autb. No* CAPITAL 1-34- # rriittyylTTtffeeqquurrsstf'' 1' to expend (Show Cash and Warehouse Outlay Amount) j ..?9/000_ fW iLow Pressure Condensate Recovery System Location VCM Plant - Westlake, Louisiana Reason (Explain Folly) Presently, condensate from ten users Is being discharged to the sewer* In addition to the loss of 34,558 pounds per hour of condensate, the present mode of operation causes corrosion of the concrete paving and is hazardous, particularly during cold weather when the possibility of icing and fog exists. A condensate recovery system, consisting of collection headers, a flash drum, steam condenser and return pump, will recover the condensate. Some of The condensate is ODrained from heaters and reboilers which have corrosive material (HCI) on the process side at a higher pressure than the condensate. To protect the boiler plant in the event of a leak in any of these exchangers, a conductivity cell will be placed in the condensate flash drum. The cell will detect the presence of small amounts of HCI, shut down the return pump, aj^^mpty the condensate flash drum to the sewer. The value of the recovered condensate (less operating cost) is approximately $10,500 per year. The $29,000 investment will yield a 19 percent DCF return based on a ten year life and straight line depreciation. In addition to the economic advantages, this project will reduce outfall temperature thereby reducing our thermal pollution problem. Signed: A V1/- . ^ -/T Approved: r7\ A 6a R. IT.-Geriacb Chief Process Engineer L. N. Vernon Plant Manager Distribution: MBM-MPL-TWS-RWG-GBM-LNV SUMMARY CT COST Material: Air Cooled Condenser, 1027 gallon tank, 25 HP pump. Collection headers, Auxilliary Piping, Valves and Instrumentation, bor for Installation: OTHER MATERIAL | ON HAND CASH AND WAREHOUSE OUTLAY $20 200 $ 8 800 Is thhts project prouted for in c.u rrent Budget? . Yes If soo in what *7-w+"t rLr?0G_ , Project No.. If not shou cnnitnge-ii y or allocated project number. V-8 DISTRIBUTION n,/, August 22, 1969 \ Material Investment < / Intangihlrs Expense Total 1 ions y. . Correct Mv UUU ! Signed. ^y:? j Grand Total $29jOOO Signed, TOTALS GRAND TOTAL Approved: Date. / $29 000 $29 1000 CCR 00007990 Autb No. . 1-34- LOW PRESSURE CONDENSATE SYSTEM Process Description The low pressure condensate recovery system will collect steam condensate from the following services (gaseous steam is collected from the oxy blowdown drum): 1. EDC Tar Stills 2. Vinyl Tar Stills 3. r-304 Feed Heater 4. Oxy Vent Heater 5. Oxy Blowdown Drum 6. HCl Feed Heater 7. Ethylene Feed Heater 8. HCl Evaporation 9. HCl Reboiler S-104 A & B S-208 A & B H-304 H-310 S-311 H-309 H-308 S-210 A & B H-205 In addition to these services, we plan later to tie-in the condensate that drains from the R-304 steam vent line plus the bleed stream from the propylene K. 0. drum plate coils. The condensate is collected in a 1028-gallon drum (S-612) that is connected to a 15 H.P. air cooled heat exchanger (H-612). The heat exchanger condenses any flashed condensate in addition to the steam coming from the oxy blowdown drum. A small bleed is provided on the tube side of this exchanger to remove any inert gases that are trapped in this system. These inerts can cause corrosion or gas blinding of the exchanger. The level in the condensate drum is automatically con trolled by a local controller. The collected condensate is then pumped, on level control, into the steam plant condensate return line for reuse. A pump recycle restriction orifice is provided to prevent the pump from overheating during low load operation. The system is designed to handle 43,500 lbs./hr. condensate. The condenser is designed to handle 7200 lbs./hr. of flashed condensate and has a 7,000,000 BTU/hr. duty. Under normal conditions there will be 30,660 lbs./hr. of condensate, and the condenser will handle 5572 lbs./hr. of flashed steam. The flow to the steam plant condensate return line will be 64 gpm. A separate condensate collection line is run from the HC1 feed heater (H-309) to the condensate drum to eliminate freezeup problems which could occur if its condensate did not drain properly. Condensate collection pots are installed in the condensate lines from the oxy vent heater (H-310) and the HCl evaporators (S-210 A&B) because of similar freezeup problems. A separate line is run from the oxy blow down drum to the condensate drum to handle the steam flow from this drum. As a precaution against possible condensate contamination by HCl system leaks, a conductivity probe is mounted in the condensate collection drum. The board-mounted conductivity meter reads 100 000007991 OCR micromho's full scale. As a point of reference, distilled water has a conductivity of about 2 micromho's. For each ppm of dissolved salts the conductivity will rise about 2 micromho's; a ppm of HC1 will raise the conductivity about 5 micromho's. Readings on this meter normally show a conductivity of 10 micromho's which represents about 5 ppm dissolved salts - this is considered to be good quality condensate. If the conductivity exceeds 30 micromho's, an alarm will sound, a dump valve on the condensate drum will automatically open emptying its contents to the sewer, and the condensate pump (P-610) will be shutdown. In the event that this occurs, the system will have to be manually restarted. Any conductivity reading that is "on-scale" will probably be good; any salt or HC1 leak will probably "peg" the meter causing the dump valve to open. To prevent the condensate pump from cavitating under low level conditions, a low level sensing switch has been installed. This switch will shut down the condensate pump; the pump must be manually restarted if this occurs. ^ To provide protection against either high drum pressure or a high liquid level, a 3" loop seal pipe has been installed. In either case condensate will overflow through the loop seal into the sewer (steam will not vent out of this loop seal because its inlet at the condensate drum is extended to within a few inches of the drum's bottom). One possible operating problem that can occur in this system is at the oxy blowdown drum (S-311). This drum collects the hot blow down water from the oxy reactors' steam drums and flashes off low pressure steam which is piped to the condensate recovery system. The remaining blowdown water is manually drained to the sewer. If this drain is closed, the drum will fill up with liquid causing contami nated water to flow into the condensate system which will cause a high conductivity reading. CCR 000007992 Conoco Petrochemicals JDM CGNTJNCNTA.L O/L COMPANY PETROCHEMICAL DEPARTMENT, V.C.M. PLANT P. O. BOX 605, WESTLAKE. LOUISIANA 70669 phone, 31B-433-63U September 8, 1969 Mr. George Furgeson Placement Director Louisiana State University College of Engineering Baton Rouge, Louisiana Sir: The enclosed project entitled "Low pressure Condensate System" has been successfully completed by Mr. John C. Lunn, Jr. during his employment at tne VCM Plant of Continental Oil Company. The project has been review ed by the plant management and is now approved for construction. If is expected that work on this project will sfarr in late October and, hopefully, will be completed by the end of 1969. We consider the report to be a good, complete study and design project and recommend that it be accepted as proof of completion of Chris' Engineering Practice Number 149 course. Very truly yours. JDM-MC cc: Mr. R. H. Gerlach Attachment /} /John D. Minoft Sr. Process Engineer - Continental VCM Plant CCR 000007993 ^ Conoco Petrochemica CONTINENTAL OIL COMPANY PETROCHEM.CAL DEPARTMENT, V.C.M. PLANT P. O. BOX 605, WESTLAKE. LOUISIANA 70669 PHONE; 31 S'43 3-6 311 August 29, 1969 Mr. George Furgeson Placement Director Louisiana State University College of Engineering Baton Rouge, Louisiana Dear Sir; The final design of the low pressure condensate system was completed Aug ust 29, 1969. The completed project is attached to this letter for approval by the College of Engineering. A summary of the steps used in the design of this system is also attached. Because of Continental Oil Company's licensing agreement with Stauffer Chemical Company detailed descriptions of other projects are not permitted. However, general descriptions of some summer projects are presented as fol lows; 1 . Design of a breather valve and vent line system for a storage tank (drawing attached). 2. Design of a nitrogen purge system on a relief vent (drawing attached). 3. Revision of a condensate system for a column. Specification of line sizes, pumps, condenser, and instrumentation was necessary. Con denser revision cost was also estimated. 4. Design and cost estimation of a caustic wash and decanting system. Design included specification of mixers, piping, tanks and instrumen tation. 5. Study of the justification of a spare reactor. 6. Reranging flow meters. CCR 000007994 Mr. George Furgeson page 2 7. Study of the percentage loading capacity for rail cars used for product shipment. Calculation of expansion factors. 8. Data collection and plotting of a chart giving the operating con ditions of the oxychlorination reactors in the VCM Plant. 9. Design, justification, ar.d cost estimation of a column feed preheater for the 1970 capital budget. 10. Collection of plant data for exchange with a similar Japanese VCM plant. 11. Visit to Continental's Ponca City, Oklahoma operations. Included .ours of Process Engineering Group, Central Engineering, Maintenance Engineering, Refinery Process Engineering, and Petrochemical Research and Development. Other summer work consisted of general plant process engineering similar to the above projects. 1 hope this summary is satisfactory for completion of Engineering Practice 149. Very truly yours, X 5_ yXAv - John C. Lunn, Jr. Chemical Engineering-4 Student No. 438-74-0886 JCL-MC cc: RHG-JDM-DKP Attachment CCR 000007995 Low Pressure Condensate Design Outline The basis of design for the low pressure condensate system is to recover condensate which is presently being lost to the sewer. Actual operating pressures on the various steam users were too small to allow the use of the existing condensate system. The steps followed in justification and design of the low pres sure condensate recovery system are presented as follows: 1 . Justification A survey was made to determine the amount of condensate being lost to the sewer. From plant cost, a value was placed on the condensate loss for one year. Using a discounted cash flow (DCF) of 18%, a justifiable invest ment was calculated. The design cost of the condensate recovery system was required to stay under this value. 2. Piping layout The next step in the design was to locate each unit and make a rough piping and equipment layout. These approximate dimensions were used in line sizing. 3. Preliminary Flowsheet A preliminary flowsheet including material and energy balances was then prepared to be used in line sizing. CCS 0007,,6 4. Line Sizing Using the method of Cnenoweth and Martin for two-phase flow (Pet. Ref.-1955), the various condensate headers were sized. Sizing began at the condensate drum. Line sizes were calculated to keep the pressure drops below the operating pressures of the various steam users. Lines were sized assuming all horizontal pipe, all condensate flashed to atmos pheric pressure, and 10% greater flows than original plant design. 5. Equipment Specifications The next step was to size and specify the major pieces of equipment. This included specification of a pump, an air-cooled condenser, a condensate drum and the various instruments used to control liquid levels. 6. Alarm System Because of the possibility of acid leaks Into the condensate system, a conductivity alarm system was specified. A conductivity probe is located in the condensate drum. Upon detection of a leak, a control room alarm will sound, the condensate return pump will shut down and an automatic dump valve will empty the condensate to the sewer. 7. Flowsheet A detailed flowsheet was then prepared. 8. Equipment Prices Quotations for the larger pieces of equipment (condenser, alarm, and pump) were then obtained to Insure remaining within the justified invest ment limit. CCR 000007997 9. Work List A work list was then made outlining the steps to be taken to install the ! ow pressure condensate recovery system. 10. Cost Estimate A final cost estimate was then made for the system and a DCF was calculated. The design was then submitted to the plant Senior Process Engineer and Chief Process Engineer for approval. Following approval an AFE (Authority for Expenditure) was written and the design turned over to the plant Mechanical Department for construction. CC* 000799a .2 ^r4c :/ VO H V ** *- * m x S' 0^H 0P ,,r 0r ;- *c :w Head sn. i LOvaDPrESSORE CoNDCMtaTS SV%7*-\ _w= 4 DO ib >/hr w 1 l( >7o */ 40 \b S/ Wp> _U) = $9 \b< !/iec 4* 07 >03 = ^ | - \b / 6Ec. _Gj- 4 7' IS 00 E+ >/4r '' T X Cr Lt JLf m ON _G p. U QC >\0 ,,\/ DLv. M* i -R VO *_K >KJ uv [-- f- 4- s 1 io 0 *\ lii iOi. kV lfc< 4" >0 1 *. 4t Li O <SC o > - ( 4O > ) 16!>.0 7 > * 10 ,3 * * H- -- r 2 &, (a * _% SJp v< )LO me Cs> ir?So. } (4. 1 l" ! 1 X 0. 0\ 5a 2_ -- TO tai -J? _. ----~Wl 9" Co -St LV F- Co 14 5, Co. (0 (V)3Jl ) <2> _C W-! LJJJ -fVrio K<> " OF Jy BY UOlJOt .-V OHTie R -x .** LO \ i; . JD. \ "Rl CB OH p C7 OR -fe M- > " %~2 .0.^1 D|f 2 #/ pri iR 3 II t?J?L J_ \ (s' >0 V '. Jr ^ c >. C b` 70 r S.X . I*P 4* ). < >oJ "5 :n 3.( d4 Kl( [ (f i X 10 5 6. Oc -s D - ~r o. 0 c 4" 7 : i A LL_ cc R 300 00 9001 Made by____ _ Q~~7-- Checked bydate_____ ____ PAat_L--------- or-3. ' CONTINENTAL OIL COMPANY CALCULATION SHEET % Job No. FuOiO -- MeiUoo OF OtttUOWEYH ako MOrrm .TITLE......................................... .................-.:?lgT HiKFinn tky* WM IfipePiMr IK 2' k "| i 5 C? r\i Aj .* u 3! -KEuzms 3 !I1 VTF| VRLOtf L/b- 13 7t >7 : l - -- >8 7 V 1 ir >s L ... >/ B -- D_: * -- -- ---- -- El ou T -- "e CHA T vr E ao /IAlA.1 <T ---- K LCNh>TM (*) vs Leu *T>\ **) K AV) L4 TM A < 7 ec e>cuyb Ls>cf). C (a 4- 50 s 53 .7 T a e b. p Lh - 10 ..... *BRN i>. LAk SO c i.*: >0 7C * * - * 'i TH ER ' s 2) C3 -> <>.3 0 ? ' \ T or OL 3 U------- 1 l THL +. E&.L ENS 3 9>- e ,7 4 3` ` * Vc V , IT,.v " ;o. 7t ,6 s H * , t 1r % t- l- f MAOtBY. ________ Checked by________ ________ n ' Date _______________ ________ Pace__2.____op__3____ .TITLE. CONTINENTAL OIL COMPANY CALCULATION SHEET i CCR 000008002 Job No.. . Field.State. L (&, C^u<;ov.t\T\ow or >- ^Prp/i a.?, "C,__ __ (orooT;>5D)(i^<prl 3:*fr (c oo 70x a^y8 ) J- 3 to.o^iX 12 )* 375 % (o,oo7ti) (i2o\ 'l J- 3 ,-5 Vc y( 1 Hy s, 2?> 7 l-(s> .9 3 </*PJ ra~-Eg FHROi &YAf*A I &ARtp> lfe95 -l H- c(. 2>> &a A (oO 3~k aul too* - 1JVI i4a JLmJ&O ^PkTYt M OF -* APl-- I MjJ 0. Qooote^fc uw ipe\P,AMntF I |L 3* o.oo op o 6,2 26 V w fi * 4? // 2.26 XioT (0C|07 Is 03 C 1 9l-ZSxin-7(<p.OOT|5>( 331 Ml I fo j ail,A). 2.2`pX Orff 1 3 FaiJnxviL V el Let| - G^OxLauFMT Lffi 6"TH Ap APtp \4ia| - *0.18 H^>8 V40 iI CrSj i3 u i .j*a Made by Checked by_________ ___ DATE.-- ------------ 1 -- Page_3__ of__3- TITLE. CONTINENTAL OIL COMPANY CALCULATION SHEET 1 Job No.. > Field.State . CCR 0<>0008003 SUBJECT T?-$04 steam Cdmticou Uftuvt a <5 t\UG>TO *OR*f >17911 QUOTATION POTJ2PS CENTRIFUGAL PUMP REPLY TO: GOULDS PUMPS, INC. 5828 'Star Lane, P. O. Box 25146 Houston, Texas 77005 Ph: 713 782-7530 All quotations subject to terms and con ditions on the reverse side and expire unless accepted within 30 days from date of quotation. All quotations subject to change with or without notice. To:Continental Oil - VCM Plant P.0, Box 3605 Westlake, La. 70669 Date: 9-26-69 Proposal No.:699-716XK Revision No.: Page; 1 of 2 Attention: Betty Peloquin Inquiry Date: Inquiry No,: Verbal/Betty . N. Copies: Continental Oil Hosea In answer to your inquiry, we propose to furnish GOULDS PUMPS as described below: CONDITIONS OF SERVICE -- LIQUID___ 100" G.P.M.. Suet. Lift. ~orr~cp Vise. P.T.. ph value. T.D.H. Abrasives Steam Condenaate-Water 313 ` 212*7? Disch. Press.. 131.5 Sp. Gr. 60 F., N.P.S.H. Avail.. Solids. % Suet. Press Sp. Gr. @ P.T. N.P.S.H. Req'd. 3.32 0.96 575 Solids size (3) Cl) PUMP DESCRIPTION -- One QUANTITY 7J751 MODEL Case Impeller Size 7T"" Group "One Stages Shaft Wearing Rings Shaft Sleeves For detailed specifications see Bulletin cx cx Steel CT cl 7T57T DRIVER. 20 H.P. TEFC Enclosure 3500 R.P.M.. tt Insulation. UNIT PRICES -- PUMP, BEDPLATE and COUPLING ........................... $ __ PackedPutnp 384.00 Lubrication Bedplate Coupling Grease CX Falk Direction of Rota^jgri from Coupling End . "TI4TC Performance Curve Efficiency 50% 7372" B.H.P. Rating T975 Max. B.H.P. IMPELLER DIAMET^t: Approx. Rating 7/8 Min. / Max. ________ /__ 3/60 Phase/Cycles ~256T~ Frame 338 Weight, pounds: 230/460 Volts Goulds' Furnished bv PRICES AREF.O.B.. SENECA FALLS, N.Y.. driver .............. ......... FREIGHT (estimated) TOTAL UNIT PRICE ,, Extra for oil lubrication- 248.00 30.00 $662.00 ----------------___________ 230----- 10 SHIPMENT:Weeks after complete engineering and manu facturing information and full ap proval to proceed with work. 3M TOTAL WEIGHT $40.00 TERMS: 30 DAYS NET TT-.e following outside tquismant not of our rnaruV.^re to subject ta the sane pctctn`.s;e o! price insresss as may madj by o'T supplier to ui - "MOTORS". CCR 00008005 BULLETIN 72S.1 November 28, 1868 Sup. Bui. 1 -31 -66 STANDARD DIMENSION PROCESS PUMPS For Industry: CHEMICAL PETROCHEMICAL PULP and PAPER PRIMARY METALS GENERAL SERVICE APPLICATIONS RANGE OF COVERAGE Capacity.............................. 5 to 1,600 GPM Head.............................. 10 to 750 feet TDH Temperature.............. --350 t + 500s F. Working Pressure........ 0 PSIA to 375 PSIG GOULDS PUMPS & ^STANDARDIZATION Goulds offers you: 1. The most complete and experienced line of standard dimension chemical pumps; 2. Thousands of sizes and models of other pumps to fill your many requirements -- double suction pumps, vertical pumps, glassed pumps, multi-stage pumps, centrip etal pumps and heavy duty process pumps. Over six years ago, Goulds introduced a line of standard dimension process pumps for the chemical and allied industries. The design of this line provided both flexibility and inter changeability within the framework of practical standardization. User acceptance of the Goulds design stimu lated the forces interested in the benefits of pump standardization into action. American Voluntary Standards by a number of pump manufacturers developed. Today thousands of Goulds "standardized'' chemical pumps are in service. It is Goulds intent to continue to be a leader in this effort by providing users not only with the most experi ence but . . . the most practical design . . . quality . . . and service! Note the table below. You will see that in regard to the standard dimension pumps that Goulds gives you maximum hydraulic coverage beyond that recommended by AVS ... all con forming to AVS dimensional specifications. American Voluntary Standard Designation* and Length Gaulds STD Model Number Goulds Basic Standard Units Goulds Bonus Alturnatu 3196 Units AA-1V/2 AB-U'/j A05-23*/2 A10-23l/2 A20-23'/, A30-23|/j A40-23i/j A50-23'/j A6O-23I/2 A70-23V2 A A75-23'/j A A80-231/} 3197 3197 3196 3196 3196 3196 3196 3196 3196 3196 3196 3196 1 x 1 !/j-6 11/2 x 3-6 1 x 2-8 2 x 3-6 11/2 x 3-13 2 x 3-13 3x4-13 1l/2 X 3-10 2 x 3-10 3 x 4-10 4 x 6-10 4 x 6-13 1 x 2-6* I'/j x 3-6* 1'/2 * 3-8D 2 x 3-8D 3 x 4-8 and 3 x 4-8SD QThs bonus alternates are dimensionally interchangeable with the corresponding Goutds Basic Units. These alternates allow complete standardization with 231/2" sizes. A Goulds recommendation for AVS adoption. 2 GOULDS Model STD DIMENSIONAL INTERCHANGEABILITY Shown below are the constant dimensions that apply to both the 23 and 17'2" standardized chemical pumps. Goulds concept of maximum dimensional interchangeability is the "design key" to the inter changeability and flexibility benefits that users ob tain with pump standardization. Model 3196-STD 2314 INCHES LONG ALL 16 SIZES A ONE length for all sizes--2314" B ONE coupling for all sizes--l'/s" C ONE dimension end of suction to centerline of discharge--4" D ONE bolt size to hold to base--W E ONE bolt spacing F ONE spacer coupling length for all sizes--314" Model 3197-STD 1714 INCHES LONG 2 SIZES A ONE length for 2 sizes--1714" B ONE coupling for 2 sizes--J4" C ONE dimension end of suction to centerline of discharge--4" D ONE bolt size to hold to base--Vi" E ONE bolt spacing F ONE spacer coupling length for 2 sizes--314" GOULDS GIVES YOU MAXIMUM FLEXIBILITY BETWEEN BOTH PUMPS AND PUMP PARTS In addition to bonus sizes in the Model 3196-STD, Goulds gives you a choice of bearing frame and shaft arrangements. You can mount pump ends on S, M and L bearing frames with corresponding 1M", 1M" and 2 ^"shafts, or all pump ends on one frame. This flexibility provides for selection on the basis of an economic evaluation as well as these other necessary considerations: technical design, plant inventory, future system changes, and maintenance require ments. Evaluation of all these factors will lead to a sound selection by the process engineer. Goulds allows the process engineer to make the choice, the best choice for his company. CCR 000008007 PUMPS offer maximum user benefits THE GOULDS LINE ALLOWS A "CUSTOM FIT" STANDARDS PROGRAM FOR YOUR COMPANY The minimum "AVS" offerings shown below may not always provide the best coverage or efficiency to meet your company's needs. Goulds, therefore, offers you a bonus of additional sizes. This allows you to custom tailor a select number of sizes that will give you both minimum parts inventory and maximum hydraulic efficiency ... all within "AVS" dimen sional standardization. 17'/z" STANDARD SIZES f|jf 23'//' BASIC STANDARD SIZES IZVi" BONUS STANDARD SIZES BULLETIN INDEX page Design Features 4 Specifications 6 Section Drawings 8 Parts Lists 9 Construction Details 10 Pressure Temperature Data 10 Composite Rating Data 11 Performance Curves 12 Bearing Frame Selection 17 Material Specifications 17 Bearing Life Information 18 Dimensions 19-20 STANDARDIZE ON 23%" SIZES FOR OPTIMUM STANDARDIZATION The American Voluntary Standards established eight 23'//' and two 1714" pumps to cover the full range of temperature, head and pressure requirements. Goulds gives you the plus benefit of completely cover ing and far exceeding this range with sixteen 23*4" sizes . . . one bearing-shaft unit to handle all sizes. This is the optimum in pump standardization that offers users maximum benefits. ccR 000008008 3 GOULDSTHE PROVEN DESIGN FEATURES OF MODEL STD MAINTAIN CONSTANT EFFICIENCY WITH GOULDS EASY EXTERNAL ADJUSTMENT You do not need to disassemble pump to renew running clearances. Impeller clearance is set by telescoping thrust bearing housing into the frame through a precision fit. This is all you do . . . it's simply a matter of minutes: 1. Use a common open-end wrench to loosen bolt "A" (top). Ease impeller assembly (shown in blue above) forward until it contacts casing. 2. Turn jacking bolt, "B" 1 flat, which backs up impeller establishing the proper running clearance. With Goulds Model 3196-STD this is all there is to maintaining the correct clearance for constant NPSH and pump performance. You don't disturb gaskets or run the risk of damaging oil seals. Also, with no disassembly, downtime is kept to a minimum. When it is consistent with routine maintenance, impeller clearances can easily be set on the power end "on the bench." This method of external adjustment has been a feature of pumps Goulds has supplied for process applications for more than 25 years- MAINTAIN POSITIVE ALIGNMENT WITH GOULDS PRECISION ALIGNERS Precision aligners (shown It. blue) align bearing frame, frame adapter, and casing. Aligners are minimum tolerance-interference fit components. They eliminate the inherent mis alignment caused by an accumulation of machin ing tolerances in a series of lock fits. This is the same method of obtaining precision alignment that has long been used by the machine tool industry in the best grades of precision ma chinery . . . machines costing many thousands of dollars. Aligner holes are bored and reamed in the same machine setup and at the same time as the critical bores in the part. Their position with respect to the bore is held to a tolerance of three-ten thou sandths of an inch, and the diameter of the hole itself is held to within two-ten thousandths of an inch. The precision ground aligners are held to similar tolerances. There is never any question that any subsequent repair parts will always fit perfectly, and be in alignment. Aligners (C) are tapped for easy removal by standard cap screws. Goulds precision aligners will save you time and money on pump disassembly and they assure "like new" alignment when you put a pump back in service after maintenance. CCR 000008009 4 THE IMPELLER DESIGN PROVEN BEST FOR CORROSIVE/ABRASIVE SERVICES Impellers are fully open, with partial shrouds for maximum vane support. Large, smoothly contoured flow passages combine best slurry and solids handling ability, yet meet low NPSH requirements. The shearing action of the impeller vane on the casing wall prevents brakebanding. Back pump-out vanes keep solids from behind the impeller and reduce pressure on the stuffing box. This impeller design is first choice for corrosive/ abrasive liquids because wear is distributed over the complete vane surfaces and the complete casing area swept by the impeller. Wear is not concentrated in a small close tolerance, high velocity area as it is with closed or semi-closed impellers. Example: A typical open impeller pump size 1V2 x 3 10 will have a wear area of a 10 inch circle with a 3 inch circle out of the center on each side of the impeller. Area Formula = -- ^Dl` " D2^ 4 = .785 (100-9) = 71.5 in2 per side Total Wear Area = 143 in2 The same size closed impeller would have two 3 inch diameter wear rings or a total wear area of 28 in2. The closed impeller would have approximately the same wear concentrated on ]A, the area. The open impeller, therefore, can take about 5 times more wear than a closed impeller before performance is reduced and NPSH requirements increased. Semi-open, or semi-closed, impellers with horizontal wear areas do not overcome the closed impeller design weakness of the close tolerance wear area. Type 9 Single Unbalanced Inside with Water Cooled Box Type RO-TT Single Unbalanced Outside with Carbon Restricting Bushing Type 9B Balanced Inside with Quench Style Gland Type RO-TT Double Unbalanced Inside OPTIMUM SHAFT SEALING AND COOLING ARRANGEMENT FLEXIBILITY A wide variety of shaft sealing problems are encoun tered in practice. Many of these problems become apparent only after the pump is installed or after process changes are made. Therefore, a wide variety of sealing approaches must be available to the pump user. The following features show some of the flexi bility available in Goulds model STD units. 1. Stuffing box fully machined and faced to accom modate either packing or mechanical seal. No machining required to convert in the field. 2. Jacketed box available for heating or cooling to maintain required stuffing box temperature. 3. Special shaft materials and hard facings for severe corrosion and abrasion problems. 4. Renewable hook-type shaft sleeve available. Sleeve can be supplied in special materials and inexpensively replaced. Stepped sleeve allows easy application of balanced seals. CCR 000008010 GOULDSSPECIFICATIONS- MODEL STD in maintenance. Adapter houses stuffing box drip basin, non-spark ing rotating deflector and inboard bearing oil seal. Either frame adap ter or drip basin may be piped to drain. On Model 3197, adapter is integral with bearing frame. CASING AND IMPELLER Top centerline discharge, self-vent ing casing, arranged for back pull out. Fully confined gasket. Foot support under casing for maximum resistance to misalignment and distortion from pipe loads. ASA 150 lb. flanges standard, 300 lb. optional for working pressures to 375 PSI with corrosion allow ance. For maximum corrosion- erosion resistance casing is supplied without tapped openings, but gage and gasketed drain plug openings are supplied when specified. Impeller matched to casing for high efficiency and low NPSH. Fully open, has partial shrouds for maximum vane support without high thrust inherent in full shroud designs. Impeller is screwed on shaft, and threads are sealed by a Teflon O-ring. This eliminates pro jecting impeller nut and exposed threads from impeller eye. Smoothly contoured passages for good solids and slurry handling. All impellers statically balanced. STUFFING BOX COVER Stuffing box cover encloses back of casing, and contains stuffing box chamber. Cover is bolted to frame adapter so that a spare back pull out assembly can be stocked com pletely assembled. Cover can be supplied with jacket for cooling packing or seal in high tempera ture services. Jacket can also be used for heating when handling viscous or high freezing point liquids. Packed box has 5 rings of packing and a lantern ring. Quench gland with quench water taps and an auxiliary ring of packing is stand ard. Gland is split, and can he com pletely removed for easy repacking. Tapped openings to the lantern ring permit "in and out" sealing, ex ternal flushing or lubrication as required. Stuffing box is completely ma chined for mechanical seal installa tion, either originally or as a field con version. Inside, outside, double and balanced seals, with any required quench gland, restricting bushing and flushing line furnished to meet individual sealing problems. Gland completely confines stationary seat gasket. Both packed box and mechanical seal can be used with either solid or sleeved shaft, depending upon application and user preference. FRAME ADAPTER Machined with precision aligners as reference, to keep bearing frame and casing in perfect alignment. Fur nished with lifting eyebolt for ease BEARING FRAME, SHAFT AND BEARINGS On Model 3196 the liquid end of the pump can be driven by any one of three pump shafts (1J^", 1%", 2J/g") with corresponding bearings (307, 309, 311) depending upon the severity of the process application. The over-all length of the pump (23 J^") is the same for all combina tions. The two sizes of Model 3197 have 1 y% shaft, and overall length of 17 %?. BEARING FRAME Heavy cast iron construction with precision aligners to maintain align ment with frame adapter. Contains large oil reservoir, water jacketed. Oil level is maintained at proper level by means of a constant level oiler with visible. oil supply. Oil breather vent fully protects oil from contamination while allowing for expansion or contraction of air caused by ambient temperature change. Model 3197 has frame adapter integral with frame, not water jacketed. qO 6 .G* SHAFT AND SHAFT SLEEVES Shaft is designed for .002" maxi mum deflection at stuffing box face. All bearing and packing surfaces ground to less than 32 micro inches. Threads where shaft screws into impeller are sealed by Teflon O-ring. Choice of shaft with or without sleeve for utmost flexibility in solv ing sealing problems. Renewable shaft sleeves are posi tively driven, hooktype with one end free to expand with tempera ture variations. Teflon O-ring pre vents leakage under sleeve. The hooktype shaft sleeve permits ap plication of inside balanced me chanical seals where required. BEARINGS Inboard bearing is pressed on shaft and is free to float axially in frame, to carry radial load only. Outboard bearing is shouldered and locked on shaft and in bearing housing to carry radial and any unbalanced thrust load. All bearing fits are precision bored. Inboard bearing is single row, deep groove. Outboard bearing is double row, deep groove angular contact, as standard. As an option, a single row outboard bearing iden tical with the inboard bearing may be supplied. Both radial and thrust bearings are sized for minimum two year life. See page 18. CAST IRON R STRUCTURAL STEEL BEDPLATE Each bedplate takes a range of NEMA frame motors. In most cases a larger motor can be added (or a larger pump) without changing bedplates. Four bedplates take any size motor required by any pump. Cast iron bedplate has camber top to prevent liquids from being trapped on bedplate, and grout and vent holes for proper grouting to foundation. Steel bedplate has raised drip lip. Either type can be jackscrew (inline) or spring suspension mounted for low est installation cost. MATERIALS OF CONSTRUCTION Goulds 3196 can be manufactured in any machinable alloy service conditions require. Goulds inventories units and parts in the following materials: Ductile Iron, heat treated (ASTM 395-56T, Type 60-45-15) Cast 316 Stainless Steel (ACI-CF-8M) Gould-A-Loy 20 (ACI-CN-7MCU) For detailed Materials of Construction Table see Page 9. DUCTILE IRON ... a standard material Ductile Iron, sometimes referred to as Nodular Iron or Spheroidal Graphite Iron is produced under a licensed process of International Nickel Company. In this process the shape of the graphite particles, which are essential in gredients of iron, are changed from flat flakes to spheroids. The spheroid graphite particles have much larger areas of iron matrix between them, and since they have no sharp edges, ductile iron exhibits much greater tensile strength, yield strength, ductility, impact resistance, and resist ance to thermal shock than gray cast iron. Ductile Iron approaches carbon steel in physical properties at appre ciably less cost. The corrosion resistance of Ductile Iron is comparable to that of gray cast iron; thermal expansion comparable to carbon steel. One hundred times photomicrographs show graphite formation and distribution for High Strength Gray Cast Iron and Full Ferritized Annealed Ductile Iron. 1 Tensile Yield Elon* Colt Strength Strength gition Ratio Notes ! [Cast Iron A48-56 30.000 PS1 0 0 1.0 ! Goulds Ductile Iron (ASTM A39S-56T) 60.000 to 45.000 to As Heat 70.000 PSI 50.000 PSI 15-2555 1.1 Traatad to Full Ferritized Anneal n%1 Corbon Steel lASTM A-216-59T-WCB 70.000 PSI 36,000 PSI 1.7 STEAM JACKETED PUMPS AVAILABLE The table at the right shows sizes of Model 3196 pump which can be supplied with a steam jacketed casing for han dling liquids which solidify at ambient or above ambient tem peratures. The jacketed casing is normally used with the jack eted stuffing box cover to pro vide a completely heated liquid end. This construction easily handles high melting liquids such as sulfur, naphthalene, tars and waxes. / SIZES AVAILABLE 1 x 2-8 3x4-8 2x3-6 2 x 3-13 VA x 3-13 3 x 4-13 Hi x 3-10 2 x 3-10 3 x 4-10 4x6-13 CCR 000008012 7 SECTION DRAWING Model 3196-STD 412 361A 113A 168 333A 123 370B 360A * 132 184 370A 360B 351 370G 122 469B 210 353 355 107 247 106 469A '''Upper half of Stuffing Box shows Type 9 Unbalanced Mechanical Seal. Lower half shows Packing. Model 3197-STD 332A 370D 361 111 112 361A 113A 168 123 333A 228 122 107 370A 106 105 101 100 8 CCK 00008013 Group "S" Construction Showing NonCooled Stuffing Box and Solid Shaft. Water Cooled Stuffing Box Showing Shaft Sleeve Construction. PARTS LIST POWER END PARTS NUMBERS ON SECTIONAL VIEW SHOWN IN BLACK No. Item Req'd No. Per Pump Part Name 105 1 Lantern Ring 106 1 Set Stuffing Box Pecking 107 1 Gland --Packed Box 111 1 Bearing Housing 112 1 Ball Bearing--Outboard 113-A 1 Bearing4Frame Breather 122 1 122-A 1 Pump Shaft (Less Sleeve) Pump Shaft (With Sleeve) 123 1 Deflector 1260 1 Shaft Sleeve 132 1 Eyebolt 168 1 Bali Bearing--Inboard 210 1 Gland Packing 228 1 Bearing Frame 247 1 Drip Basm 251 1 Constant Level Oiler 309 1 Shaft Bushing 332-A 1 Oil Seal (Outboard) 333-A 1 Oil Seal (Inboard) 353 2 Gland Stud 355 2 Gland Stud Nut 360-A 1 Gasket (Bearing Frame to Frame Adapter) 361 1 Retaining Ring (Shaft) 361 -A 1 Retaining Ring (Bearing Housing). 370-A 4-12 Hex Head Mach. Bolt (Frame Adap. to Casing) 370-B 4 Hex. Head Mach. Bolt (Frame Adapter to Bearing Frame) 370-C 3 Hex Head Tap Bolt (Bearing Housing) 370-D 3 Hex Head Tap Bolt with Jam Nut (Impel. Adjust.) 370-E 2 Hex Head Mach. Bolt with Lockwasher (Casing Foot to Casing) (Not lllus.) 370-F 1 Dowel Bolt (Frame to Frame Foot) 370-G 2 Hex Head Tap Bolt with Jam Nut (Bearing Frame Foot Adjustment) 370-H 2 Hex Head Tap Bolt or Stud (Stuffing Box Cover to Frame or Frame Adapter) 412 1 "0"-Ring (Bear'g Hous`g) 428 1 Impeller Gasket 428-A 1 "0"-Rmg (Impeller) 428-B 1 MQ"-Ring (Shaft Bushing) 469-A 2 Precision Aligner (Frame Adapter to Casing) 469-B 2 Precision Aligner (Bearing Frame to Frame Adapter) 469 -D 1 Roll Pm (Shaft Sleeve) STANDARD MATERIALS OF CONSTRUCTION INTERCHANGEABILITY All All All All All All All All Ductile Bronze 316 GA-20 ISO-B ISO-C Monel Nickel Iron S.S. 3197 3196 SFR MFR LFR Glass Filled Teflon Blue African Asbestos [ Teflon 316 | GA-201 ISd-BTlSO-C | Monel | Nickel T T T SM L sML sML 1000 T s M L Steel T s M L' Steel S 2237 | *316 Ti-20 T Hast-B|Hast-C| Monel | Nickel 2238 | 316 T T sML sML Glass Reinforced Nylon T sML 4201 1 316 I C-20 | Hast-Bffiast-Cl Monel | Nickel T s M L Steel Steel -s T sML Blue African Asbestos T sML 1000 T s M L -| 316 T s Glass & Steel Ts 316 | C-20 j Hast-B|Hast-C|Monel [Nickel S iNotReq'd Buna Rubber TS Buna Rubber T S| M |L 316 Monel Ts 304 Monel Ts ' Vellumoid Steel s T sML Steel T sML Steel 304* Ts Steel Steel Steel <T) s S N1 SM Steel Steel s 0.) s Steel s Steel Buna Rubber Teflon Teflon Teflon Steel Steel 420 Ts T S| M|L T- --s -- S | Not Req'd s _s s o Optional sae 4140 on Modal 313; ^ Material shown, butt welded to carbon steel and machined as a single piece. PUMP END PARTS-NUMBERS ON SECTIONAL END SHOWN IN BLUE CODE 304 316 316 420 GA-20 C 20 1000 1012 1013 1103 MATERIAL AND SPECIFICATIONS WfOiifbl Stainless AISI type 304 Cast Stainless ACI-CF-8M Wrought Stainless AISI type 316 Wrought Stainless AISI type 420 Cast Goulds-A-Loy 20 ACi CN-7MCU Wrought Carpenter 20 Cast Iron ASTM MilL Ductile Iron. Meet Treated A$TM A395 56T Type fiQ-4M5 Ductile Iren Ai Cast ASTM AJ38 &5 Type 80 60 03 Anti-Ana Bronze 223?: 2238 ISO-B Hast-fi Lso C Molybdenum Alloy Stfl SAE41S6 Steel SAE 4140 Hot Rolled Double Heat Treated Cast ISO B ASTM B332 58T Wrought Hastefloy B ASTM B335-56T Cast ISO'C ASTM B332-58T " Hilt'C Mortal Monti Nickel Nickel Wrought Hastefloy C ASTM B336-UT Cast (Goulds 1119) Wrought Cast (Goulds 1601) Wrought tFlame hardened to SOQ Brinnell through Stuffing Box. No. Item Req'd No. Per Pump Part Name 100 1 Casing 101 1 Impeller STANDARD MATERIALS OF CONSTRUCTION All All Ductile All 316 All All All All All Iron Bronze s.$+ GA-20 ISO-B ISO-C Monel Nickel 1012 1103 316 GA-20 ISO-B ISO-C Monel Nickel 1013 1103 316 GA-20 ISO-B ISO-C Monel Nickel INTERCHANGEABILITY BY CASING CLASS Mooel 3197 Model 3196 7 7 7re 7[ 40 1 CO tSX1| CD fO1 40 1 cXsi eo 1 00 mx1 2 oo CCXMO1 1 1 nX O CO o CCXOsl o C3 4X0 <T) 7 nK re 7 Csl re 7rXeX- 74X0 108 1 Frame Adapter 131 1 Casing Foot 1000 1000 Cv 6 6 184 1 Stuffing Box Cover, Standard, Model 3197 Stuffing Box Cover, 184 1 Standard, Power End Stuffing Box Cover, 184 1 Standard, "M" Power End Stuffing Box Cover, 184 1 Standard, "L" Power End o Stuffing Box Cover, Water 184-A 1 Jacketed, Model 3197 1012 1012 1012 1012 1012 1103 1103 1103 1103 1103 316 GA-20 ISO-B ISO-C Monel Nickel 316 GA-20 ISO-B ISO-C Monet Nickel 1 _ 316 GA-20 ISO-B ISO-C Monel Nickel 316 GA-20 ISO-B ISO-C Monel Nickel 316 GA-20 ISO-B ISO-C Monel Nickel T-A _ 6S 6M 6L O Stuffing Box Cover, Water 184-A 1 o Jacketed, "S" Power End Stuffing Box Cover, Water 1012 1103 316 GA-20 ISO-B ISO-C Monel Nickel 6S-A 184-A 1 Jacketed, aiMM Power End 1012 1103 316 GA-20 ISO-B tso-c Monel Nickel 6M-A O Stuffing Box Cover, Water 184-A 1 Jacketed, "L" Power End 1012 1103 316 GA-20 ISO-B ISO-C Monel Nickel i -- 6L-A 241 1 Bearing Frame Foot 1000 J 351 1 Gasket (Casing) Vie'Thick Blue African Asbestos >6 6 360-B 1 Gasket (Frame Adapter to Stuffing Box Cover) .006' Thick Manila Paper Not Req'd 6 Frame Adapter and Frame Foot are Integral with Frame on Model 3197. Casing Foot is Integral with Casing on Model 3197. Casing Foot is Integral with casing on 4x6-13. CCR 8 81 8S 8M 8L 8S-A 8M-A 8L-A 8 8 8 10 13 10 111 13 Al 13 | _ 10S _ 10M 13M 10L 13L _ 10S-A _ 10M-A I3M-A 10L-A 10 13L-A 13 13 10 13 OUUUUO 9 MODEL STD CONSTRUCTION DETAILS 4x6-10 2x3-13 4x6--13 PUMP END Minimum Casing Thickness Casing Corrosion Allowance Maximum Diameter Solids Impeller Eye Area Working Pressure Test Pressure Maximum Liquid Temp. (Without Cooling) Maximum Liquid Temp. (With Cooling) Unit Weights Model 3197 Model 3196 T 1X1 TcXn i< TXcm IX TCXO cm TCXM 1X 2 ICXM CTXO as T S o 7CSXO 0r--t XCXM O1c--o511 C O< 4 #--* W %" Vie" H" Me" V2" M" 5/i6" w w y%" %"l Ml Me" | w | i`/s"|u/i6"| ihi \ Vs" I Vs" I r | See Individual Performance Curves, Pages 12-16 150 PSIG See Pressure-Temperature Chart Below 150% Of Maximum Working Pressure at 100F. 350F 450F See Dimension Print, Pages 19 and 20 50OF CO 7COa l%" y% y%" 1 h' 11" POWER END SHAFT DIAMETERS BEARINGS STUFFING BOX At Impeller In Stuffing Box (Less Sleeve) In Stuffing Box (With Sleeve) Sleeve Outside Diameter Between Bearings At Coupling Radial Coupling End (Single Row) (Double Row) Bearing Span (Single Row) (Double Row) Shaft Overhang Bore Depth Packing Size No. of Rings Width of Lantern Ring Distance--End of Box to Nearest Obstruction Model 3197 Vi" 1W" W 1W" 1M" r 206-S 305-S 5305 4%" 4M" 5M" PA" l13/is" Vie" x M" 7/is" 2M" S s/8" 1M" 1" 1M" 154" 307-S 307-S 5307 7Vis" 7Vie" 8M" 2" 213/is" Model 3196 M 1" 1M" 1M" 1M" 2M" 1M" 309-S 309-S 5309 7" 6M" 8 k' 2M" 2W M"xM" 5 y," 3 L 2!4" l7/s" 2!4" 2M" 311-S 311-S 5311 6`Vie" 6Vie" VA" MODEL STD PRESSURE TEMPERATURE DATA -300 -200 --100 0 100 200 300 400 S00 TEMPERATURE-- *F E-2092 400 - 300 -200 -100 0 TEMPERATURE- 100 200 300 400 500 E-2091-1 CODE FOR PRESSURE TEMPERATURE CHARTS CODE A CODE B CODE D CODE M CODE N 316 (ASTM A296-60 CF-8M) BRONZE (GOULDS 1103) DUCTILE IRON MONEL (GOULDS 1119) NICKEL (GOULDS 1601) GA-20 (ACI CN7MCU) (ASTM A395-56T) ISO-B (ASTM B 332-58T) 10 ISO-C (ASTM B 332-58T) CCR 000008015 COMPOSITE RATING CHARTS For detailed hydraulic performance see individual performance curves. TOTAL DYNAMIC HEAD IN FEET 1750 RPM PERFORMANCE GALLONS PER MINUTE CCR 000008016 11 HYDRAULIC COVERAGE Following are individual performance curves for all sizes of GOULDS STD LINE Curves are color coded by speed according to the index below. 3500 RPM I 750 RPM II 50 RPM ERFORMANCE CURVES MODEL 3197 40 50 CAWnr-GPH lxlVi-6 CAPACITY-- 12 Mx 3-6 CAPACITY--$NI *.1676 CCR 000008017 PERFORMANCE CURVES MODEL 3196 11/2X3-6 OS 1572 ' 2 CCR 000008018 13 PERFORMANCE CURVES MODEL 3196 80 100 ttfAOTY-- 140 160 ant 1795 160 200 CAPA0TY-6FM 14 CCR 000008019 PERFORMANCE CURVES MODEL 3196 IVz X3-13 CCR 000008020 15 PERFORMANCE CURVES MODEL 3196 4x6-10 200 800 OOO 1400 1600 CAPACITY --GPM Ort 1602 800 1000 CAPACITY --_6P6 1400 1600 OK |7$6 4x6-13 CCR 000008021 BEARING FRAME SELECTION CHART A-FRAME SELECTION CHART--MODEL 3196 S----------*-[4--------M-------k-|^-- L ---| SHAFT DEFLECTION CHART B-SHAFT DEFLECTION AT SEAL FACES AT SHUT-OFF--MODEL 3196 To select minimum bearing frame size: 1. Enter Chart A above for pump size required. 2. Read horizontally to intersection of operating RPM line. Scale at bottom of chart gives Frame Load Factor. 3. To correct load factor for liquid handled, multiply by specific gravity. 4. Then to correct load factor for actual impeller diameter being used, multiply by ratio of impeller diameter required to maximum diam eter available. 5. Enter Table A with corrected load value to determine frame size. Table A Frame S M L Max. Allow. Load 5.3M 19M 40M 6. A further limitation on frame size is B.H.P. for various R.P.M. shown in table at right. Enter chart with frame load factor determined as at left. Reading to pump shaft used will give shaft deflec tion at mechanical seal face at shut-off. , The limit of .002" is recommended as the maximum shaft deflection for good design practice. B, H. P. LIMITS TABLE Table below shows maximum allowable Brake Horsepower per frame size and R.P.M. RPM 3500 2900 1750 1450 1150 Frame S 24 20 12 10 8 M 120 100 60 50 40 L 120 100 60 50 40 860 6 30 30 MATERIAL SPECIFICATIONS AND TYPICAL COMPOSITION CODE 304 3)6 316 420 GA-20 C-20 1000 1012 MATERIAL AND SPECIFICATIONS Wrought Stainless AlSlIype 304 Cast Stainless ACI-CF-8M Wrought Stainless AISI type 316 Wrought Stainless AlSlIype 420 Cast Goulds-A-Loy 20 ACI CN-7MCU Wrought Carpenter 20 Cast Iron ASTM A48-56 Ductile Iron, Heat Treated ASTM A395-56T Type 60-45-15 Fe Bal Bal Bal Bal Bal Bal Bal Bal Cr 18-20 18-21 16-18 12-14 20 20 -- - CHEMICAL COMPOSITION PER CENT Nl 8-12 9-12 10-14 _ 29 29 -- c 0.08 Max 008 Max. 008 Max, Over 015 "0 07 Max 0 07 Max, 3.4 Mo - 2.03.0 2.02.0 _ 1 75 Mm 200 Mm, -- Cu _ _ _ _ 300 Mm 300 Mm. -- Si 100 Max 150 Max 100 Max. 1.00 Max 105" Max 100 Max. 2,2 Mn 2.00 Max 1 50 Max 200 Max. 1.00 Max 150 0,75 0.5 P Max. 0.04 0,04 004 004 0 04 03 s Max. 0.03 0 64 0 03 0.Q3 004 _ 0.15 10 38 - - 2 75 04 0 08 - 1013 1103 Iren At citt ASTM AUS 55 Type I0-M.03 Anti-Acid Bronze Bal - 1.0 38 - - 2,75 04 0 08 - 0 5-1.0 -- --86-88 """ 22371 Molybdenum Alloy Sttel SAE 4150 Bal 81.10 - .45- .15- 55 25 .6-9 0.04 0.05 2238 Steel SAE 4140 Hot Rolled Double Heat Treated Bal .801 10 35- - - 0 60- 0 04 0 05 .45 .25 0 90 ISO-8 Hist-B IS0-C Cast 150-B ASTM B332-58T Wrought Hastelloy B ASTM B335-56T Cast ISO-C ASTM B332-58T 4-6 1 0 Max Bal 0 12 26-30 Max 10 Max 10 Max 0.04 0.03 4-6 10 Bal 0.05 25-30 " ~T5~ 1 0 0'OZ5" 0 03 Max, Max.' Max. Max. 4 5-15 ' 155-17 5 Bal 0.12 16-18 Max 1.0 Max 10 Max 004 0.03 Hist-C Wrought Hastelloy C ASTM 8336-58T 4-7 14 5-16.5 Bal Monel Monel Cast (Goulds 1119) Wrought 20 -- 62 1.4 -- -------jj-- Nickel Cast (Goulds 1601} 1.25 Max - 97 Nickel Wrought 015 - 955 {Flams hardened to 500 Brinnflll through Stuffing Box 008 Max 02 Old 006 15-17 10 Max -- -- 10 Max - '"515" 30 - 0 05 15 01 2.0 Max 0 05 10 Max. 08 1.0 15 Max .25 004 -t -- ~ - 0 03 -- 0Q1 - Other _ _ _ _ _ _ -- Mg 006 Sn 5.5-6 5 Pb 3,5-5.5 2n 1 0-2 5 - - Co 2.5 Max V0 2-0 4 Co 2 5 Max V 0 2-0 4 Co 2.5 Max. W 3 75-5 25 V 0,2-0,4 to 2 5 Max W 3-4 5 V 0 35 Max Cb 1 4 -- " - Tmmparatura of liquid in pump stuffing ton for various pumping tampsraturas CCR 000008022 17 W E-2070 BEARING LIFE INFORMATION THRUST BEARING The charts below show minimum thrust bearing 4 a SUCTION PRE55URI-PSIS SUCTION PRESSURE--PSIC RADIAL BEARINGS The inboard, or radial bearing is subject to radial load only. The two charts below show the minimum radial bearing life with the pump operating at zero flow and at rotative speeds indicated. To find radial bearing life, proceed as follows: 1. Determine load factor "W" from chart "A" and steps 1 thru 4 on page 17. 2. Enter applicable chart below using load factor "W." 3. Read vertically up to the intersection with the required frame size. 4. Read horizontally to left to find the minimum radial bearing life in years. 1750 R.P.M CO CoD <N S SN X 2 Z S22ZZ 5? 8S 2 S3 2 BEARING LIFE CALCULATIONS The design of the unit is such that under maximum load condi tions, the calculated minimum bearing life will be not less than two years. Under average or minimum loads, the calculated minimum life of the bearings will be considerably greater. Bearing manufacturers present data in the form of charts giving rated capacity in pounds at various RPM. This data makes it possible to calculate statistically the expected mini mum life of the bearing. Minimum life is the service that 90% of a given size bearing will exceed for a given load condition. The life of 50% of the bearings will be five times the minimum life. The minimum life of the bearing is calculated from: `Minimum life in years = .057 (rate^ capacity V V actual load / For example, the maximum allowable load on the M frame radial bearing is 420 pounds. The radial bearing is a 309-S with a rated capacity of 1925 pounds at 3500 RPM. The minimum life is: M - .057 = 5.5 years However, the load on the M frame radial bearing could go as low as 126 pounds and the minimum life would then be: M = .057 = 200 years *As defined by AFBMA 18 CCR 000008023 BED- MOTOR SLATE FRAME HA NO H8 HD * 6", 8" 8 10" n" a 13" PUMPS t PUMPS 4 HE HF APPROX WEIGHT Hr HG HH C OF BEDPLATE, mx CPLG.CPLG6UARD AND MOTOR 143 T 12 45 4 i '4 4 155 143 T 12 45 1 B7 12 45 1 182 T 184 T 12 45 213 213 T 12 45 215 2l5T 12 45 Z34U ?54T 1$ 52 12 4 44 4 4 3A J4 4 44 4 4 44 4 4 f4 4 44 6 *1 4 .4 4 1 4 e 5 '4 4 i '4 4 i '4 A 4 165 175 190 240 2 55 390 256 U 15 52 256 T 284U 15 52 284T 2 284 TS 15 52 286 U 286 T IS 52 286 TS 15 52 121 6 4 4 B 4 4 4 30 6 49! 4 4 27 545 "s 6 49 i *i 14 4 545 46 44 46 49i 4 29 "T 4 555 555 3*4 U~ 324 T 18 32TST 324TS 18 326 U 326 T 18 58 58 58 13 4 >4 4 4 'I 1 yJ 145 4 s4 'I '* 700 700 803 3 326 S 18 326 TS 58 4 41 805 36 4 U 36 4 T 18 56 4 55^ 4 1 h| 940 J64US 364TS 565US 365TS IB 18 58 58 14 4.45 41 31 =44 4 i 32 940 995 404 US 404TS 18 60 4 40SUS 18 405 TS 60 444US 444TS 18 60 15 6 i ALSO INCLUDES 4X6*10 57| i 1 94 ^ 1220 415 54li 4, ssj 1350 16 7 5T2 *! 1 38g 1535 + DOES NOT INCLUDE 4X6*10 SUGGESTED FOUNDATION BED FLtfTE NO. eu \ t 2 `3 5 4 SUGGCSTCO FOUNATION BOLTING pips sleeve for kopi. i* I ^ PIPE SLEEVE FOR aCOPL I 2 ? 'in' connections directly opposite 2 `out connections Directly opposi plug two not used AH dimensions in inches. Not to be used for construction. DIMENSIONS GOULDS MODEL 3196-STD aSX3-6 4X6-10 Only \ *\ ivue f L ANGE OlVENSlOlS 1D 0D SC THK NO OF $*? OF HOLES HOLES l *4 9 IS 4 5 s l? s rs 2 64j l i 'i $ IS } 4 13 ? <6 3 4 *6 '! T B Q|41 1} 2 - HOLES * MAY BE EXCEEDED BY BUT never less than DIMENSION SHOWN ALLOWANCE SHOULD BE MADE FOR GROUTING AND BOLT LENGTH 300 LB FLANGE DIMENSION F F 1D 00 BC thk NO OF SIZE CF HOLES HOLES 1 4 3? 4 a 4 44 4 24 4 i i 3 Bi 'g *4 10 'a '4 4G ',1 e 8 12 7 a 1 8t i a suction flange on 3 xx e nas 0 ^ - igNC TAPS O suction flanGE ON 4x6 o A 4x6 i3 MAS 12 I - ONC TAPS PIPE CTAASPINLGOCATION BAAVPRAPERRIOORUXJSMPWFHUf.GSAIHNMTGti CNOP DSlSl?CFH SSUlZCFT CLCAASSS 0 1126 j X 7 N | 0, P( 0, R , S( V, W, s 'a *2 'i 4 1 1 4 3i 4 ? 154 ML 168 162 2 12 3 6 32 3 6 *1 4 1 ^0 2 B j- 1 F Z 1 2 4 'i 1 4 160 174 188 1 ft 4 1 j H *5 164 i78 192 41 28 5 6 12i_ 3 8 8 7 3 4 80 -- .'1 4 s7 9? '8 1. i5 4 1 ?87 2 4 'i 11 83 4 4 4 4 1 4 a2 2S 11412 1 21 4 4 4 3I 5g 5i I7G 183 186 206 I4C5 204 IU7 2i 1 ?00 2i4 220 234 e34 e H 'i 4 4 4 2i s 3I 206 220 234 2 15 16 12? 17 10 10 10 sf I$ 'I 4 4 1 1n 45 4 ' 'i 1 a_ 4i .1 "k 4 4 203 216 21 r 23i 230 244 'I i 4 1 f 4 l 24 11 4 4 250 264 278 4 <2 13 '2? 14 3 4 6 3 3 4 6 10 13 13 13 10 2i l3i 24 i 1"31 ,54 . s8 - 2i H1 2i <i 7i 7 4 1J '? l2i * 'i 75 2i 4 1 ? 4i 8 g 'i si 1 J 4 s7 13 35 'H 4 6j 4 4 3J 305 3i9 246 260 276 290 330 344 405 419 NOTE CASING SUPPLIED without pipe taps tapped hole nos IS. 2D . 2HL A X CAN 0E FuRHiSmEO WHEN REQUWEO A I - PTAP EXCEPT FOR SIZES 1X2-6 a I X2 . WHICH HAVE 1 P TAP # I - P TAP E XCgPT SIZES SxA-S 6 3X4-13 ARE 1 - P TAP 4 X6-IO a 4x6-0 HAVE NO TAP . PTAP . WHEN THIS HOLE FURNISHED IT IS DRILLED 8 TAPPED TO ACCOMMODATE SPECIAL GASKETED PIPE IX-UG SIZE 3X4-I3 - 300* FLANCES N, i 1^ AND 0, , 3V4 NO NO OF Taps i2 n2 PIPE TAP 3 3 i m1 IE 4 3E 2 ml !, 1 2 l 4 A in . w1 n2 21 + i 3 6 PURPOSE CORRECTION IN STUFFING BOX COVER FOR LANTERN RING OR MECH, SEAL FLUSHING - ALWAYS FURNISHED CONNECTIONS FOR COOLING W,C ST BOX CCV ONLY frame adapter Drain - always furnished FRAME COOLING - ALWAYS FURNISHED QUENCH CONNECTION - PACKED STUFFING BOX GLANO DISCHARGE NO^LE GAUGE CONNECTION - s^jp,ED SUCTION NOZZLE GAUGE CONNECTION - SF*EClV?ED CASING DRAIN - WHEN SPECIFIED IN 6 OUT CONl'tCTION FOR fctCHAMCAL SEAL QUENCH GLAND - WHEN SPECIFIED CONNECTION FOR STUFFING BOX CIRCULATING LINE WHEN SPECIFIED, PIPE TAP LOCATION Stuff wo $0X COYER GLAND PACKED BOX FRAME STD STD WC w,c OR 180* 100* *80* ShaXT 5CRIE5 WC APART APART APART D, A B( c, E, F. H, J, K, hCWlZ S 2|*0 t t5` 15* 3i 1i 5 44 4 M 2|rad HORlZ t 20' 20* 3i 1a 4 9S 13 3j HORlZ 2I"" <1 20* 20* 3i 1 4 10 13 i 3i MECM seal OjCNChGlMC L, T, u, 3i i 2i 3! 4 | 2i 3i 4I 4 STUFFING BCH COVER CCR 000008024- DIMENSIONS 60ULD5 MODEL 3197-STD All dimensions in inches. Not to be used for construction ,12-4i ORRfPEMETCAHP-LSAON`TERN RING 'Z-4l PCIPOEOLTINAGP TIOSRO*APART water cooled stuffing box DtME sz FRM <E0 y ut TOR MOTOR FRAME HA HB to HE HP HG C SIZE M "(I APWOXWCTOF BEDPLATE, CPL5 CPLOGROBMTR (29 I43T I45T 10 HE 1*4 90 4 13 iji 9 (4i is A 130 130 (35 145 IB4T 1lb 12 39 8i T *1 >99 IT* 220 *2 aL 235 DIMENSIONS DETERMINED BY FUMR oisch 9JCT CASING SIZE SIZE CLASS *1 P, o. "i 3, V, W| x----------- 1 ,i 7 `5 9 <i 'i 3i '1 3I 60 A6 '1 2 '1 .i 4 '6 12 38 70 * MSAHNAODYWBFNEOUEANXLDCLAEOTEWIODANENDCBOEBLYTFO3LR/EtNfVBGAUTRTHIAWNICLLEN9E0WX0BEBLEESMSATDHEAINN (OMREON/TING OP1 lONAL CASINO TAPS NO SIZE PURPOSE 4l DISCGHAGAERGE 711 4i "SB?" snr i s4 4 05CY'D0APR<SAAI*$NIN$G+TD ISO LB FLANGE DIMENSIONS (ASA $TC EXCEPT FLAT FACET1) 1D o o, BC THK NO OF HOLES 4i 16 SIZE OF HOLES i ,1 4 '2 3 72 6 ii 16 i5 ii 4 4 i 8 3 4 249*34 GOULDS COMPLETE LINE OF STANDARDIZED PROCESS PUMPS Back Pull Out Design -- Interchangeable Pump Dimensions See Bulletin 725.1 XL for model 3196XL coverage GOULDS (, PUMPS Goulds Pumps, Inc., Main Plant and Headquarters in Seneca Falls, N.Y. 13148 BRANCH SALES OFFICES:ATLANTA-1760 Tally Circle, N. E,, Atlanta, Georgia 30329, BATON ROUGE-8520 Airway Drive,, Baton Rouge, Louisiana 70806, BOSTON--1330 Beacon St, Brookline, Massachusetts 02146, BUFFALO--5554 Main St, Buffalo, New York 14221, CHARLESTON --1018 Kanawha Blvd E., Charleston, West Virginia 25301. CHICAGO--2439 Crescent Dr., Broadview. Illinois 60153. CLEVELAND--5061 West 161st Street, Cleveland, Ohio 44142, DENVER--2186 S, Holly St., Denver, Colorado 80222, DETROIT--15660 W. Ten Mile Rd.. Southfield, Michigan 48075. HOUSTON--5828 Star Lane. Houston. Texas 77027, LOS ANGELES--3951 Capitol Ave., City of Industry, Calif 91747. MONROE--205 S. Stanley St., Monroe, Louisiana 71201. NEWYORK--341 Broad St., Clifton, N. J, 07013, PHILADELPHIA--354 Lancaster Ave , Haverford. Pennsylvania 19041, PITTSBURGH--223 Fourth Ave,, Pittsburgh, Pennsylvania 15222, RICHMOND--5928 Nine Mile Rd,, Richmond, Virginia 23223, ST. LOUIS--1401 S. Brentwood Blvd,, St. Louis, Missouri 63144, SAN FRANCISCO--1043 Stuart St,, LaFayette, California 94549, TULSA--4580 East 50h St., Tulsa, Oklahoma 74135, PACIFIC NORTHWEST--Goulds Pumps Western, Inc., 1919 N W. Thurman St,, Portland, Oregon 97209, CANADA--Beloit Goulds Division. Beloit Sorel Ltd., Quebec. Canada. INTERNATIONAL SALES--Export Dept., Seneca Falls, New York 13148. CCR 000008025 FORM 0466-EL SUP. 7990-EL lOM FLF PRINTED IN U.S.A. GOULDS MODEL 3S55-3755 PEffORHflKCE CURVES 60 Cycle Speeds CUSTOMER................................................................................................ ITEM. . . . . . SERVICE. . . . . . GPM. . . . . . HEAD...... EFFICIENCY. . . . . . RPM. . . . . . 710.1C6 August 26, 1968 (Sup. 710.1C6 of 5/14/68 3500 R.P.I5I. ( \ gzoeo GOULDS PUMPS INC. Seneca Falls, New York, U.S.A. Sjll or a*at&ials /W-fZ-CiT. / 1 C/vi/e> ? / C*S- rtsGl? 5^rf-C77>^ -ssister) / Ex o rsS& 3 4 / tfCc F**S: 8'A/A 4 Be. A? 07-s9Tf / dob/c.^:. . 04r*At*s*: s*dA s*/*X- W* *oc^r " - " / / ? %/?. 3 ^ 3 4**o*- 8 /1 s'/>/, 3 is 3 &^aoy--________ 9 k A? t st't/ef j ac*tv>x ikOoZPrt 4S>&/3/,o 7^.' 2v5d / .,,**,> /'/z */jp-x *>,*<? r*. /? / C<y/>J-ffAr& &exr &pj**? /%. */ ? -xs*, /vr 72^ /3 / A//?So+4 u,j*A2./4-r/o'U sc^tretf '7Aajst\ c A________________ J4- DWN JOB /-? t_y i v"?9 PO `703, DATE ,12,.I2. ft_______ 4. CCR 000008027 'yy88 /r see e?' D. model z&s^ 9;?s & <!!$!> FOR ('C&SV TSSS^JV.n*_____^____i^k.____________ DWG CON-RAD division ot US INDUSTRIES, INC. I  ty\-rp -= (212-^5") _V^\ j=c*- 2^.... _____ toft. 2^ 5Zv^ 1.2. Co -^,_=_LQa. 1*^ ! PVasovu^fr 2^ Te^iy v\^.e < vo F\-r-e~To_ ___ 0 - \ 0C> Aretb = -7,000,000 (\ o o) c 1 o 20 _ ,,,Aft ----- ` . ` , ... i;;.' ... . . ' . / ( ' ', ' l ' Co^C ?+ ^ (CCR 000008028 "SpSC\P l PTT\OTv)S Pag e----------------- of------------------- ---------------------------------------------------------------------------------------- '.-------- --------------- :-----------------------. State 72 OO w AtH sre^Mf /D " s-hennt-'' (EtoeSi.^ z*k - <2_*aj Cep/9i* *"& -- 6s 50 temperature: rise o r water r % The above chart shows five quantities: R "`Temperature Rise (Water outlet temperature minus water inlet temp.) in *F. C* Quantities of water heated in Gallons per hour. Line "C" shows ' also the required size of the water pipe line. S* Quantity of steam in pounds per hour. Line "S'* also gives the , ' proper size of the condensate offtake pipe .,V"S~team pii;pe size and regulator valve size in inches diameter. Size of regulaaitor valve should be always smaller than the proper size of the steam pipe as shown on th'iis iiine. P" Steam gage pressure in pounds per square inch. Line "P" shows also the corresponding temperature for saturated steam. 000008033 ' To find the proper pipe and regulator sizes and the required amount of steam for a known quantity of water being heated through a desired temperature rise, proceed as follows: Connect with a straight edge lines "R" and ^S" intersecting "R" at the desired temperature range and "C" at the known quantity of water being heated; read pn "C" the required water-pipe size and on "S' the steam consumption and required -^^coconndensate pipe size; connect lines "S" and "P" with a straight edge intersecting "S" at the found quantity of steam and "P" \td)e known steam gage pressure or its corresponding temperature, read on line "V" the required steam pipe and regulator ^^vahve size. The example indicated by the dotted line shows that 5,000 Gallons of,water heated from 40 to 180 Degrees F., with steam *t5# Gage pressure require 6,000# of steam per hour, that the steam pipit should be 8", the regulator valve 6", the condensate piping 2" and the water inlet and outlet piping V'. o, pj =#= S Made by_____ m3 Checked by.. ~ Date------------ Page of. TITLE CONTINENTAL OIL COMPANY CALCULATION SHEET Job No. Field-- State * I\ r .. -__<4sl, ^: s. 13 10 * : . ... .3 , .38 ii\.:\s _ *; "TCU^ . 1.^ -JL 3>% 31 .47 : &4 lo:Q i '60pL_ . A.P " 31.3 VjPsM OuOoJ^cA^x. .*7 - 4- i Date_____ Pace .TITLE. . FIELD- .State____ Mr. Goorpo Fumoaon ftocomont Dtrottor Lowltlono Stoto Untlvworafty Coitopo of Enptijportng' > I Sk, Tho otBlwd pro|oct ontltipd lew Mkw Condonanlo Syotom" hoi boon sueeouMty compMod by Mr. Joho C* Uwii, Jr, during ht onploymont of Hio VCM Plant of Contlnontol OH Cowpony. Tho projoct ho# boon rovtow- od by Ibo plod DMOpnont and U now oppwwl for eonrtgiettaa. ft b oxpoetod that work on this pro|o#w(il dart In Mo Qetobar and, hopofidly, will bo aamptofcod by Mia and of TWf >> Wo oansldor tho roport to bo a goad/comploto otwdy and Mpn projoct and rocammond that It bo occoptod a proof of camplofton of Cbrli* Englnoorinp Proettco Nwabor 149 eoarao. f l Vary Indy yad|' JDM-MC * oci Mr. t. H. Gorloob Attachment John D. Mtnatt Sr. hacow Englnoor Cowtlnontol VCM float CCR 000008038 ) Cy?sv&x iroc, "Pe^^^-oTie7 s /H - a,tst p*J- W '*! Ltxo'PResso^e Comocm^at Swabia 1 _] ,,w=. z 01 --* S lbs ./ If. Aa) - t s,< \ b' b/' bee <s 10. as 7,2 1^ B+ J /_ Ir Cb LO JLf rn ON _o f J-l at lit) -- "1 w i< >7,,W U Li 07 iV-0 2. 2.2 `SC ) ** Co. ie> lb &/ lb s*/ Sib-- --- -- ' V X.V Ml L_J PR UC `AC >KS -< LV f") ! Sr m f. , t u? ;o., LY jfc. w ).0' 2 ^ ' >2JL jj LJ >8. % 2" 3 * - ),3 83, ?7P> - \\ JO, 221 P) ie 3.0 7 i # .<5 10 ,3 3. "7 ^17 ) , _2 ftj =>1 u ** 1 2.0 >5' > Q 0. 0\ o.l a -- v< >LO Hie - f > P <D< 3 * r=r TO rM 21 e" 20 J n 51 LV P ' ft o 01 =l!Ul :pj -FT CIOM_OF _3 ew uo J3! ._U CM Be M JO. _J -ftl T_i OKI T.P LCl oR > niA j .. 3-S .oN --7- R, > ; rXr> X>t LO s,) IX- . iL * Pip E " Pif rrsR 4- ii R( .\_ . U 2ri > X- < 10 1-; J7 4 V ,0 $4 ft rJ fri 73J>, IX > s i < 0. i )0< w // J X 10^ *1 . \c . 0 0*5 0 V. n <n 7 ). c[O' - 1, ''V , ---- -----( LLK UUUUUOU<ti -- ,-4. A J. .1__L.. 1.. 1. -_L .1 J MADE BY- 3^- Checked by_________ i Date_____ .________________ Page --!-------- or--3L ^ CONTINENTAL OIL COMPANY Job No- '" CALCULATION SHEET $ TtOOPrtfVbe TUOtO -- METHOD P ,,TlTLE .----'J,--.1 j, CticuoMwm nit> mattih fiV'----------`RePfielp Otr^ ______________"' state. A Lous'PressO'RE C Noewtftre * AJ A)0 Pe \otO VJ 'oOCO 1 b-j /tiR. ____ W t 16% _ lo<500 \b i 0*3 - 11 "o "S I b s /sc <-- :, A P - A, CiOO 003,3(3 4 L Vm7- V 6 2 _ S"93 */^ 3*' 06^ q-^/d9- ____ ! ; . 2 ' 0,0 23- "5 " (3,^3.r .| : VHZ. 31/.^ 211,-B ED OY \ or. TITLE CALCULATION SHEET Field. State LOjaPnesscRE CoNoew&ftre S-wtem 1 -1 ... * -- _ wi = 5.C . u> r z. SO ibt ./ I* tb !/' !>e< w- l l(>% W =, 05 + I 07 2. 13 G?*. 4e 3,0 13 i/.: U -- --- > G> Cf> LCJLfrn ON _ o p_ u QC HD M DUV mi PR kC UC >KJ -< LV / )b &y \b */ ,, ___TmO-Xn____ :1 -- f, c. ---- V * c 4 V *U4 ;o,j LV f Sc ><9 D >.>' '4 -a 4-0 ) 07 3 # - (2 40 J0" T is> SC *,) tei 5.0 7 10 ,3 r * V S 65 % 2 a_.jk v< >LO ME 2. l a i9 . u n t X 0. o\ 61 2 -- TO rM _ - 11 PI 7 -a LV V=;j X -- .... _Ci lOI :o -ft- r_u> T?< : OF C ! .1 i.__. _ PitIe m Pi f jY4 rrt rR 3 i 4n EY 1401 -os lW U*4 EE R M m. *Ri sn 014 jip CT OR .(p < 3-2 .0s ^t .T i; Ik i. , ... 7 .!'< .it 10* - `. ' iX V ** * 74 i . a<| ' 1 >6* i! ' *. ?< `ft k i-- -- . 0 X 1 0 j > t. V`> \0 D.< id ' .t * r* 1 / *' -A \ - --S Made by. Checked by. n " Date_________ PAflE_ I ,____OF_3- 1 -L. ... ^CCR 000008049 CONTINENTAL OIL COMPANY CALCULATION SHEET 46 Job No.. TtOiO -- TActWd OW -- i-' TITLE----- ,, i '------------- .11:, cttwovem wwctih :'fteTi 'Rbpfifln 0m*- wrt 1 State. T Lous Pressore CoNtAewscv-re Svvteh Ft pe. Section.... ^ 1kjS s _.<s ?-=- n .ac >o c i>.T & ns io< IbiV Ak lb i/sBC e* / ilFL *-- W *. w +J TJ l_v ! 3 s' <S> Cft lc.\JLfm ON __Q. F_ _Ll Oii no M X.v Ml PR kC 1C .. c * 4 * il< .0, iM V ).Cf 2 8 Oc <=> A 7 Q )0 - ( ^)47 ,&6 a 1 - t oc 10 .3*> " s' 4 X 2 &J ) idi3.0 7 ss u <9 ~4-* ^ Z ?>4 3 ,, X 0. o\ 67 2. l-- TO rM -c a -- ? 0 0 <&. 6 Co - lb -/ HT lb s/ sec ..... / LV * \ 1. - v< ILO HE 1 2). 2^:|o 2> 1 ^ |2< i a LV p jD r-O 0-3 <2 _C_ RL< LL! -FT no OP j? BY ViO JDS ,_U OH SB BU At JD. _J TU STA OH J^p CT OR f*L 5-S l\ \\ Pi fr = - TL V ."+* i; Ak " Pip g " Plf nrf ;R R< 1 l kTg .... ii 3 r < n A < >, c 0<t 3, e> ) r id S o. 3<y 4 // i .7 I * 10 A 4. c 6i >s 3.1 4 ) .n * 3. < 30 - .. 1 E Made tv. 3^- 3 Checked bv.-._______ ' Date___________________ LPage___ . OF_ ; \ \ t ~Ui V CONTINENTAL OIL COMPANY _> Job No._____ ._____ CALCULATION SHEET $ T06*rtft*e PtOtO -- Piewoo OF CtiOJOWCTU nwb MOPTIH .TITLE ------- --------------- - ' ,. x--------- -... Jlgr. 3tuF..-.-n Cb-r- wc^ State, I.*.l. Iftl.ll.liMlil II. ii. ,`V> , ,V Louo'PResfcORE CoNTscM^ft-re `Svvaem FpE_SecToN- w= .JU) = __(c !=. -- A 50 lb? * / -1* 0. A 7' tbi !*/' *e< iOO E* >/ 4r_ 4 ; >VgL w- U< ga + 1 07 3 -- 1*0 4o 0.- 0 C.P LC JLf m Olsj _0 `AC LV.U qc lit) _v 5LV Ml >__1 -K IlCI -( >K f\ \ iH. 4* fa*? iO^ SA 4 * _L 4 0 0 >.t>" ' " 4: Sic >0. tb &/ He L- -- \b */ >e r % = (r 4c o'] - ( t 4 Oi * ) 10 ).0 7 ` H- 3j IP .3 r 2 6, G X L. 2 SlJ -- jsr u 1 1" r 1 X 0. 0\ &7 ? C TO rM _ = ---- v< )LVl MS G> 1 *2 ---- ---- 1 LV1 <->. G >-4r F Co 4 5, (s>. A C\( t?v ,,c 4L< a>' -ft" ro A _ OP t; EY uo JOt .JkJ DM BE R JD K< = -Xr-- r(i 7 V .-* o-> i) -- k - Pipe' Pi f >wl rtE :R 0. i/ v\ 1 (s~ fix 10 1r * *. e O' 70 3n 1 a Lx ip < * ' ( >- < >0" CAKA""Rl CCA Fp CY OR -fe q-: .o') T?< -- -- r_ i.. .. 3. o4 Xl( I* u > X to 5 <0. oc s 0 ,,Da oc 4' 7 ! made by_ i Checked by. i date............._ Page___ L. A .- TITLE. *_ - CONTINENTAL OIL COMPANY Job Mo. f OCR 000008055 _____ CALCULATION SHEET $4 TvOd^t+h^ftr TLOtO -- HeWOO O* CtitVIOvnEm Apb HAITTIH ... -PleTi H p f , ELp Oe.r_-_rt <5^ ..... * . 1 ,. state .__________ _____ A % ; i ' JP\peDift>AEi[?R 2* a .... ' L 3'1 JL' Vl C6T 3.1 ?0 K -F :i JGi VTF VOLOS >./ o- 13 -- L/t > " XA V-- -- \ &! >8 > " "|r 1*5 ... - a..1 --- -- -- ECoui Hue* rr K LAN stm m) v< A- E iOlC CVA rr te*j GTVt -- L/ 0- --- %t K S 60* /MJl<rr u NG'M -- ---- ---- 7 EC B>CuVb (.<&< p). L/d --. 30 1 . . 1). T eiA1 KOh * Vti - 20 c ,(o <1- ... AP "E^b= a saw HL L/1L> = SO i 53 .7 0 TH ER c i. *: >0 7C .5 > i. ' s lO 2) c3 c>3 0 2 ' - T trr OL TflL + E 3 3 \r ,, C5 6 . S ;o. 7C ,6 3` Uc * ? 3<S y\ * i f t % j E MADE BY.. 3 Checked by date. Page___2...__ of___ 3-------- - TITLE. CONTINENTAL OIL COMPANY CALCULATION SHEET ' < V^.yTJyT'. "7l'. - JOB No.. . FIELD.State . CCR 000008056 CftLC.Ov.^TVON OF ! ^Atf y fcL- K Pipe t>iftaerer > (ptoost^(i -+| 7i)(( TO SI >8) ^-3^ - 5. 22. ? 1-k .-<=)- 3 <oQ75 ,^rjs. prom OvnfH !iI at .5y_ ms u s>s~U.OSr^X i? 5! ) + % (Ci*007^>) (\2 57 ^ J* 3 -5 7 i v2r Br? r (oO 3-fe l-Utl IA- ( MV >y 3AlbOV - Cm,,CULftT\C W O F___ A?* UsKweji-'z Tipg^iftMmH //! Us : 1Lif _. \p" o. 00000^6 W J*.... POO, ooq.o,? 26 . W at x -7 2.26 \to (0, c 07 X3 ^4c_Jj i 2ZJL2 2L2.5xtQ"7 (.cp,C>075)(5ftl 7(| 154-0 V* - ( 211,ft). f2* <-1? t u V- F^wwaL ~*e A?k ^A*1 A^ IS^... HML \4&h - XaCfun vTwAT;iifi \jet< Ci'W &PTP ^.48 dr8f ra-23r J Made ov,,. Checked by____ Date........... ........ Page .33_____ or. .TITLE. 1' ( (, CONTINENTAL OIL COMPANY `CALCULATION SHEET Job no.. , , >: >` .. >' '' in ti ri in .. ............. ...... i i i.H !. i ..................Ajj*w>ni i !! J-- Pi eld_ 1 '-w / ,a * , Ai r t.'..i . State - CCR 000008057 LOgOpRESSORE CoNt>CM%ftTe SVVffcM PiPE SecrioH _ A ; -- w - 2 S'- 50 lb? V rR U) = i 5. c lb =./ oec 0S T ^c ,4" 5 E+ i/.i 4r M W- 1. w >7W -- U +-I 07 ><ua - 2 S` ^2 ~ < 0.7 Z 'Nu.. -- 0 C.R LC.\ JLf IT! ON _o p u Qv. )\X> V >, DL.V 4' Ml L_' =R kC uc >K1 A LV r [J 4- S Z 2Ji iO 0 .0. V V f \fc< i.o- f ^c "7( vz. 41 S fc r , \b S>/ Ab / [ f. * - (T $<s <l 5 ' ( ><? 3 ) tei 5.0 7 10 .3 *> n bS A X 2 &.{ r u l (q(o X .0, o\ &7 2,__ * C TO FM ,, ^ v< >uo MG 1 c t .ft' \ 3: \ * i SI LV F ft) >3 i < o / -- ' _c 4L< koj -FT rio 4^_ OF EX R< > : i: MI JDS lJM LO V i; 1k Pip p "Pif\\S\ ITTf ;R R A fa , V 6 4ix 0 t: a_ At JO. - J- ^ v < xo II 2 r 9 X 1,0 4 . ',0 , c > . - *- , \ 1* ou -XI CX4 Te cx OR -fr r^w. 5-5 .0^ ' *R( rji 0^ Kl ' 6 'i i X 0s i 1 0 0, 3 o. 0 D4 ^4 g made by_ 3^- 3 Checked by--r_______ - Date__________________ Paoe --!_ of_3.. * , CCR 000008058 CONTINENTAL OIL COMPANY Job No.-. CALCULATION SHEET $ T06*t4ft*e TLOoO -- TITLE. ctiEviovitcm bnb HArriH 3etiHmyFiELpJD6iAiftgJft- --- ___ ________l i* i. - > - . --- . . - 'sr .State . Ol* A "Pipe 'Sect o*o ^ .......................... W- I^OS /hr........................... W+ 10% 1440 Ib^/ny ErQOflf i i pJ ^-1,0 , Gewc t,, .j; : AP - O-OOQ ( OOO: . : i .. ___ Ca3Co2> , ^ .................. a<*___: W UV L = 2Z -t+. y - 2 (d 9 A Pr B.G^X'lO0 ( Vn-4-o)^ (z-j)(-z<* <k)r 0.009 ____ _______________ ____ . Y 407-71 ^.................. ........................ (D a. Made by___________ Cm ecked by______ ) Date ------ Pageof. TITLE -1___ I___ L - : --!. CONTINENTAL OIL COMPANY CALCULATION SHEET 1 CCR 000008061 Job No. -- Field. _ .... State________ Uxo Pressore C ndcm^rtc Pipe Section A Js s <S ?F- 15 1C > \\>\ ,.i !>.'*4 lb s>/se< ... 5 B+ i/: 4r -- " i1i W wb%W -- + 1 0/aU3 c/ 7 2' ' " lb &/ Wt , 4 e lb s/ sec 0 Cft LC* JLf iTt ON _ 0 .U qc >\E>rv 3Uv Ml i PR VC >KI A LV J c + * ;o. LV IE< >.fi? - ( 4ft ' 1* V -- ' IV 1 l<5 7J >... 41 <S T \ 6 1 C r> l >.0 7 >110 .3 *> * _2 S>.{ -- * ---- v< two H\e V 7*5) 1 ut ' I X 0. o\ to"7 ? %-- TO rM _ = 2 4-. 331 ; -H LV p Pi , Oi 2 JCj 3JU rj_o b*_ OP __3 e* uo< JDt lM OM se _Ai m _J `RV CT\ DIO Ff i cn OR (P fTltE 5-5 l) L. >- OO \ ij ; -c iN Pip E " Plf rxi;R y 1' 2n ; ?L \ 2 .4; , O' 1 SC > x - * ---- ' 1 r* - ibC ft 0 oc >8 T?< c >.? X o' r >(re ' b. bo 4. \ X b* GO 1 t% * >* .... " cc R ooc100 306 2 Made by.. 3ti Checked by.. Date_______ _ LPage___ .TITLE. CONTINENTAL OIL COMPANY CALCULATION SHEET $ TvOD^rtp-bl'pcOtO -- Mervkro OP CWewovoeth amo mMtih ---------- ----------------- -----------!--r--TlCT! >*jPFIiM n OtY^Wg% ' }' h . STATE. o-23i.n Cowoe LouaPRessoRe CoNoeK^cv-re Swceva APipe Section 'l. i ---- . w= >0 lbs 7 -Iw w- K >v0 -- 4 7, =>C 1 \b&v __u) ,0 & lb */ !>E< , 0$ +j 05/ )03 1 9 - \b a/ ...Q* 8` SS !>8 i.Z. 4lV -- --- -- "' *~r<& Cft LC JLf m OtsJ O p_ -U ac lit) V ?Lv HiS .,' PR kC _ic KJ -< LV f1W ;o. k_V. + JL m0 s >.0' A O' 0 8 S: l j' 8 s * ' to *at i [ C. -- '> V . - ( bv r 00 > l&li.o 7 3: 10 .3 5 - t -- S x 2 tedL twoM f ii - 4i 1 p- a<5 _3; 74 . X J>_. oio7 2. A Co* 3 TOrM_ -a 4-2 3 7 V 7 - LV F 0 O 15 ,,Cj3lUJOj .ft"no R, _OF _5 ev10(0 JOSlMOH we L -o.T LO i\; ;-C \ _Al m _!-M"*HV * OKi Fp CT oR -fc ntw J - 3-2 Q> --_ Pip E " PipIP'*1 TX\ ;R 3 // rJ \...' - S, .BL<1C I- 4 < >.e hk .. TJ V7 10' > v Tqr~ o. bo- 4 ii & > .K*i*'Kk >* ' < O<*t, a Z 5w , X 10 5, 1 3 , fa . * S Made by_ 3t. h Checked by____ ---------- m " DATE____________________ PAOt.._!______ OF--3 ; 4 -il*:,f CCR 000008068 v;i; CONTINENTAL OIL COMPANY Job No... 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