Api spec 11p 1989 scan (american petroleum institute)

Packaged Reciprocating Compressors for Oil and Gas Production Services API SPECIFICATION 11P (SPEC 11P) SECOND EDITION, NOVEMBER 1, 1989 American Petroleum Cnsfibfë 8.220 L Street, Northwest T,&Shington, DC 20005 11’ COPYRIGHT 2002; American Petroleum Institute Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 Issued by AMERICAN PETROLEUM INSTITUTE Production Department FOR INFORMATION CONCERNING TECHNICAL CONTENTS OF THIS PUBLICATION CONTACT THEAPI PRODUCTION DEPARTMENT, 2535 ONE MAIN PLACE, DALLAS, TX 75202 - (214) 748-3841 SEE BACK SIDE FOR INFORMATION CONCERNING HOW TO OBTAIN ADDITIONAL COPIES OF THIS PUBLICATION Users of this publication should become familiar with itsscope and content, including any provisions it may have regarding marking of manufactured products This document is intended to supplement rather than replace individual engineering judgment OFFICIAL PUBLICATION REG US PATENTOFFICE Copyright COPYRIGHT 2002; American Petroleum Institute @ 1989 American Petroleum Institute Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 ~- A P I SPEC*IIP m 0732290 0087352 I m American Petroleum Institute TABLE OF CONTENTS Page Policy Foreword Section 1: General Section 2: Compressor Section 3: Capacity Control 16 Section 4: Prime Mover 18 Section 5: Cooling System 21 Section 6: Pressure Vessels 24 Section 7: Piping and Appurtenances 26 Section 8: Electrical Systems 29 Section 9: Instruments and Controls 30 Section 10: Shutdowns Alarms and Annunciators 32 Section 11: Skids 33 Section 12: Paint and Painting 34 Section 13: Inspection Testing and Preparation for Shipment 35 Section 14: Marking 37 Section 15: Corrosive Gases - H, S and CO, 38 Section 16: Offshore and/or Marine Environment 40 Appendix A: Excerpt from GPSA Engineering DataBook 42 Appendix B: List of Authorized Packagers 44 Appendix C: Use of API Monogram 44 Appendix D: API Packaged Compressor Data Sheets Part 1- Service Conditions 45 Appendix E: API Packaged Compressor, Data Sheets, Part - Packager’s Design 61 Attention Users of This Publication: Portions of this publication have been changed from the previous edition The location of changes has been marked with a bar in the margin In some cases the changes are significant while in other cases the changes reflect minor editorial adjustmerits The bar notationsin the margins are provided as an aidto users to identify those parts of this publication that have been changed from the previous edition.butAPImakes no warranty as to the accuracy of such bar notations Note: This edition supersedes the first edition dated February 1975 It includes changes adopted by special letter ballot dated January5 1988 COPYRIGHT 2002; American Petroleum Institute Reqztesfs for permissio~lto reproduce or translate all or part of the material publishedhereinskoztld De to Director.p y o ~ z c c t ~ oDepaTtnle t 2535 o.l e Place Dallas Tx 75202.390h Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 A P I S P E C s 1 P 87 m 2 00 Spec 11P: Packaged Reciprocating Compressorsfor Oil and Gas Production Services POLICY API PUBLICATIONS NECESSARILY ADDRESS P R O B L E M S O F A GENERAL NATURE WITH RESPECT TO PARTICULAR CIRCUMSTANCES, LOCAL, STATE AND FEDERAL LAWS AND REGULATIONS SHOULD BE REVIEWED APIISNOTUNDERTAKING TO MEETDUTIES OFEMPLOYERS,MANUFACTURERS OR SUPPLIERS TO WARN AND PROPERLY TRAIN AND EQUIPTHEIREMPLOYEES,ANDOTHERSEXPOSED,CONCERNINGHEALTHANDSAFETY RISKS AND PRECAUTIONS, NOR UNDERTAKING THEIR OBLIGATIONS UNDER LOCAL, STATE, OR FEDERAL LAWS NOTHINGCONTAINEDINANYAPIPUBLICATION IS TO BE CONSTRUED AS GRANTING ANY RIGHT, BY IMPLICATION OR OTHERWISE,FOR THEMANUFACTURE,SALE, OR USEOFANY METHOD, APPARATUS, OR PRODUCT COVERED BY LETTERS PATENT NEITHER SHOULD ANY- COPYRIGHT 2002; American Petroleum Institute THINGCONTAINEDINTHEPUBLICATIONBE CONSTRUEDASINSURINGANYONEAGAINST LIABILITYFORINFRINGEMENTOFLETTERS PATENT GENERALLY, API STANDARDS ARE REVIEWED AND REVISED, REAFFIRMED, OR WITHDRAWN AT LEAST EVERY FIVE YEARS SOMETIMES A ONE-TIME EXTENSION OF UP TO TWO YEARS WILL BE ADDEDTO THIS REVIEW CYCLE THIS PUBLICATION WILL NO LONGER BE IN EFFECT ITS PUBLICATIONDATE FIVEYEARSAFTER AS AN OPERATIVE API STANDARD OR, WHERE ANEXTENSIONHASBEENGRANTED,UPON REPUBLICATION STATUS OF T-HE PUBLICATIONCANBEASCERTAINEDFROMTHEAPI AUTHORING DEPARTMENT (TEL.214-748-3841) A CATALOG O F A P I PUBLICATIONSANDMATER I A L SI SP U B L I S H E DA N N U A L L YA N DU P DATEDQUARTERLYBYAPI, 1220 LST., N.W., WASHINGTON, DG 20005 Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 A P I S P E C * l l P 87 Petroleum m 2 00 American m Institute FOREWORD a ThisSpecification is underthejurisdiction of the API Committee on Standardization of Production Equipment b AmericanPetroleumInstitute(API)Specifications are published as aids to the procurement of standardized equipment and materials, as well as instructions to manufacturers of equipment or materials covered by an API Specification These Specifications are not intended to obviate the need for sound engineering, nor to inhibit in any way anyone from purchasingor producing products to otherspecifications c Theformulationandpublication of APISpecifications and the API monogram program is not intended in anyway to inhibit the purchase of productsfrom companies notlicensed to use the API monogram d API Specifications may be used by anyone desiring to so, and diligent effort hasbeen made by the Institute to assure the accuracy and reliability of the data containedtherein However, theInstitutemakes no representation,warrantyorguarantee inconnection with the publication of any API Specification and hereby expressly disclaims any liability or responsibility for loss or damage resulting from their use, for any violation of any federal, state, or municipal regulation with which anAPISpecificationmay conflict, or forthe infringement of any patent resulting from the useof an API Specification Any manufacturerproducingequipmentormaterials represented as conforming with an API Specification is responsible for complying with all the provisions of that Specification The American Petroleum Institute does not represent, warrant or guarantee that such products in fact conform to the applicable API standard or specification e f The purpose of API Standards on Production Equipment is toestablishminimumrequirementsrelating primarily to mechanical considerations This limitation in scope is one of charter as opposed to interest or concern Energy conservation is of concern and has become increasinglyimportant in allaspects of equipment design,application,andoperation.Thus, innovative energy-conservingapproachesshouldbeaggressively pursued by the manufacturer, packager and purchaser during these steps Alternative approaches which may result in improvedenergyutilizationshouldbethoris espeoughly investigatedandbroughtforth.This cially true of new equipment proposals, as the evaluation of purchase optionswill be increasingly based on thetotal lifecosts versus low initial cost Equipment manufacturersandpackagers, in particular,areencouraged to suggest alternatives to those specified when these approaches achieve improved energyeffectiveness and reduced total life costs without sacrifice of safety, quality, or reliability COPYRIGHT 2002; American Petroleum Institute Thisstandard is based upon theaccumulated knowledge and experience of manufacturers, packagers and purchasers of reciprocating compressors The objective of this publication is to provide a purchase specification to facilitate the manufacture and procurement of reciprocating compressor packages for oil and gas production services This standard requires the purchaser to specify certain detailsandfeatures A bullet ( ) in themarginindicatesthat a decision by thepurchaser is required These decisions should be indicated clearly on the data sheets.Although it is recognized thatthepurchaser may desire to modify, delete, or amplify sections of this standard, it is strongly recommended that all modifications, deletions, and amplifications be made by supplementing this standard, rather than by rewriting or by incorporating sectionsthereof intoanother complete standard Suggested revisions are invited and should be submitted to the Chairman, Committee on Standardization of ProductionEquipment,AmericanPetroleumInstitute, Production Department, 2535 OneMainPlace,Dallas TX 75202-3904 g ThisStandardshall become effective on thedate printed on the cover but may be used voluntarily from the dateof distribution h The current editions of the following standards, codes, andspecificationsshall,totheextent specified herein, form a part of this standard The applicability of changès in standards, codes and specifications that occur after the inquiry shall he mutually agreed upon by the purchaser and the packager RELATEDCODESANDSTANDARDSAREAS FOLLOWS: AFBMA: Anti-FrictionBearingManufacturers Association, 1235 Jefferson Davis Highway, Arlington, Virginia 22202 AFBMA STD 11: Load RatingsandFatigueLife for Roller Bearings ANSI: American National Standards Institute,1430Broadway,New York, New York 10018, ANSI B1.l: Unified Screw Threads ANSI B1.20.1: Pipe Threads, General Purpose (Inch) ANSI B16.1: C a s tI r o nP i p eF l a n g e sa n d FlangedFittings,Class 25, 125, 250, and 800 ANSI B16.5: PipeFlangesandFlangedFittings,SteelNickelAlloyand Other Special Alloys Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 A P I SPEC*:LLP A7 m Spec UP: Packaged Reciprocating Compressors 2 00 5 m for Oil and Gas Production Services ANSIB16.42: DuctileIronPipeFlangesand FlangedFittings,Class 160 and 300 ASTM A-216: Carbon-Steel Castings Suitable for Fusion Welding for High-Temperature Service API: AmericanPetroleumInstitute, ProductionDepartment.211 N Ervay, Suite 1700, Dallas,Texas 75201 ASTM A-269: Seamless and Welded Austenitic Stainless Steel Tubing for General Service ASTM A-278: API STD 1B: S p e c i f i c a t i o nf o rO i l - F i e l d V-Belting Gray Iron Castings for PressureContainingPartsforTemperatures UpTo 650 Deg F API RP 14F: Recommended Practice for Design and Installation of Electrical Systems for Offshore Production Platforms ASTM A-307: Carbon Steel Externally Threaded StandardFasteners ASTM A-312: Seamlessand Welded Austenitic Stainless Steel Pipe ASTM A-320: Alloy-Steel BoltingMaterials Low-Temperature Service ASTM A-358: Electric-Fusion-Welded Austenitic Chromium-Nickel Alloy Steel Pipe for High-Temperature Service ASTM A-395: Ferritic Ductile Iron PressureRetaining Castings for Use a t Elevated Temperatures ASTM A-487: SteelCastingsSuitable sure Service ASTM A-503: Ultrasonic Examination of Large Forged Crankshafts ANSI/ASME B31.3: Chemical Plant and Petroleum RefineryPiping, A Section of the ASME Code for Pressure Piping ASTM A-536: Ductile Iron Castings ASTM A-668: Steel Forgings Carbon and Alloy for General Industrial Use ASME SEC II: Boiler and Pressure Vessel Code, Material Specifications ASTM A-703: ASME SECVIII: Boiler and Pressure Vessel Code, Rules for Constructionof Pressure Vessels SteelCastings.GeneralRequirements for Pressure Containing Parts ASTM A-781: Castings,Steeland Alloy, CommonRequirementsforGeneral Industrial Use ASTM E-709: Practice for Magnetic Particle Examination API RP 500B: APT RP 520: ASME: ASME SECIX: Recommended Practice for Classification of Locations for Electrical Installations at Drilling Rigs and Production Facilities on Land and on Marine Fixed andMobile Platforms Recommended Practice for the Design and Installation of PressureRelievingSystems in Refineries Part I - Design and Part II Installation American Society of Mechanical Engineers, 345 E a s t 47th Street, New York, New York10017 Boiler and Pressure Vessel Code, WeldingandBrazing Qualifications for for Pres- ASTM: American Society for Testing and Materials, 1916 Race Street, Philadelphia, Pennsylvania 19103 GPSA: ASTM A-53: MaterialSpecification for Pipe, Steel,BlackandHot-Dipped Zinc-Coated, WeldedandSeamless Gas Processors Suppliers Association, P.O Box 35584, Tulsa, Oklahoma 74153 NACE: National Association of Corrosion Engineers, P.O Box 218340, Houston, Texas77218 ASTM A-106 SeamlessCarbonSteelPipefor High-Temperature Service NACE MR-01-75: ASTM A-192: SeamlessCarbonSteelBoiler Tubes for High-pressure Service Material Requirements - Sulfide Stress Cracking Resistant Metallic Materials for Oil Field Equipment ASTM A-193: Alloy-SteelandStainlessSteel B o l t i n gM a t e r i a l sf o rH i g h Temperature Service NEMA: National Electrical Manufacturers Association,2101L Street N.W Washington, D.C 20210 COPYRIGHT 2002; American Petroleum Institute Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 NEMA MG-1: NFPA: Protection National Fire Motors and Generators Structures Steel SSPC: Painting Association, Batterymarch Park, Quincy, Massachusetts 02269 NFPA 70: National Electrical 500 and 501 OSHA: Occupational Health and Safety Administration, U.S Department of Labor, 200 Constitution Avenue N.W., Washington, D.C 20210 COPYRIGHT 2002; American Petroleum Institute Council, 4400 Fifth Avenue, Pittsburgh, Pennsylvania 15213 SSPC SP3: Power Code, Articles Tool Cleaning Commercial SP6: SSPCSandblast , TEMA: Tubular 'Exchanger Manufacturers Association, 25 North Broadway, Tarrytown, New York 10591 Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 A P I SPEC*lLP 87 Spec 11P: Packaged Reciprocating Compressors m 2 00 7 O W for Oil and Gas Production Services SECTION GENERAL 1.1 Scope This standard covers the minimum requirementsfor a packagersupplied,designedandfabricated,skid-mounted,reciprocating,separable o r integralcompressorwithlubricatedcylindersandits prime movers used in oil and gas production services It also includes all necessary auxiliary equipment such as water and gas coolers, exhaust silencer, emission control equipment, inlet air filter, scrubbers, control panel, to installanoperableunit in piping,etc.Required compliance with the purchase specifications and with a minimum of field constructionandfieldpurchased equipment Compressorsintended for refinery,chemicalorpetrochemical services as covered in API 618 - ReciprocatingCompressorsforGeneralRefineryServices, compressors that are block-mounted, compressors that are non-lubricated,compressorswithsingle-acting,trunktype (automotive-type) pistons that also serve as crossheads, and either utility or instrument air compressors that discharge at125 pounds per square inch (PSIG) or below a r e specifically excluded from this specification Diesel engine,gasturbineandsteamturbineprime movers are also specifically excluded 1.2 Data Sheets Service and operating conditions, material requirements and sub-vendors are set out on the ‘API Packaged Compressor Data Sheets - Part 1.’ The packager shall indicate the specificsof their offering by completing the ‘API Packaged Compressor Data Sheets - Part 2.’ One copy of the completed data sheets shall accompany each copy of a quotation One complete set of ‘as-built’ ‘API Packaged Compressor Data Sheets’ shall be included in each copy of the data book furnished by the packager 1.3 Compressor Package Performance Curves.When specified, compressor package performance curves shall cover the range of operating conditions indicated by the purchaser Any limitations such as rod load, available driverhorsepower,additionalclearancerequiredto meet the range of operating conditions, etc., shall be marked on the performance curves 1.7 ElectricalLocationClassification.Allelectrical installationsshallbe in accordancewithNFPA 70 except thosein OuterContinental Shelf (OCS) areas which shall be in accordance with API R P 14F, with all locations classified in accordance with API RP500B and so specified by the purchaseron the ‘API Packaged Compressor Data Sheets- Part 1.’ 1.8 Package Installation The purchaser shall specify the site conditions (altitude, ambient temperature, etc.) on the ‘API Packaged Compressor Data Sheets - Part 1’ andwhethertheinstallation is indoors (heatedor unheated) or outdoors (with or without a roof) and the weatherorenvironmental conditions in whichthe equipment must operate (including maximum and minimumtemperatures,unusualhumidityordustproblems) The unit and its auxiliaries shall be suitable for operation in these specified conditions Purchaser shall specify size limitations,if any 1.9 TorsionalAnalysis.Thecompressorpackager will assumeresponsibilityfor a torsionallysound system consisting of primemover,coupling,compressorand flywheel, if required If the purchaser requires a torsional analysis report, the compressor packager will be responsibletocoordinatewiththecompressorand prime mover manufacturers to produce sucha report 0 1.10 Definition of Terms Use of the word ‘Design’ in any term (such as design horsepower, design pressure, design temperature, or design speed) should be avoided in the purchaser’s specifications This terminology should only be used by the equipment designer and the manufacturer Terms used in this standard are defined by the following paragraphs: 1.10.1 Maximum Allowable Operating Rod Load The maximum allowable operating rod load (manufacturer’spublishedratingcalculated by manufacturer’s standard methods) is the highest force that a manufacturer will permit forcontinuous operation 1.5 Drawings.Thepackagershallfurnishplanand elevationdrawings.Pre-fabricationapprovaloradditional drawings may be specified by the purchaser in the‘API Packaged Compressor Data Sheets - Part 1.’ 1.10.2 Combined Rod Loading The combined rod loading is the algebraic sum of gas load and inertia force Gas load is the force resulting from differential gas pressure acting on the piston differentialarea Inertia force is that force resulting from the acceleration of the reciprocating mass The inertia force with respect to the crosshead pin is the summation of all reciprocating masses (piston and rod assembly, and crosshead assembly including pin) times their acceleration 1.6 Sound Pressure Level Control of the sound pressure level of all equipment furnished shall be the joint effort of the purchaser and the packager When specified, theequipmentfurnished by thepackagershall conformtothemaximuinallowable sound pressure level required by the purchaser 1.10.3 RodReversal Rod reversal is a change in direction of force in the piston rod loading(tension to compression, or vice-versa), whichresults in a load reversal at the crosshead pin during each revolution The duration of rod reversal is usually expressed in degrees of crankcase rotation 1.4 Package Arrangement The arrangement of the packagecomponentsshallbe developed by the compressor packager to provide reasonable access for operation and maintenance COPYRIGHT 2002; American Petroleum Institute Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 A P I SPEC*11P Institute Petroleum W 2 00 8 American 1.10.4 MaximumAllowableWorkingPressure Maximum allowable workingpressure (MAWP) is themaximumcontinuouspressureforwhichthe manufacturerhasdesignedtheequipment (or any part to which the term is referred) when handling the specified fluid at the maximum specified temperature See Paragraph 2.5.1.1 fordefinition of compressor cylinder maximum allowable pressure rating 1.10.5 Rated Discharge Pressure Rated discharge pressure is the highest pressure required to meet the conditions specified by the purchaser for the intended service 1.10.6 MaximumAllowableTemperature Maximum allowable temperature is the maximum continuous temperatureforwhichthemanufacturerhas designed the equipment (or any part to which the term is referred) when handling the specified fluidat the specified pressure 1.10.7 M a x i m u m A l l o w a b l e S p e e d M a x i m u m allowable speed in revolutions per minute is the highwill estspeed at whichthemanufacturer’sdesign permit continuous operation 1.10.8 Minimum Allowable Speed Minimum allowablespeed in revolutions perminute is the lowest speed a t which the manufacturer’s design will permit continuous operation COPYRIGHT 2002; American Petroleum Institute W 1.10.9 Standard Cubic Feet Per Minute or Million Standard Cubic Feet Per Day Standard cubic feet perminute(SCFM) or million standard cubic feet at 14.7 perday(MMSCFD)referstothecapacity pounds per square inch absolute and 60 deg F 1.10.10 RequiredCapacity.Requiredcapacity is the capacity specified by the purchaser to meet process conditions 1.10.11 Quoted Capacity The quoted capacityis the capacity used by the packager to size the compressor at conditions specified by the purchaser See Paragraph 2.1.1 power is thehighest 1.10.12 RatedPower.Rated power required for any of thespecifiedoperating conditions 1.10.13 Normal Operating Point The normal operating point is the point a t which the packager certifies that the quoted capacity and power consumption is met 1.10.14 D a t a Book The data book is a book containing the manufacturer’s instructions, parts lists, data sheets, ‘as-built’ planand elevation packagedrawings, ‘as-built’ ‘API Packaged Compressor Data Sheets - Part 2’, and other pertinent data Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 API SPECmLLP 87 0732270 0087359 Spec 11P: Packaged Reciprocating Compressors for Oil and Gas Production Services SECTION COMPRESSOR 2.1 General 2.4 Rod Loadings 2.1.1 Quoted Capacity The compressor shall be sizedtohandlethequotedcapacitywiththegas analysis, suction pressures, suction temperatures,discharge pressures and site conditions specified in the - P a r t 1.’ ‘API Packaged Compressor Data Sheets The number of stages of compression shall accommodate pressure limitations and gas additions or withdrawals as set forth by the purchaser The package design shall also allow for all pressure drops through the scrubbers, pulsation bottles (if any),coolers and piping from the inlet flange to the outlet flange on the skid 2.1.2 Performance Calculations The compressor packager shall use the gasanalysis, suction pressures, suction temperature,dischargepressuresandsite conditions as specified by the purchaser to calculate molecular weight, ratio of specific heats (Cp/Cv), and compressibility factor (Z) The compressor packager shall indicate his values on the ‘API Packaged Compressor Data Sheets - Part 2’, provide them with the quotationandusethemtocalculateperformance data 2.1.3 Compressor Size When specified, the compressorframesshallbefurnishedwithcylinders which, when operating atthe specifiedoperating condition@), shall,asfaraspractical, load the gas enginetothelimitspecified in Paragraph 4.2.1 or electricmotortothelimitspecified in Faragraph 4.3.2 NOTES: Compressors driren by indz(ctiot1 motors shall be sized at the motor operatiny speed 2.1.4 ForcesandCouples When specified by the purchaser,thecompressormanufacturershalIfurnish values for the un-balance primary and secondary forcesand couplesin thehorizontalandvertical planes for the quoted cornpressor 2.2 MaximumAllowableSpeeds.Themaximum allowable average piston speed (in feet per minute) and the maximum allowable speed (in revolutions per minute) may be specified by the purchaser 2.3 MaximumAllowableDischargeTemperature The compressor shall be provided with sufficient compression stagesandinterstage cooling tolimitthe actual discharge temperature of each stage to 350 deg F unless otherwise specified by purchaser This limit shall hold for a11 specifiedoperatingand Ioad conditions Whenspecified,thecompressorpackagershall provide the purchaser with both the estimated actual andthecalculatedadiabaticdischargetemperature rise COPYRIGHT 2002; American Petroleum Institute 2.4.1 Maximum Allowable Rod Loading The maximum operating rod load (gas or combined) shall not exceed the maximum allowable operatingrod loading for the compressor or any rod load limitation specified by the purchaser at any specified operating condition The packager shall quote gas rod load unless specified otherwise by the purchaser If other than operating rod load calculations are specified, the purchaser will provideoperatingparameterstothe packager for making these calculations 2.4.2 Piston Rod’ Load Reversal For all specified operating load conditions, the axial component of the combined rod loading shall reverse enough to ensure adequate lubrication between the crosshead pin and bushing during each complete turn of the crankshaft 2.5 Compressor Cylinders 2.5.1 General 2.5.1.1 Cylinder Maximum Allowable Working Pressure The maximum allowable working pressure of thecylindershall exceed therated discharge pressure by a t least 10 percent or 25 psig, whichever is greater 2.5.1.2 Cylinder Orientation Horizontal cylinders shallhave bottom discharge connections except where side or top dischargeconnections are acceptable by the purchaser 2.5.1.3 Cylinder Maintenance Cylinders shall be spaced and arranged to permit access and removal for normal maintenance of all components (including covers, packing, valves, or unloaders mounted on thecylinder)withoutremovingthecylinder, major piping or pulsation bottles 2.5.2 CylinderFrame Appurtenances 2.5.2.i CylinderSupports.Thecylindersupport shall be designed to avoid misalignment or excessive rod run-out during the warm-up period and at actual operating temperature The cylinder support shall not be attached to the outboard cylinderhead The pulsation bottle, if furnished, shall not be used to support the compressor cylinder unless approved by the compressor manufacturer 2.5.2.2 CylinderBody.Cylindersmaybe noncooled (no provision for coolant jackets) or cooled (coolant jacket around cylinder bore and cylinder head) 2.5.2.3 Cylinder Bolting Cylinder heads, stuffing boxes for pressure packing, clearance pockets, and valve covers shallbefastenedwitheithercap- Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 Petroleum 68 American Institute COMPRESSOR PERFORMANCE Continued 2.1.2 - 2.1.3 - 2.3 - 2.4.1 CASE SERVICE STAGE NUMBER OF CYLINDERS - INCHES BORE CYLINDER RATED DISCHARGE PRESSURE - PSIG ALLOWABLE WORKING PRESSURE - PSIG ALLOWABLE WORKING - "F - INCH-# TEMP NOZZLE SIZE AND RATING CYLINDER ACTION - (DA/SACE/SAHE) - CFM PISTON DISPLACEMENT/CYL SPECIFIC GRAVITY C&, (K) VALUE CRITICAL PRESSURE - PSIA CRITICAL TEMPERATURE - "R COMPRESSIBILITY (Z) AT SUCTION COMPRESSIBILITY (Z) AT DISCHARGE GAS SUCTION PRESSURE* - PSI- GAS DISCHARGE PRESSURE * - PSI- "F - "F GAS SUCTION TEMP GAS DISCHARGE TEMP - ADB GAS DISCHARGE TEMP - EST ACT - "F REQUIRED CAPACITY - MMSCFD QUOTED CAPACITY - MMSCFD GAS HORSEPOWER/STAGE - BHP - BHP GAS HORSEPOWER - TOTAL HORSEPOWER - ACCESSORIES - BHP UNIT HORSEPOWER - TOTAL - BHP BHP-TOTAL/BHP-SITE X 100 -% ACTUAL SPEED - RPM ACTUAL PISTON SPEED - FPM CYLINDER CLEARANCE - H E -% CYLINDER CLEARANCE- C E -% VOLUMETRIC EFF - H E -% VOLUMETRIC EFF - C E -% ROD LOAD (GAS) - COMP - POUNDS COPYRIGHT 2002; American Petroleum Institute Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 Spec 11P: Packaged Reciprocating Compressors for and Oil Gas Production Services 69 COMPRESSOR PERFORMANCE Continued - TENS ROD LOAD(GAS+INRT) - COMP ROD LOAD (GAS+INRT) - TENS - POUNDS - POUNDS CLEARANCE POCKET TRAVEL - % OPEN VALVE SPACERS INSTALLED - #/CYL VALVE VELOCITY -AVERAGE - FPM ROD LOAD (GAS) - POUNDS VALVES/CORNER-SUCTION/DISCHARGE VALVE TYPE AND SIZE - INCHES VALVE - INCHES AREA LIFT VALVE - SQINCH LIFT FEET TEMP: AIR BAROMETRIC PRESSURE: PSIA "F UNITCAPACITY - MMSCFD - ISMEASUREDATPSIAAND 60 "F * - PRESSURES MEASURED AT INLET AND OUTLET FLANGES OF COMPRESSOR CYLINDERS ALTITUDE: COMPRESSOR CAPACITY CONTROL PART LOAD OPERATION CASE SERVICE STAGE CYLINDER ACTION - (DA/SACE/SAHE) GAS SUCTION TEMPERATURE - "F GAS SUCTION PRESSURE - PSI- GAS DISCHARGE PRESSURE - PSI - REQUIRED CAPACITY - MMSCFD CAPACITY QUOTED - MMSCFD HORSEPOWER/STAGE GAS - BHP GAS HORSEPOWER - TOTAL - ACCESSORIES UNIT HORSEPOWER - TOTAL HORSEPOWER - BHP - BHP - B H P BHP-TOTAL/BHP-SITE X 100 "x ACTUAL S P E E D - RPM - H E CYLINDERCLEARANCE - C E -% CYLINDERCLEARANCE -% CLEARANCE POCKET TRAVEL - %OPEN VALVE SPACERS INSTALLED - #/CYL CLEARANCE PLUG - YES/NO CLEARANCE BOTTLE - YES/NO UNLOADERS VALVE CAPACITY CONTROL BYPASS COPYRIGHT 2002; American Petroleum Institute - YES/NO - YES/NO Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 API S P E C m L l P 89 m 2 00 2 Petroleum 70 American i Institute COMPRESSOR CAPACITY CONTROL Continued PART LOAD OPERATION CASE SERVICE STAGE CYLINDER ACTION - (DA/SACE/SAHE) GAS SUCTION TEMPERATURE -OF GAS SUCTION PRESSURE - PSI- GAS DISCHARGE PRESSURE GAS HORSEPOWER/STAGE - PSI- MMSCFD - MMSCFD - BHP GAS HORSEPOWER - TOTAL - BHP HORSEPOWER - ACCESSORIES UNIT HORSEPOWER- TOTAL - BHP - BHP BHP-TOTAL/BHP-SITE X 100 -% ACTUAL S P E E D - RPM CYLINDER CLEARANCE - H E -% CYLINDER CLEARANCE - C E -% CLEARANCEPOCKETTRAVEL - %OPEN VALVE SPACERS INSTALLED CLEARANCE PLUG - #/CYL - YES/NO CLEARANCE BOTTLE - YES/NO VALVE UNLOADERS - YES/NO CAPACITY CONTROL BYPASS - YES/NO REQUIRED CAPACITY QUOTED CAPACITY PART LOAD OPERATION CASE SERVICE STAGE CYLINDER ACTION - (DA/SACE/SAHE) GAS SUCTION TEMPERATURE - "F GAS SUCTION PRESSURE - PSI- GAS DISCHARGE PRESSURE - PSI- REQUIRED CAPACITY - MMSCFD - MMSCFD CAPACITY QUOTED HORSEPOWER/STAGE GAS GAS HORSEPOWER - TOTAL HORSEPOWER - ACCESSORIES COPYRIGHT 2002; American Petroleum Institute - BHP - BHP - BHP Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 87 M 2 00 2 A P I SPEC*LLP Spec 1 P Packaged Reciprocating Compressors for M Oil and Gas Production Services COMPRESSOR CAPACITY CONTROL Continued UNIT HORSEPOWER -TOTAL - BHP BHP-TOTAL/BHP-SITE X 100 "x - RPM SPEED ACTUAL CYLINDERCLEARANCE - H E -% CYLINDERCLEARANCE - C E -% CLEARANCE PLUG - %OPEN - #/CYL - YES/NO CLEARANCE BOTTLE - YES/NO CLEARANCE POCKET TRAVEL VALVE SPACERS INSTALLED - - YES/NO UNLOADERS VALVE CAPACITY CONTROL BYPASS - YES/NO PART LOAD OPERATION CASE SERVICE STAGE CYLINDER ACTION- (DA/SACE/SAHE) GAS SUCTION PRESSURE -O F - PSI- GAS DISCHARGE PRESSURE - PSI- REQUIRED CAPACITY - MMSCFD QUOTED CAPACITY - MMSCFD GAS HORSEPOWER/STAGE HORSEPOWER - ACCESSORIES - BHP - BHP - BHP UNIT HORSEPOWER- TOTAL - BHP BHP-TOTAL/BHP-SITE X 100 -% ACTUAL SPEED - RPM CYLINDER CLEARANCE - H E -% CYLINDER CLEARANCE - C E -% CLEARANCE POCKET TRAVEL VALVE SPACERS INSTALLED - % OPEN - #/CYL CLEARANCE PLUG - YES/NO CLEARANCE BOTTLE - YES/NO - YES/NO - YES/NO GAS SUCTION TEMPERATURE GAS HORSEPOWER - TOTAL VALVE UNLOADERS CAPACITY CONTROL BYPASS COPYRIGHT 2002; American Petroleum Institute Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 71 American Petroleum Institute 72 COMPRESSOR CAPACITY CONTROL Continued 3.2.1 - SPEED VARIATION: NO YES MANUAL [ ] 3.2.2.2 - CLEARANCE POCKETS: YES NO FIXED (OPEN/CLOSED) [ ] VARIABLE [ ] MANUAL [ AUTOMATIC [ ] CYLl [ ] CYL2 [ ] CYL3 [ CYL4 [ ] 3.2.2.3 - VALVESPACERS: HEAD-END: CYLl [ CRANK-END: CYLl [ ] YES [ ] CYL2 [ I YES [ ] CYL2 [ I 3.2.2.4 - CLEARANCEBOTTLES: CYLl [ ] CYL2 [ CYL2 [ I CLEARANCE PLUGS: r cYL1 3.2.3.1 - BY-PASS SYSTEMS: START-UP MANUAL [ c 1 RANGE TO _ RPM AUTOMATIC [ ] ~ NUMBERNO [ ] CYL3 [ ] CYL4 [ ] NUMBERNO [ CYL3 [ ] CYL4 [ ] YES [ CYL3 [ YES CYL3 [ ] NO [ CYL4 [ ] NO CYL4 [ ] CAPACITY CONTROL [ ] HOT [ ] COLD [ ] AUTO [ ] YES NO PLATE DEPRESSORS [ ] AUTOMATIC [ ] PLUG [ ] MANUAL [ ] CYLl [ ] CYL3 [ ] CYL2 [ ] CYL4 [ I 3.2.4.3 - VALVE UNLOADERS: 3.2.5 - PRESSURE CONTROL YES NO [ ] [ ] SUCTION [ DISCHARGE [ ] P R I M E MOVER - GAS ENGINE MANUFACTURER MODEL SITE RATED POWER -BHP BORE: INCHE ES NUMBER OF POWER CYLINDERS: COMPRESSION RATIO: MIN SPEED: _ RPM RATED SPEED: _ RPM STROKE: -INCHES DISPLACEMENT: CU INCH TURBOCHARGED [ ] NATURALLY ASPIRATED [ FBTU/BHP-HR U E L CONSUMPTION: ~ ~ - STARTING SYSTEM: ELECTRIC AMPERE-HOUR BATTERY 4.2.3.2.3 CHARGINGALTERNATOR - ANDYES 4.2.3 4.2.3.2.2 ORGAS [ ] SET: 4.2.4 - FILTER AIRMANUFACTURER’S STANDARD DRY TYPE: YES 4.2.4.1 - OR OTHERYES [ ] AIR [ ] [ ] NO [ ] IF ELECTRIC, YES [ - MFG’S STANDARD INDUSTRIAL SILENCER TYPE YES 4.2.5.1 - OR OTHER YES [ ] NO [ ] 1 IF YES, SPARK-ARRESTING NON SPARK-ARRESTING [ ] SOUND ATTENUATION: PERSONNEL PROTECTION [ ] (EXPLAIN): - QUOTED EMISSION DATA (GM/BHP/HR) IS FROM MFG’S PAST PERFORMANCE 4.2.8.1 - DATA [ ] OR ACTUALSTACKTEST ENGINENAMEPLATERATING [ 1: - [ ] AND IS BASED ON QUOTEDBHP GALLON CRANKCASE STORAGE OIL TANK: YES - CRANKCASE EXPLOSION COPYRIGHT 2002; American Petroleum Institute NO [ ] OR DIOXIDE: SULFUR [ 4.2.11.5 FILTER/SEPARATOR - FUEL YES 4.2.12 CH4 HYDROCARBONS: MONOXIDE: CARBON 4.2.10 NO NO [ ] 4.2.8 NITROUS NON OXIDE: NO 1 NO IF YES, EXPLAIN: PRESSURE AIR INDICATOR DROP YES 4.2.4.2.6 FILTER 4.2.5 1 1 NO NO DOORS: YES NO Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 [ 1 A P I SPEC*lLP 89 2 7000 2 Spec 11P: Packaged Reciprocating Compressors for Oil and Gas Production Services 73 PRIME MOVER - ELECTRIC MOTOR 4.3.1 MANUFACTURER MODEL: SYNCHRONOUS [ ] INDUCTION [ ] SITE RATED POWER RATED SPEED: S.F.: NEMA RATING: ENCLOSURE TYPE: FRAME VOLTS: PHASE: HERTZ: _CLASS: GROUP: DIVISION: INSULATION: TEMPERATURE RISE: "C ABOVE "C SPACE HEATER: YES [ ] NO [ ] I F Y E S , VOLTS PHASE: HERTZ: NO [ ] IF YES,NEMA RATING: MOTOR STARTERAND CONTROLS: Y E S [ ] MANUFACTURER FULLVOLTAGE [ ] VOLTAGE REDUCED ~ ~ ~ RPM ~ ~ [ ] COOLING SYSTEM MANUFACTURER MODEL ELECTRIC MOTOR DRIVE [ ENGINE V-BELT [ ] VERTICAL [ ] HORIZONTAL [ ] MOUNTED ON ENGINE/COMPRESSOR SKID [ MOUNTED ON SEPARATE COOLER SKID [ 5.3.1.2 - SIGHT FLOW 5.3.5 - GAS AFTERCOOLER TO [ ] AND/OR TEMPERATURE INDICATORS "F: WATER SECTION MAWP : -# SECOND STAGE GAS MAWP : -# FOURTH STAGE GAS MAWP : _ # YES C [ ] YES NO[ NO [ 1 FIRST STAGEGAS MAWP : _ # # THIRD STAGE GAS MAWP : # AFTERCOOLER GAS MAWP : ~ ~ FPM SPEED: TIP FANS: FEET DIAMETER NUMBER 5.6.6 5.6.7 - AUTOMATIC [ ] OR MANUAL [ CONTROL O F COOLER AIR CIRCULATION ON INTERSTAGE GAS [ ] AND/ORFINAL DISCHARGE GAS [ ] YES [ ] NO [ I F Y E S , BY: LOUVERS [ ] VARIABLE PITCH RE-CIRCULATION [ ] OTHER [ ] (EXPLAIN): FAN [ ] - COOLER BUG SCREENS AND/OR HAILGUARDS [ [ ] 1: YES C I NO C PRESSURE VESSELS 6.1.3 - 6.2.5 - 6.2.6 - 6.3.5 - 6.3.7 6.3.2-PULSATION STUDY YES [ ] NO [ ] SCRUBBERS I F Y E SE,X P L A I N STAGE STAGE STAGE DESIGN CLASS DIAMETER INSIDE - INCHES SEAM-TO-SEAM LENGTH PRESSURE DESIGN - INCHES - PSIG DESIGN TEMPERATURE - "F MESH PAD/VANE MIST EXTRACTOR MIST EXTRACTOR MATERIAL DRAIN MANUAL - YES/NO TYPE AUTOMATIC DRAIN CONTROL TYPE AUTOMATIC DRAIN VALVE LIQUID LEVEL GAGE GLASS - YES/NO PRESSURE INDICATOR - YES/NO TYPEANDSIZEINLETFLNG - INCHES TYPEANDSIZEOUTLETFLNG - INCHES CORROSION ALLOWANCE - INCHES PADS/SADDLES WELD COPYRIGHT 2002; American Petroleum Institute - YES/NO Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 DISCHARGE API SPEC*:LLP W 2 00 2 O m American Petroleum Institute 74 PRESSURE VESSELS Continued SUCTION PULSATION/VOLUME BOTTLES VOLUME INCH - CU SWEPT VOLUME MULTIPLIER DIAMETER INSIDE SEAM-TO-SEAM LENGTH - INCHES - INCHES TYPEANDSIZEINLETFLNG - PSIG - "F - INCHES TYPEANDSIZEOUTLETFLNG - INCHES CORROSION ALLOWANCE - INCHES PRESSURE DESIGN DESIGN TEMPERATURE ASME CODE OR B31.3 TYPE DRAIN OPENING PADS/SADDLES WELD - YES/NO DISCHARGE PULSATION/VOLUME BOTTLES VOLUME - CU INCH SWEPT VOLUME MULTIPLIER INSIDE DIAMETER - INCHES SEAM-TO-SEAM LENGTH - INCHES DESIGN PRESSURE - PSIG DESIGN TEMPERATURE -OF TYPE AND SIZE INLET FLNG - INCHES TYPE AND SIZE OUTLET FLNG - INCHES CORROSION ALLOWANCE - INCHES ASME CODE OR B31.3 TYPE DRAIN OPENING WELD PADS/SADDLES - YES/NO PIPING AND APPURTENANCES 7.1.4 - T H E E X T E N T O F T H EGAS PIPING SUPPLIED SHALL BEGIN AT THE PACKAGE SUCTION FLANGE AND BE CONTINUOUS THROUGH THE SYSTEM TO THE PACKAGE DISCHARGE [ NO FLANGE? YES OR T H E GAS PIPING SHALL BEGIN AS FOLLOWS: UBBER SUCTION AT FLANGE SUCTION: FLANGE AT SUCTION BOTTLE [ ] OR FLANGE AT COMPRESSOR NOZZLE [ ] [ ] OTHER(EXPLA1N): [ ] INTERSTAGE: FLANGE AT SUCTION BOTTLE [ ] SIDESTREAMCONNECTION [ COPYRIGHT 2002; American Petroleum Institute FLANGE AT INTERSTAGE SCRUBBER [ ] OR COMPRESSOR NOZZLE [ ] COMPLETE INTERSTAGE PIPING SYSTEM [ ] Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 A P I SPEC*KLLP 89 H 2 00 2 Spec 11P: Packaged Reciprocating Compressors for Oil and Gas Production H Services 75 PIPING AND APPURTANCES Continued OTHER(EXPLA1N): [ ] AT FLANGE DISCHARGE COOLER DISCHARGE [ FLANGE DISCHARGE AT BOTTLE [ ] OR COMPRESSOR NOZZLE C SPOOL PIECE FROM FINAL DISCEARGE COOLER TO DISCHARGE SCRUBBER C ] I OTHER(EXPLA1N): [ ] PIPING, BOTTLES(IF ANY), VESSELS AND THERMOWELLS DESIGNED AND ARRANGED FOR INSULATION: AND/OR TRACING HEAT YES NO c 3RD 2ND 1ST INTERINTERINTER SUCTION STAGE STAGE STAGE DISCHARGE 7.12 - 7.20.2 - 7.21 PIPING I.D PRESSURE DESIGN DESIGN TEMPERATURE - INCHES RELIEF VALVE SIZE RELIEF VALVE SETTING RELIEF VALVE ORIFICE - INCHES BLOCK VALVE SIZE BLOCK VALVE RATING - INCHES - PSIG BLOWDOWN VALVE SIZE BLOWDOWN VALVE RATING - INCHES - PSIG - INCHES - PSIG CHECK VALVE SIZE CHECK VALVE RATING 7.8 7.10 7.11 - PSIG - "F - PSIG - INCHES - SEALWELDED,THREADEDPIPINGJOINTS: - ERW STEEL USED FOR SCREWED, FLANGED OR WELDED PIPI1 - STEEL ~ 0SERIES STAINLESS STEEL c I YES YES TUBING FITTINGS: 7.12 7.15 7.16.2 7.17.1 - VALVES IN FLAMMABLE OR TOXIC SERVICE SHALL HAVE BOLTED OR WELDE BONNETS C BOLTED GLANDS AND BE'FIRE-SAFE' c YES C NO - TEMPORARY START-UP SCREENS: YES C NO C REMOVABLE SPOOL-PIECE: - STEEL [ OR300STAINLESSSTEEL [ J OIL LINES NO DOWNSTREAM THE OF OIL YF E ISL T E R - COMPLETE ON-SKID COOLANT PIPING SYSTEM FOR LIQUIDCOOLED 7.19.3 - COMMON DISTANCE PIECE VENT HEADER - COMMON DISTANCE HEADER DRAIN PIECE YES 7.19.4 - COMMON PACKING HEADER VENT 7.20.4 - RELIEF AND BLOWDOWN VALVESVENTTOATMOSPHERE 7.21 - INTO COMMON HEADER 7.19.2 OR OTHER(EXPLAIN): COPYRIGHT 2002; American Petroleum Institute [ [ ] c NO YES c NO NO c 1 YES [ ] NO [ I YES CYLINDERS: OR [ ] Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 A P I SPEC*LLP 87 W 2 7000 2 W American Petroleum Institute 76 ELECTRICAL SYSTEMS 8.2 SERVICE ELECTRIC MOTOR MANUFACTURER MODEL SPEED NEMA RATING FRAME TYPE DC VOLTS AC PHASE/HERTZ/VOLTS ENCLOSURE TYPE SERVICE FACTOR MOTOR CONTROL MANUFACTURER NEMA RATING 8.5 - ELECTRICAL MATERIAL SUITABLE FOR TROPICAL LOCATION YES NO INSTRUMENTS AND CONTROLS 9.1 - IN ADDITION TO ANY INSTRUMENT AND CONTROL PANELS AND TO ANY CAPACITY CONTROL, T H E FOLLOWING CONTROL SYSTEMS ARE INCLUDED: FUNCTION: MANUAL/AUTO: 9.1.5 - PNEUMATIC INSTRUMENT SUPPLY GAS [ ] 9.2.1 - INSTRUMENT ENCLOSED PANEL WITH YES BACK 9.2.2 - FREE-STANDING, SKID-MOUNTED 9.2.3 - WIRINGTOREMOTEPANELSINSTALLEDINCONDUITS ARMOREDCABLE [ ] 9.3.1 - PANELMOUNTEDDIGITAL 9.3.2 - LIQUIDFILLEDTEMPERATUREINDICATORS: 9.3.2.4 - GROUNDED [ 9.3.3 - LIQUIDFILLEDPRESSUREINDICATORS: ORINSTRUMENT AIR [ ] I OROFF-SKID MOUNTED NO [ ] PANEL [ ] OR ENCLOSURES [ ] OR [ ] OR ANALOG [ ] TACH: OR UNGROUNDED [ ] YES C YES [ ] THERMOCOUPLES: YES YES 1 1 NO NO NO C 1 E NO SHUTDOWNS, ALARMS AND ANNUNCIATORS 10.1 - SHUTDOWNS, ALARMS AND ANNUNCIATORS COPYRIGHT 2002; American Petroleum Institute - PNEUMATIC [ OR ELECTRIC [ ] Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 Spec 11P: Packaged Reciprocating Compressors for and Oil Gas Production Services II PART 1- MATERIAL REQUIREMENTS SHUTDOWNS, ALARMS AND ANNUNICIATORS SENSING TYPE DESIRED LOCATION ANNUNCIATION ACTION 9.3.2 - 9.3.3 - 10.2.1 NOTE: S [X]DESIRED ACTION, INDICATES THE AND TYPE LOCATION ANNUNCIATION OF AND LOCATION SENSING THE OF DEVICE MARK EACH BOX FOR REQUIREMENTS MULTIPLE A D H U T D O W N DEVICE LOCATION I N I v u A C I D P L A S I A A U T B N N O C A L E R O L E L M R R E M T E P A L O E L A L COMPRESSOR SUCTION GAS PRESSURE - FIRST STAGE LOW HIGH SUCTION GAS PRESSURE- INTERSTAGE LOW HIGH DISCHARGE GAS PRESSURE - INTERSTAGE LOW HIGH DISCHARGE GAS PRESSURE-FINAL STAGE LOW HIGH LUBE OIL PRESSURE I N - FILTER OUT - FILTER LOW LUBE OIL TEMPERATURE IN OUT HIGH GAS TEMPERATURE- EACH STAGE SUCTION DISCHARGE - EACH CYLINDER HIGH - EACH CYLINDER LUBE OIL LEVEL LOW - FRAME LOW - LUBRICATOR LUBRICATOR NO-FLOW VIBRATION HIGH CYLINDER COOLANT TEMPERATURE IN OUT - EACH CYLINDER HIGH [XI CXI C l [ I LX1 C J [ I [XI E l [ I C l [XI C l [ I [ I C l C l Cl [ I [XI Cl C l c [XI [ I C I Cl Cl Cl [ I [XI C l [ I [ I [ I [ I Cl Cl [ I [ I Cl C l C l [XI [XI C l C l Cl [ I Cl [ I Cl [ I Cl [ I CXI C l C l C l Cl C l Cl r [ I C l C l Cl [ I Cl Cl Cl Cl [ I Cl [ I [ I [ I Cl [ I [ I C l Cl [ I [ I E l [ I Cl [ I [ I [ I Cl [ I C l Cl Cl C l C l [XI [XI C l E l Cl Cl Cl [ I [ I Cl [ I [ I [XI [ I C l [ I [ I [ I Cl [ I Cl [ I [XI C l C l [XI [ I C l [ I C Cl l rx1 NATURAL GAS ENGINE - IF FURNISHED HIGH/LOW MANIFOLD PRESSURE/VACUUM COOLANT TEMPERATURE IN OUT HIGH COPYRIGHT 2002; American Petroleum Institute Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 American Petroleum Institute 78 SHUTDOWNS, ALARMS AND ANNUNCIATORS Continued NOTE: S [X]DESIRED INDICATES THE ACTION, AND TYPE LOCATION OF ANNUCIATION AND LOCATION OF SENSING THE DEVICE EACH MARK BOX FOR MULTIPLE REQUIREMENTS H U T D O W N I N A D I A C L A AU T B R O M R v I S u D P I A N N O C A L E L E L R R M T E P A E L LUBE OIL TEMPERATURE IN OUT HIGH LUBE OIL PRESSURE IN - FILTER OUT - FILTER LOW COOLANT PRESSURE IN OUT LOW FUEL GAS PRESSURE STARTING AIR/GAS PRESSURE VIBRATION HIGH LUBE OIL LEVEL LOW OVERSPEED STATOR WINDING TEMPERATURE HIGH VIBRATION HIGH HIGH COOLER COOLANTLEVEL LOW SCRUBBER LIQUIDLEVEL COPYRIGHT 2002; American Petroleum Institute Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 L O A L API SPEC*kLLP 87 W 2 0O 2 T m Spec 11P: Packaged Reciprocating Compressors for Oil and Gas Production Services 79 SKID 11.1 - CONSTRUCTION: STRUCTURAL STEEL [ ] PRE/POST STRESSED CONCRETE [ ] CONCRETE FILLED STRUCTURAL STEEL [ OTHER(EXPLA1N): BEAM: POUNDS WEIGHT INCHES FLANGE C YES PLATE:DECK I] - FRAME MOUNTING BOLTED 11.2.3 - PRIME MOVERMOUNT: BOLTED [ ] GROUTED [ ] SOLE PLATE/RAIL ’[ ] - SHIMMATERIAL - FOUNDATION BOLTS: NUMBEROFFOUNDATIONBOLTSPERSIDE: - SCRUBBER MOUNTING BOLTED [ ] WELDED TO STRUCTURAL MEMBERS [ ] - WALKWAYS/STAIRS: PROVIDED WITH WALKWAYS: YES NO 11.2.6 11.2.9 11.4 SOLE PLATE/RAIL 11.2.3 11.2.4 GROUTED [ NO [ ] OVERALL SHIPPING DIMENSIONS AND WEIGHT MAIN SKID HEIGHT -FEET WIDTH - F E E T LENGTH - FEET WEIGHT - POUNDS PAINT AND PAINTING 12.1 - PACKAGE: PACKAGER’S STANDARD [ SPECIAL (EXPLAIN): r 12.1 - COMPRESSOR PACKAGER’S STANDARD [ ] SPECIAL (EXPLAIN): I I 12.1 - PRIME MOVER PACKAGER’S STANDARD [ ] SPECIAL (EXPLAIN): I l 12.5 - AIREXCHANGER SIDING/STRUCTURE: HOT-DIP GALVANIZING [ J PACKAGER’S STANDARD [ ] SPECIAL(EXPLAIN): [ ] PACKAGER’S STANDARD [ ] SPECIAL (EXPLAIN): [ I HEADERS: HOT-DIP GALVANIZING [ I INSPECTION, TESTING, AND PREPARATION FOR SHIPMENT 13.2.1.3 13.2.3 13.3.1.1 - TESTS PERFORMED: REVIEW OF QUALITY CONTROL MECHANICALRUN [ ] PACKAGE ASSEMBLED [ ] [ ] - HYDROSTATIC [ AIR PRESSURE TEST OF OTHER (EXPLAIN): [ ] 13.2.2 COPYRIGHT 2002; American Petroleum Institute - INSPECTIONS: BY PURCHASERTYPE(EXPLAIN): Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 API S P E C m L L P B9 m 2 00 b W American Petroleum Institute 80 INSPECTION, TESTING,AND PREPARATIONFOR SHIPMENT Continued 13.5.1 13.5.2 YES [ YES YES EXPORT CRATED: PACKAGER STORAGE: SPECIAL SHIPMENT PREPARATION - SHIPMENT: 1 NO NO NO 1 1 NO IF YES, EXPLAIN: ~~~~ ~ SPECIAL LIFTING YES LUGS, ETC IF YES, EXPLAIN: CORROSIVE GASES 15.1 - CORROSIVE COMPRESSED: GAS YES [ NO 15.3.2.3 - PRECIPITATIONHARDENEDSTAINLESSSTEELPISTON ROD [ ] OR 15.4.3.2 4140 STEELPISTON ROD ANNEALED TO C22 [ ] WITHHARDENINGINTHEPACKING AREAEITHER BY CHROMEPLATING [ ] OR TUNGSTONCARBIDE COATING [ ] OR NACE MATERIAL EQUIVALENT PISTON ROD [ ] 15.3.3.7 - PURGED PACKING CASES: YES GAS [ ORINERT GAS [ ] 15.3.3.7 - DISTANCE PIECE: TYPE EVACUATED WITH ORPURGED YES ORINERT GAS [ ] 15.3.4 NO [ [ ] IF YES, WITH SWEET NATURAL TYPE: [ APUMP: VACUUM [ ] NO [ ] ORTYPE [ ] ORTYPE [ YES NO WITH SWEET NATURALGAS [ TYPE: - H# AND/ORCOz: FURNISHAUSTINITIC r OR 12CR [ I STAINLESSSTEELONALLPARTSTHATARE IN CONTACT WITH THE PROCESS GAS STREAM: PROCESS STEEL GAS PIPING COLD SIDE PIPING PIPINGHOT SIDE PIPING BYPASS LINES VENT LINES DRAIN PULSATION BOTTLES SUCTION DISCHARGE SCRUBBERS SUCTION INTERSTAGE DISCHARGE GAS COOLER HEADER TUBES VALVES SUCTION BLOCK DISCHARGE BLOCK VALVES BYPASS BLOWDOWN VALVE VALVE CHECK UTILITY PROCESS VALVES VALVES RELIEF INSTRUMENTATION SCRUBBER CONTROLS SWITCHES PRESSURE TEMPERATURE SWITCHES TUBING FITTINGS COPYRIGHT 2002; American Petroleum Institute CARBON [ [ [ [ I I I I [ [ [ [ [ [ I I I I I I [ I [ I [ [ [ [ [ [ [ I I I I I I I [ [ [ [ [ I I I I I STAINLESS OTHER STEEL [ I Cl [ I [ I r t I r [ I [ I [ I Cl [ I Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 I " OFFSHORE AND/OR MARINE ENVIRONMENT 16.1.3 ENVIRONMENT: -YES CORROSIVE 16.2.1 - SHIELDED [ ] 16.4.1 - COOLER HEADERS: OR NON-SHIELDED [ ] C ] HOT-DIPPED GALVANIZING 16.8.4 NO LOW TENSION MAGNETO IGNITION SYSTEM PACKAGER'S MANUFACTURER'S STANDARD PAINT SPECIAL (EXPLAIN): PAINT C ] [ ] - DISCHARGEPIPINGINSULATION: DISCHARGE BOTTLE INSULATION: 16.10.3 - BLOCK VALVES: MANUAL AND/OR DISCHARGE [ ] [ OR PILOT-OPERATED [ ] BLOCK VALVE: YES SUCTION [ NO C C 16.10.4 - PISTON DISCHARGE TYPE CHECK VALVE: YES MISCELLANEOUS INDICATED: DRAWINGS PROPOSAL REPORTS COPIES FURNISH DATA BOOKS 1.3 MISC CURVES - PERFORMANCE CURVES: INDICATE RANGE: 1.5 - APPROVAL DRAWINGS: AS BUILTDRAWINGS: MISCELLANEOUS DRAWINGS: IF YES, EXPLAIN: - TORSIONAL REPORT COPYRIGHT 2002; American Petroleum Institute Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584 NO [ 1 ~~ A P I SPEC*ltLP 87 82 m 2 00 T m American Petroleum Institute EXCEPTIONS TO API SPECIFICATION 11P COPYRIGHT 2002; American Petroleum Institute Document provided by IHS Licensee=Sincor Venezuela/5934214100, User=, 08/13/2002 13:04:35 MDT Questions or comments about this message: please call the Document Policy Management Group at 1-800-451-1584