Art's Collection of Spec Sheets

IntroductionSpecification Sheets Included in This WorkBook1Art's API 650 Storage Tank2Art's Centrifugal Pump3Art's Air-Cooled Exchanger4Art's Shell & Tube Exchanger5Art's Plate & Frame Heat Exchanger6Art's Process Vessel7Art's Control Valve8Art's Centrifugal Blower9Art's Orifice Meter10Art's Coriolis Meter11Art's Ultrasonic Meter12Art's Mass Meter13Art's Turbine Meter14Art's Vortex Meter15Art's Magnetic Meter16Art's .The accurate and complete preparation of Specification Sheets is one of the most (if not THE most)important capabilities that a Chemical, Process, or Project Engineer should acquire very early in his/hercareer.An engineer is a problem solver, pure and simple. However, one cannot simply solve problems bydirectly applying ones own efforts and time. In the industrial and competitive world, an engineer simplydoes not have the time available to do all that must be done in order to resolve day-to-day problems.That is why engineers are required to lead and supervise those around them in order to assure anorganized team-effort in resolving problems. To this end, engineers use communications skills (bothoral and written) as well as language, psychology, and interpersonal skills to inform and lead otherteam members to a successful resolution.At the very basic foundation of problem solving is the successful communications of the requiredcapital equipment required to resolve engineering problems. An engineer is unable to resolve a problemif he/she is unable to successfully describe it in detail to the "stake holders" in a project. The ability toreceive constructive and cost-effective help and supply from parties involved in the project is directlyrelated to the timely and accurate description of the supply needed to resolve a problem.Specification sheets are the indicated tools that are relied upon by engineers to convey an accurateand detailed description of their needs and expected supply. These Specification sheets not only serveto identify the required supply, they also serve to organize and structure the knowldege of the owner'sengineers as to the criticality and strategic importance of the supply. They force the Owner to complywith the classic business rule: Emptor Caveat - buyer beware.It is a basic business principle and law that the responsibility of defining the specific need for a supplyof goods or materials lies directly with the purchaser (or Owner). If you don't know what you need or don'tknow how to describe what you need, you will never resolve your own problems. The Specification Sheetdescribes to others not only what you identify as your specific needs, it also documents them andcommunicates this information to all interested parties.A large part of the problem in preparing accurate Spec Sheets is that the lead engineers (who often are themost experienced and knowledgeable) are not the ones that prepare the Spec Sheets. It falls upon theProcess and Project engineers to prepare them and many times these individuals have to be trained andinstructed on how to describe and specify equipment that they are only superficially familiar with. Therefore,good Spec Sheets should be easy and simply to prepare, with a minimum of detail knowledge required.I have arranged and organized the Spec Sheets found in this WorkBook in a manner that they should berather easy and intuitive for young engineers to prepare. A maximum use is made of drop-down list boxesin order to facilitate the required information to engineers who are unaware of the various feature choicesavailable or much less how to describe them or spell them correctly. This method also "standardizes"a variety of choices and does not leave it up to the individual to select whatever he/she thinks is required.This method also allows the Spec Sheet to impose Corporate standards and pre-selected features withoutwasting manpower to check their correct usage.The utilization of an electronic spreadsheet such as Excel makes it easy for project documentation to besafely stored, modified, and transmitted with a minimum of manpower. Engineers can generate and processthe documentation without further engineering assistance.Additionally, the inherent calculation features of a spreadsheet are utilized to the maximum in allowing forinvolved calculated information to be self-generated by the spreadsheet automatically. The spreadsheetscan be protected by the used/author for assurance that data will not be revised without prior knowledge.The need to have calculations and related documentation readily available and filed due to legalities (suchas OSHA requirements on safety relief valve calculations and specifications) makes the spreadsheet anatural tool for these requirements.The utilization of Check boxes and Option buttons also give versatility and compactness to these SpecSheets, allowing the user to store more details and data in them. I have endeavored to limit the size of theSpec Sheet to one page and design them around the need for communications of Process data for:1.Documenting the results of calculations and other equipment details;2.Preparing data and information for procurement inquiries (RFQs - Request of Quotes);3.Obtaining Supplier information as related to a specific specification;4.Preparing information that enters the Operations and Maintenance Manuals of a Unit;5.Transmitting information regarding Unit equipment to other parties.These Spec Sheets should be continuously revised and improved as spreadsheet technology improves oris upgraded.I will continue to work on and add additional Spec Sheets to this WorkBook in order to achieve as completea set of Spec Sheets as I can attain within the framework of available time.

&LArt Montemayor&CProcess Specification Sheets&RMarch 12, 2003Rev. 0&CPage &P of &N&RFileName: &FWorkSheet: &AArt's API 650 Storage TankArt's Centrifugal PumpArt's Air-Cooled ExchangerArt's Shell & Tube ExchangerArt's Plate & Frame Heat ExchangerArt's Process VesselArt's Control ValveArt's Centrifugal BlowerArt's Orifice MeterArt's Coriolis MeterArt's Ultrasonic MeterArt's Mass MeterArt's Turbine MeterArt's Vortex MeterArt's Magnetic Meter

Spec Sheet Index 1Index of Process/Mechanical Data Sheet and Specification FormsEquipment Typego-bydraft*complete*debuggedissuable**acceptedAgitator, MixerPressure VesselTower, ColumnMist EliminatorFractionation Tray DataTower Packing DataStorage Tank (API type)Heat Exchanger, TubularHeat Exchanger, Plate & FrameHeat Exchanger, Double-Pipe/Multi-tubeHeat Exchanger, Air-cooledFilter, SeparatorCentrifugePump, CentrifugalPump, Reciprocating/MeteringPump, Rotary (Gear, Screw, Lobe, etc.)Pump, Progressive CavityCompressor, CentrifugalCompressor, ReciprocatingCompressor, Screw-typeFan, BlowerVacuum PumpVacuum Ejector SystemEductor, MixingRotary Feeder ValveWeigh-FeederSolids BlenderIn-line MixerElectric MotorTransformerNoise Compliance Data* in Excel spreadsheet format ** write-protected

&LArt Montemayor&CSpec Sheet Log&RMarch 12, 2003Rev: 0&CPage &P of &N&RFileName: &FWorkSheet: &AP r o c e s s E q u i p m e n t S p e c i f i c a t i o n sAuxiliaries, Other

Spec Sheet Index 2Index of Process/Mechanical Data Sheet and Specification FormsEquipment Typego-bydraft*complete*debuggedissuable**acceptedControl ValvesPressure Relief ValvesOrifice PlatesCentrifugal Pump Calculation SheetPSV Selection Criteria* in Excel spreadsheet format ** write-protected

&LArt Montemayor&CSpec Sheet Log&RMarch 12, 2003Rev: 0&CPage &P of &N&RFileName: &FWorkSheet: &AInstrument SpecificationsData Sheets, Calculations (not specs.)

API 650 Storage TankSTORAGE TANK SPECIFICATIONSheet1of1(English Units)Project No.1952.0001Service :CRUDE OIL StorageEquipment No. :T-400 & T-405ConeYesFlat2Location :Galveston, TexasUnit :KirwinDesign Engineer :Art MontemayorDomeNoSloped3Manufacturer :Model :Mfr Ref. No. :No. Req'd :TwoFloatingCone4P&ID No.PID115-EPF-01-112A1Plot Plan No. :Other Ref. Dwg No. :567891011121350.00Ft141532.00Ft161718192021222324Shell Diameter :50.00FeetShell Height :32.00FeetNominal Volume :11,191BarrelsFlatGallons25Roof Type :ConeBottom Floor Type:SlopedSlopedBarrels26OPERATING/DESIGN DATANOZZLES/CONNECTIONSCone27Fluid Stored :CRUDE OILSp. Gr. :0.7900MarkServiceQtySizeRatingFace125#R. F.28This Tank Service is considered:CyclicARoof Manway224"150#F. F.Cyclic150#F. F.29Vapor Pressure @ Max. Operating Temperature5.5psiaEShell Manway224"125#R. F.LethalL. J.30Flash Point (Closed Cup) :FOperatingDesignFFlush Cleanout MW148"x48"125#R. F.OtherAPI31Negative Pressureoz/in.20.000.50GStilling Vent16"125#F. F.in. WC32Positive Pressurepsig1.002.00HTemperature Indicator11"150#L. J.oz/in.233(Hydro)test Pressure expressed in Psig----IOutlet Nozzle18"150#APIpsig34Minimum Fluid TemperatureF-25JFill Nozzle110"150#L. J.35Maximum Fluid TemperatureF200KMixer Manway130"150#F. F.36Emergency Vacuum Design ?YesSet @0.0.3oz/in.2LWater Draw Nozzle14"150#R. F.37METALLURGYMTop Center Vent18"150#API38ComponentMaterialCA, in.RemarksN1Sample Tap13/4"150#R. F.39Shell & Bottom573700.1250NormalizedN2Sample Tap13/4"150#F. F.40Roof516 Grade 550.1250NormalizedPRoof Nozzle14"150#L. J.41Lining/CoatingDSpare12"150#APIHeater131 Grades A-B-CS0.0312542150#APICooler131 Grade EH-360.0625043Stress Relieve ?Yesfor:150#APIMixer, Agitator283 Grade C0.0937544CONSTRUCTION/FABRICATIONBaffles285 Grade C0.1250045Code (as appl.):API 650 LATEST EDITIONInternals (attach separate sheet, as req'd):Others:Roof SupportA3646Design Specifications:SumpOthers:442 Grade 5547Tank Insulation ?NoThickness :in.Seismic Zone3Design Wind Velocity100mphHot442 Grade 6048Insulation Type:HotRadiograph85%Inspection Req'd ?YesCold516 Grade 5549Fireproofing ?YesPaint Spec.EmptyTank WeightlbFull of WaterlbPers. Protect.516 Grade 6050RemarksAnti-Sweat516 Grade 65511. Items marked with an asterisk (*) to be completed by Vendor/Fabricator.516 Grade 70522. Fixed cone roof with internal floating roof.5371Approvals5372RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.573580For InquiryArtM5736557370633C - D662B662C678A678B737B

Montemayor, Inc.604530Rev. No.Comment: Indicate special conditions and operations during startups, shutdowns, regenerations, vibrations, etc. which may affect mechanical design inputComment: Is a vacuum relief required for certain emergency scenarios? If so, give the set relief pressure.48" X 48"FLUSH CLEANOUTFAMPGKDELEHN2N1JI8'-0" S-SMin.4'-0" ODAL2L1CH1H2BComment:Indicate any Client or specifically indicated tank design specifications that must be considered in the fabrication.Note: This information must be filled in by the Tank Fabricator or VendorNote: This information must be filled in by the Tank Fabricator or VendorNote: This information must be filled in by the Tank Fabricator or VendorNote: This information must be filled in by the Tank Fabricator or VendorNote: This information must be filled in by the Tank Fabricator or Vendor

Centrifugal PumpCENTRIFUGAL PUMP SPECIFICATIONSheet1of1(English Units)Montemayor CorporationProject No.1234567$1ServiceCrab Juice Transfer PumpEquipment No.P-37$2LocationGalveston, TexasUnitBalinese RoomP.O. No.$3Manufacturer*Model*Mfr Ref. No.*No. Req'dOne$4P&ID No.PID-01-0000Plot Plan No.PLT-03-0000Specification Engr:A. Montemayor$5OPERATING CONDITIONS, EACH PUMPPERFORMANCE$6Liquid PumpedCrab JuiceManufacturer's Proposal Curve No.*$7Capacity @ PT, Normal400gpmRated500gpmRPM*No. Stages*Hydr. Eff'y*%$8Suction Pressure14.7psig (Norm.)16.7psig (Max.)Rated Brake Power*HP@ Max. Impeller*HP$9Disch. Pressure77.7psig (Norm.)90psig (Max.)NPSH Req'd @ Impeller CL*ft@ TOC*ft$10Differential Pressure63.0psiDiff. Head (TDH)170.4098360656ftMin. Flow Req'd*gpmCont.Thermal$11Temperature, Normal120FMax.190FSuction Specific Speed*fps$12Specific Gravity0.854@ PT0.839@ Max. Temp.Rotation (viewed from Cplg end)CWCCW$13Vapor Press. @ PT6.87psiaNPSH Available14ftSITE CONDITIONS$14Viscosity @ PTcPcStSSULocationIndoorsXOutdoorsElev.97ft ASL$15Corrosion/Erosion Caused By:Ambient Temp.100F Max.10F Min.$16Solids PresentConcentration%CW Supplypsig @F Max.$17Size DistributionCW Returnpsig, Min. @F Max.$18Liquid isFlammableToxicOther:Electrical Power220/440v3Ph60Hz$19ContainsChloridesH2SOther:Area Classification:ClassIIDiv.AGroup1$20CONSTRUCTION$21NozzlesSizeRatingFacingLocationMaterials$22Suction1"150#FFCase/Trim (API Class)$23Discharge3"150#RFCasingCorr. Allow.in.$24Int'l Ctg/LiningGland$25Case Mount'gCLFootBrcktVert. (Type)ImpellerWear Rings$26SplitAxialRadialVoluteSingleRadialDiffuserShaftSleeve(s)$27Case MAWP*psig @*FHydrotest @*psigBaseplateDrip Pan$28ConnectionsVentDrainGaugeSteam JktEpoxy Grout, etc.$29ImpellerOpenClosedSpecialInternal Wear Parts$30Diameter:Rated*in.Max.*in.Min.*in.Wear RingsCaseImpeller$31MountBetw. Brgs.OverhungTypeDiameter*in.; Clearance*in.$32BearingsRadialThrustInt'stge Bush'gs, Diam.*in.; Cl'rnce*in.$33LubeRing OilFloodOil MistFlingerPressureWeights and Dimensions$34Cplg. MfrModelApprox. Wt., Pump & Base*lb$35Driver Half Mounted ByPump MfrDriver MfrMotor Wt.*lbTurbine Wt.lb$36SealMech.PackingAuxiliaryMech.PackingBaseplate Dimensions (in.)*$37Seal Mfr.TypeModelBaseplate No.*ANSIAPI$38Mfr CodeAPI CodeApplicable Specifications$39Jacketed BoxOtherAPI610$40Gland TapQuenchDrainFlushVentANSIB73.1B73.2$41Auxiliary PipingCustomer Specs:$42CW PlanTotal CW Req'dgpmSight FI ?No$43CW Piping Mat'ls :Stainless Steelfortubing & pipingInspection and Tests$44Packing Cooling Injectiongpm @psigShop InspectionReq'd$45API Seal Flush PlanSSCSTubingPipeHydrostatic TestReq'dWitness$46SF Fluid :gpm @psigBoxpsigPerformance TestReq'dWitness$47Auxiliary Seal PlanSSCSTubingPipeNPSH TestReq'dWitness$48Auxiliary Seal Flush/Quench FluidInternal Insp'n After TestReq'dWitness$49Seal Flush PipingThreadedSocket WeldFlangedOther:Req'dWitness$50Remarks1. Items marked with an asterisk (*) to be completed by Vendor.$512. See Motor Data, Sheet 2 of 2.$52RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.09-Oct-02For InquiryABCDEFXYZFull ScaleNEMA-4X4 to 20 mAlbIA1None"Liqgpmlb/ftReadingNEMA-7PulsekgIIB2H"Vapgphlb/galNEMA-4DigitalUS galIIICC1"Gaslb/hg/ccNEMA-12ftC&DPP1"2-Phlb/minft/lbDAS2"ft/seccc/g"125#WNFFE2"ft/minm/kg"150#SORFF3"ft/h1"300#SWLJG1"600#ThrdRTJcP2"900#SSU3"1200#CoppercSt4"1500#Carbon Steel6"Stainless SteelYes8"No10"tubing12"pipetubing & pipingFluid Density @Specific Volume @

D R A F TRev. No.M

Air-Cooled ExchangerAIR-COOLED EXCHANGER SPECIFICATIONSheet1of1(English Units)CorporationProject No.12345671ServiceProcess Vapor CondenserEquipment No.2LocationCedar Rapids, IowaUnitFurfuralP.O. No.3Manufacturer*Model*Mfr Ref. No.*No. Req'dOne4SizeTypeDraft Type:ForcedNo. of Bays5Heat Duty100,000,000Btu/hEffective MTD150FSurface/Unit, Finnedft2; Bare Tubeft26Transfer Rate, Ext'd Surface :250Btu/ft2hFBare Tube - Service :Btu/ft2hFClean :Btu/ft2hF7P&ID No.Plot Plan No.Other Ref. Dwg No.8PERFORMANCE DATA - TUBE SIDE9Fluid NameLethal Service?NoInletOutlet10Total Fluid Enteringlb/hSpecific Heat, LiquidBtu/lbF11InOutSpecific Heat, VaporBtu/lbF12TemperatureFThermal Cond., Liq.Btu/fthF13Vaporlb/hThermal Cond., Vap.Btu/fthF14Mol. Wt.Viscosity, LiquidcP15Liquidlb/hViscosity, VaporcP16Non-Condensableslb/hLatent HeatBtu/lb17Mol. Wt.Pour/Freeze PointF18Steamlb/hDew/Bubble PointF19Waterlb/hOperating Pressure, Inletpsig20Fluid Vaporized or Condensedlb/hVelocityXMax.Min.fps21Steam Condensedlb/hDP, Clean (Allow./Calc.)psi22Liquid Specific GravityMin. Fouling Resistanceft2hF/Btu23PERFORMANCE DATA - AIR SIDECarbon Steel24Air Quantity, Totallb/hscfmPlant Altitudeft Above Sea Level304 Stainless Steel25Air Quantity per Fanlb/hscfmTemperature In (Design Dry Bulb)F316 Stainless Steel26VelocityXMax.Min.Temperature OutFAluminum27Face Velocitystd fpsMass Velocity (Net Free Area)lb/hft2Min. Design Ambient Temp.FCopper28CONSTRUCTION AND MATERIALS29Design PressurepsigTest PressurepsigDesign TemperatureFSeamless30SectionHeaderTubesWelded31SizeTypeMaterial :316 Stainless Steel32No. per BayTube RowsMaterial316 Stainless SteelFabrication Type :Seamless3" 150# RF6" 125# FF1/4"27Rolled, unbeadedCircumferential33Arrangement:TwoNo. of PassesSlopein./ftOD1-1/2"in.Gage, B.W.G. :183" 150# RF6" 125# FF3/8"24Rolled, beadedLow-Finned34Bundles inSeriesParallelPlug MaterialNo./Bundle :50Length :40ft1/2"22Welded, rolledMedium-Finned35Bays inSeriesParallelGasket MaterialPitch :1.25in.Pattern :Rot. Square5/8"20Welded36Bundle Frame:Corrosion Allowance0.125in.Tube Sheet Joint :Welded3/4"1837MiscellaneousConnectionsNo.SizeRatingFacingFins7/8"16Triangular38Structural MountingInletType :Low-Finned1"14Rot. Triangular39OutletMaterial :1-1/4"12Square40Surface PreparationTemperatureODin.Stock Thk.in.1-1/2"Rot. Square41LouversAutoManualPressureFins/inchDes. Temp.F2"42Code Requirements:ASME Sec. VIII, Para. 1 (1992)43MECHANICAL EQUIPMENT44FanDriverSpeed ReducerSteam Turbbine45Mfr/Model No.TypeType :Gear boxMulti-pole motor46No./BayHP/FanMfr/Model No.Mfr/Model No.Gear box47DiameterftPitch AngleNo./BayNo./BayVari-speed motor48Blade Mat'lRPMHP/DriverRPMAGMA RatingHP49Tip SpeedfpsEnclosureRatio :StructureNone50Pitch Adj.%Auto-Variable%PowervPhHzSupport :StructurePedestalInternal51Steam Coil?YesNoAir Recirculation Control :External - Over SideExternal - Over Side52Air Failure Control Action: Fan PitchMin.Max.LockupLouversOpenCloseLockup0.031External - Over End53Vibration Switches Req'd?YesNoChemical Cleaning, etc.0.06354Plot Area*Weight - Bundle*lbShipping Weight*lb0.09455Remarks1. Items marked with an asterisk (*) to be completed by Vendor.0.125560.156570.1880.219RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.0.250027-Nov-02For InquiryABCDEFXYZFull ScaleNEMA-4X4 to 20 mAlbIA1"Liqgpmlb/ft1ReadingNEMA-7PulsekgIIB2"Vapgphlb/gal2NEMA-4DigitalUS galIIIC1"Gaslb/hg/cc3YesNEMA-12ftC&D1"2-Phlb/minft/lb4NoD2"ft/seccc/g5"125#WNFFE2"ft/minm/kg6"150#SORFF3"ft/h71"300#SWLJG81"600#ThrdRTJNonecP92"900#NoneHotSSU103"1200#Carbon Steel0.03125ColdcSt114"1500#Stnless Steel0.06250Personnel Protection126"0.12500Heat Conservation138"Gross0.250001410"EffectiveSingle1512"Series16Parallel17Fluid Density @Specific Volume @

Rev. No.Montemayor

Shell & Tube XchangerSHELL & TUBE HEAT EXCHANGER SPECIFICATIONSheet1of1(English Units)CorporationProject No.1Service:Lean MEA Solution CoolerEquipment No.2Site:Km 8, Avda. Venezuela; Lima, PeruUnitGerman HuanucoP.O. No.3Manufacturer:*Model*Mfr Ref. No.*No. Req'd4TEMA Size, Type:Horiz.Vert.Connected inSeriesParallel5Surface/Unit:*ft2GrossEff.Shells/UnitOneSurface/Shell*ft2GrossEff.6P&ID No.:Plot Plan No.Other Ref. Dwg No.7PERFORMANCE OF ONE UNIT8Fluid AllocationSHELL SIDETUBE SIDE9Fluid Circulated10Total Fluid Enteringlb/h11Vapor (In/Out)lb/h250012Liquidlb/h13Steamlb/h250114Non-Condensableslb/h42,56715Fluid Vaporized or Condensedlb/h16Steam Condensedlb/h17TemperatureF18Density, Specific Gravity19ViscositycP20Vapor Molecular Weight21Specific HeatBtu/lbF22Thermal ConductivityBtu/hftF23Latent HeatBtu/lb24Operating Pressure, Inletpsig25VelocityMax.Min.fps26Pressure Drop, Clean (Allow./Calc.)psi27Fouling Resistanceft2hF/Btu28Heat ExchangedBtu/hLog MTD (Uncorrected)FLog MTD (Corrected)*F29Transfer Rate, Service*Btu/ft2hF .Transfer Rate, Clean*Btu/ft2hF .30CONSTRUCTION AND MATERIALS31SHELL SIDETUBE SIDESketch (Bundle, Nozzle Orientation)32Design Pressurepsig33Test Pressurepsig34Design TemperatureF35Number of Passes per Shell36In37Out38Intermediate39Tubes:TypeNumber*OD0.75in.16BWGorin.XMin.Av. Wall40Tube Lengthin.Tube Pitch0.9375in.Flow Pattern (circle one)41Shell:ID*in.OD*in.Tube-to-Tubesheet Joint :Rolled and welded42Baffles - Cross:Type*Spacing*in.*% Cut onXDiam.Area43Baffles - Long:Perm.RemovableSeal Type:Bypass Seal:44rv2:Inlet Nozzle*lb/ftsecBundle Entrance*lb/ftsecBundle Exit*lb/ftsec45Expansion Joint?YesXNoType:Impingement Protection?XYesNo46PARTMATERIALTHK, in.C.A., in.PARTMATERIALTHK, in.C.A., in.47TubesStnless Steel14 BWG Min0.0625Floating TubesheetCarbon Steel*None48ShellCarbon Steel0.0625Fixed TubesheetCarbon Steel*None49Shell CoverCarbon SteelNoneTube SupportsCarbon Steel*0.12550ChannelCarbon SteelNoneCross BafflesStnless Steel*0.12551Channel CoverCarbon SteelNoneLong BaffleCarbon Steel*None52Fltg Head CoverCarbon SteelNoneGasketsCarbon SteelNone53 Stress Relieved (Mark "SR') and/or Radiographed (Mark 'XR') PartsUser Spec.:54Code Requirements:ASME Sec. VIII, Para. 1 (1992)Stamp?XYesNoTEMA Class:55Weights: Shell*lbFilled with Water*lbBundle*lb56Remarks:1. Items marked with an asterisk (*) to be completed by Vendor.5758RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.0For PurchaseFull ScaleNEMA-4X4 to 20 mAlbIA1"Liqgpmlb/ftReadingNEMA-7PulsekgIIB2"Vapgphlb/gal1NEMA-4DigitalUS galIIIC1"Gaslb/hg/cc2YesNEMA-12ftC&D1"2-Phlb/minft/lb3NoD2"ft/seccc/g4"125#WNFFE2"ft/minm/kg5"150#SORFF3"ft/h61"300#SWLJG71"600#ThrdRTJNonecP82"900#NoneCarbon SteelHotSSU93"1200#0.03125Stnless SteelColdcSt104"1500#0.0625BronzePersonnel Protection116"0.125CopperHeat Conservation128"Gross0.25Aluminum1310"EffectiveSingle1412"Series15Parallel16Fluid Density @16 BWG Min17Specific Volume @14 BWG Min13 BWG Min12 BWG Min11 BWG Min10 BWG Min9 BWG Min8 BWG Min

60904530ConnectionsSize & Rating6090453060904530Rev. No.HUNTSMANHuntsman CorporationMontemayor

Plate & Frame XchangerPLATE & FRAME HEAT EXCHANGER SPECIFICATIONSheet1of1(English Units)CorporationProject No.12345671Service:Cooling Water ExchangerEquipment No.2LocationBarbados, W. I.UnitTuffy ForbesP.O. No.3Manufacturer*Model*Mfr Ref. No.*No. Req'dOne4Size, Type* - *Frames/UnitOneConnected inSingle5Surface/Unit*ft2EffectiveSurface/Frame*ft2Gross6P&ID No.Plot Plan No.Other Ref. Dwg No.7PERFORMANCE OF ONE UNIT8Fluid AllocationHOT SIDECOLD SIDE9Fluid CirculatedCooling Water10Total Fluid Enteringlb/h31,500206,48311Vapor (In/Out)lb/h----------------12Liquidlb/h31,50031,500206,483206,48313Steamlb/h----------------14Non-Condensableslb/h----------------15Fluid Vaporized or Condensedlb/h----------------16Steam Condensedlb/h----------------17TemperatureF2351209010518Density, Specific Gravity0.9070.9290.9950.99219ViscositycP0.5413.70.760.6520Vapor Molecular Weight----------------21Specific HeatBtu/lbF0.8670.8431.01.022Thermal ConductivityBtu/hftF0.1780.1600.3580.36523Latent HeatBtu/lb--------24Operating Pressure, Inletpsig756025VelocityXMax.Min.fps8.08.026Pressure Drop, Clean (Allow./Calc.)psi10*10*27Fouling Resistanceft2hF/Btu0.0010.00328Heat Exchanged3,097,238Btu/hLog MTD (Uncorrected)157.0FLog MTD (Corrected)*F29Transfer Rate, Service*Btu/ft2hFTransfer Rate, Clean*Btu/ft2hF30CONSTRUCTION AND MATERIALS31AllocationHOT SIDECOLD SIDESketch (Frame, Nozzle Orientation)32Design Pressurepsig15012533Test PressurepsigCodeCode34Design TemperatureF30030035Number of Passes per FrameTwo*36Corrosion Allowancein.0.0625None37In3" 150# RF6" 125# FF38Out3" 150# RF6" 125# FF39Intermediate--------40rv2, Inlet/Outletlb/fts41Impingement Protection?Yes42No. of PlatesFrame Capacity (Max. No. of Plates)43PARTMATERIALTHK, in.C.A., in.PARTMATERIALTHK, in.C.A., in.44PlatesStnless Steel16 BWG min.0.03125ConnectionsStnless Steel0.0312545Plate GasketsCarbon Steel*0.03125FrameCarbon Steel0.0312546End CoverCarbon Steel*0.03125Carrying BarCarbon Steel0.0312547Carbon Steel0.03125Carbon Steel0.0312548 Stress Relieved (Mark "SR') and/or Radiographed (Mark 'XR') Parts49OSHA Type Protective Shroud?YesMaterial:Carbon SteelInsulation:Heat Conservation50Cleaning:Painting:51Code Requirements:ASME Sec. VIII, Para. 1 (1992)Stamp?Yes52Client Spec.:Weights: Empty Frame*lbFilled with Water*lb53Remarks1. Items marked with an asterisk (*) to be completed by Vendor.5455RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.021-Aug-98For InquiryArtMDEFXYZ12Full ScaleNEMA-4X4 to 20 mAlbIA1"Liqgpmlb/ft3ReadingNEMA-7PulsekgIIB2"Vapgphlb/gal4NEMA-4DigitalUS galIIIC1"Gaslb/hg/cc5YesNEMA-12ftC&D1"2-Phlb/minft/lb6NoD2"ft/seccc/g7"125#WNFFE2"ft/minm/kg8"150#SORFF3"ft/h91"300#SWLJG101"600#ThrdRTJNonecP112"900#NoneHotSSU123"1200#Carbon Steel0.03125ColdcSt134"1500#Stnless Steel0.06250Personnel Protection146"0.12500Heat Conservation158"Gross0.250001610"EffectiveSingle1712"SeriesParallelFluid Density @Specific Volume @

ConnectionsSize & RatingRev. No.Montemayor

Process VesselPROCESS VESSEL SPECIFICATIONSheet1of1(English Units)CorporationProject No.1Service:Filter Feed TankEquipment No.V - 412Site:Belle Glade, FloridaUnitFurfuralP.O. No.3Manufacturer*Model*Mfr Ref. No.*No. Req'dOne4P&ID No.PID-01-2084Plot Plan No.PLT-03-2049Other Ref. Dwg No.Note 25PROCESS (OPERATING) DATAVESSEL SKETCH6PositionHorizontalXVerticalTopBottom7Shell DiameterIDXODft-in.8'-0"8'-0"8Shell LengthTL-TLXS-Sft-in.9'-6"9'-6"9Internal Pressurepsig0010Temperature (Min/Norm/Max)FAmb.Amb.11Nominal Volume3,000galTotal Volume4,900gal12Fluid ContainedAqueous Amine Sol'nsSpecific Gravity1.0Note 413Vapor Pressure @ Max. Ambient Temperature0.95psia14Process Contaminants15Service isXCyclicLethalOther16METALLURGY17ComponentMaterialCA, in.Remarks18Shell & Heads304SS0.062519InternalsXWeld-in304SS0.0625Baffles, Dip Tubes,20Remov.304SSNoneVortex Breaker21SupportsCarbon SteelNone2223MECHANICAL DESIGN24Des. Press. @ Top5psigExt. Des. Press.N/Apsig25System PSV Set @psig; located @top of vessel26Des. Temperature100FMinimum Temp.-20F27Vessel Support(s)SkirtXLegsLugsSaddles28Height (Btm of Horiz. or BTL of Vert.)ft Above Grade29FireproofingOther30XInsulationXHCPPThicknessin.31Design Codes:ASME Section VIII (1992); no stamp req'd32Post-Weld Heat Treatment for:33XRadiograph85%Inspection Req'd?XYesNo34NOZZLES/CONNECTIONS35MarkServiceQtySizeRatingFacing36ALiquid Inlet w/Dip Tube12"150 lbRF37BLiquid Inlet w/Dip Tube11"300 lbLJ38CN2 Pad11"300 lbRF39DVent11"300 lbRF40EFill Connection (Note 4)11"300 lbRF41FAgit'r Opn'g w/Reinf. Pad (Note 3)11"300 lbRFSpecify Operating Levels Above Btm or BTL42GManhole w/Davit11"300 lbRF43HRelief Valve16"300 lbRFLCH44JLevel Indicator (DP Cell)12"300 lbLJHLL45KLevel Indicator (Equal. Conn.)12"300 lbRFLAH46LLiquid Inlet14"300 lbLJNLL47MTemp. Indicator11"300 lbRFLAL48NPump Suction13"300 lbRFLLL49OLight (Future)13"300 lbRFLCL50PSight Glass (Future)14"300 lbRF51QSpare14"300 lbRFWeights: Vessel Only*lbInternals*lb521"300 lbRFOperating WeightlbFull of Water*lb53Remarks:1. Items marked with an asterisk (*) to be completed by Vendor.542. Ref. set of detail dwgs for existing V - 41 (circa 1969). 3. Agitator supplied by Owner; conn. details on ref. dwgs.554. Nozzle 'E': Tube Turn 12" T-Bolt hinged closure.RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.030-Sep-00For InquiryArtMDEFXYZ1Full ScaleNEMA-4X4 to 20 mAlbIA1"Liqgpmlb/ft2ReadingNEMA-7PulsekgIIB2"Vapgphlb/gal3NEMA-4DigitalUS galIIIC1"Gaslb/hg/cc4YesNEMA-12ftC&D1"2-Phlb/minft/lb5NoD2"ft/seccc/g6"125 lbWNFFE2"ft/minm/kg7"150 lbSORFF3"ft/h81"300 lbSWLJG91"600 lbThrdRTJNonecP102"900 lbNoneHotSSU113"1200 lbCarbon Steel0.03125ColdcSt124"1500 lbStnless Steel0.06250Personnel Protection136"Cast Iron0.12500Heat Conservation148"0.250001510"Single1612"Series1714"ParallelFluid Density @Specific Volume @GrossEffective

KMontemayorRev. No.Standard Displacer Ranges are:14"24"32"45"Special Design Over 45"9'-6" S-S8'-0" OD11HAOPBDFCELJMNG6'-11"Vortex Breaker4 Legs (min.)Baffle(4 req'd)Dip Tube (2 req'd, Nozzles 'A' & 'B')Q

Control ValveINSTRUMENT SPECIFICATION - CONTROL VALVESSheet1of1Rev. No.(English Units)Montemayor CorporationProject No.19371LocationPerros Bravos, N. L.UnitTequila ConmemorativaP.O. No.Estimate Inquiry$2Tag NumberPCV G 1stPCV G 2nd$3P&ID NumberF-01-2411F-01-2411$4Line Number2" 300AA-5238-4571" 1500AA-5238-460$5Assoc. Equip./ServiceC - G - 02 & C - G - 03C - G - 02 & C - G - 03$6SERVICE CONDITIONS$7Fluid NamePhase(s)Flow UnitsRecycle Gas2-PhSCFMRecycle GasVapSCFMLiqgpm$8Temp., Min.OperatingMax.oF150290350150180350$9Liq. SG @ 60 oFSG @ Op. TVapor MWN.A.4.268N.A.4.268$10Critical Press., PCOp'g Viscosity, mN.A.psia0.013cPN.A.psia0.012cPpsiacP$11Flow, Min.Norm.Max.Capacity200265350350200265350350$12Upstream Pressure @ Flowpsig5005005005001000100010001000$13Downstream Pressure @ Flowpsig495495495495995995995995$14Fluid Density at Inlet T&P, Flowlb/ft30.27080291970.6081967213$15Valve CV @ Flow (Calculated)$16Maximum Closed DPFail Position7psiClosed7.0psiClosedpsiOpen$17VALVE SELECTION, FLOW CHARACTERISTICS$18ManufacturerModelValtekValtek$19Trim CharacteristicFlow DirectionLinearUnderEqual %UnderMod. ParabolicOver$20Bal./Unbal.Body SizePort SizeUnbal.in.in.Bal.in.in.Bal.in.in.$21Trim SizeStrokein.in.in.in.in.in.$22Valve Percent Open25%50%90%100%$23Actual CV @ % Open$24End Connections (Size, Rating, Facing)2"300#RF1"1500#RF1"150#Ring-joint$25Bonnet TypeNumber of PortsExtendedTwoStandardTwoCooling FinFour$26Lube & Isolating Valve (check)Lube$27Packing TypePacking MaterialMolded V-RingGraphite Impreg.Molded V-RingGraphite Impreg.BraidedGraphite$28MATERIALS$29Bonnet/BodyLiner316ss316ss$30Plug/Ball/DiskSeat/Seat Ring316ss316ss$31Cage/GuideStem$32ACTUATOR$33TypeDiaphragm, pneumaticDiaphragm, pneumaticHydraulic PistonDate12-Mar-00$34ManufacturerModel$35SizeEff. Area, in.2ServiceModulatingModulatingOn-off$36Spring ActionHandwheel Pos., Orient.OpenTop, Left-handCloseTop, Right-handOpenSide, Left-hand$37Max. Allow. Press.Min. Req'd Press.psigpsigpsigpsigpsigpsigRev.0$38Avail. Air Supply Press., Max.Min.psigpsigpsigpsigpsigpsig$39Travel starts @Rated Travel @psigpsigpsigpsigpsigpsigInstrument Form No.Automatic Valves$40POSITIONER$41TypeSingle-actingDouble-actingNone$42ManufacturerModel$43Signal incr. output to ActuatorCamIncreasesLinearDecreasesSquare RootIncreasesSquare Root$44Check OtherGaugesBy-passGaugesBy-passGaugesBy-pass$45SWITCHES$46TypeQuantityProximityMechanicalPneumatic$47ManufacturerModel$48Contacts/RatingActuation Points$49AIR SET$50ManufacturerModel$51Set Press.Other (check)psigFilterGaugepsigFilterGaugepsigFilterGauge$52SPECIALS/ACCESSORIES/TESTS$53Electrical Area Classification (if appl.)ClassIGroupADiv.1ClassIIGroupCDiv.1ClassIIIGroupBDiv.2$54Hydro PressureANSI/FCI Leak ClasspsigClass IpsigClass IIpsigClass III$55Other$56RemarksThe Recycle Gas working fluid is a binary mixture of 15% vol NH3 + 85% vol H2 (60 % wt NH3 + 40 % wt H2)$57Two control valves are required for each of the two services.$58RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr."125#RFgpmOn-offIncreasesDiaphragm, pneumatic0%"150#FFLiqgphModulatingDecreasesHydraulic Piston5%"300#Ring-jointVaplb/hPneumatic Rotary Vane10%1"600#Butt-weld2-PhSCFMNoneLinear15%1"900#Socket-weldSCFHOpenSquare RootNone20%2"1200#CloseSingle-acting25%3"1500#OpenDouble-acting30%4"ClosedNone35%6"TwoLastTop, Left-handMechanicalClass I40%8"ThreeTop, Right-handProximityClass II45%10"FourSide, Left-handPneumaticClass III50%12"Side, Right-handClass IV55%18"BraidedGraphiteClass V60%20"Molded V-RingGraphite Impreg.LinearOverBal.65%24"Lam. FilamentTFEEqual %UnderUnbal.70%Press./Vac.Mod. Parabolic75%StandardQuick-opening80%Cooling FinIA185%ExtendedIIB290%IIIC95%C&D100%DEFG

Max. flow required by ProcessFlow thru valve at 100% openCompare these CV's with calculated CV's(Line 15) to ascertain suitability of selectedvalve characteristics for specified service.Specify a range that brackets expected max. andmin. flows; normal values are 10%, 30%, 70%, 90%.M

Centrifugal BlowerCENTRIFUGAL FAN, BLOWER SPECIFICATIONSheet1of2(English Units)CorporationProject No.12345671ServicePolitical Hot AirEquipment No.CF - 1002Site:Kingston, JamaicaUnitAlf NewtonP.O. No.3Manufacturer*Model*Mfr Ref. No.*No. Req'dOne4P&ID No.PID-01-0000Plot Plan No.PLT-03-0000Other Ref. Dwg No.5OPERATING CONDITIONSPERFORMANCE6Gas Handled :Manufacturer's Proposal Curve No.7Service isContinuousIntermittent forhrs/dayTypeCentrifugalAxialVane8Capacity, Normallb/h orSCFMRPM3600No. Stages1Efficiency%9Capacity, Designlb/h orSCFMInlet Size/RatingTopBottomSide10Inlet Pressurein. WCInlet Temp.FDisch. Size/RatingTopBottomSide11Disch. Pressurein. WCDisch. Temp.FCase Design Press.psig;Design Temp.F12Gas Mol. Wt.Compr. (Z) at InletRelief Valve No.Located @13Cp/Cv at InletBy MfrBy CustomerSet @14Corrosion/Erosion Caused ByRotation (viewed from Cplg end)CWCCW15Dust Present?NoYes ; NamePacking, Type:No. of Rings16Concentrationgr/ft3Size RangemMech. Seal, Type:Mfr by17Solids areAbrasiveExplosiveSticky18Other (specify)Driver19SITE CONDITIONSType:Mfr toFurnishMount20LocationIndoorsxOutdoorsElev.97ft ASLDirectIndirect:V-BeltGear21Ambient Temp.F Max.F Min.SingleVariable SpeedHPRPM22Max. Relative HumidityOthervPhHzEnclosure23Electrical Area ClassificationNEMAService Factor2425MECHANICAL DETAILS AND MATERIALS OF CONSTRUCTION26CaseRotor(s)ShaftBearingsGearsV-Belt Drive27Cast IronAluminumSteelBallSteelV-Belt28SteelAlloy Steel316SSSleeveStatic Conductor29AluminumCast SteelRollerGuard30316SS316SSSparkproof3132Coupling(s)Bearing LubricationShaft SleeveLantern RingPacking GlandWater Cooling33FlexibleOilStellitedBronzeBronzeSeal34Fast/FalkGrease420SSCast IronCast IronBearing35GuardNoneSteelSteelNone36SparkproofNone3738Common Baseplate and Driver by Mfr?YesNoBaseplate Mat'lCast IronFabricated Steel39Baseplate DimensionsApprox. Wt., Blower & BaselbDriver Wt.lb40PROCESS CONTROL SKETCH (Incl. Scope of Supply414243444546474849505152RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.027-Dec-96For InquiryABCDEFXYZLubeRing OilFloodOil MistFlingerPressWeights and DimensionsCplg. MfrModelApprox. Wt., Pump & BaselbDriver Half Mounted ByPump MfrDriver MfrMotor Wt.lbTurbine Wt.lbSealMech.PackingAuxiliaryMech.PackingBaseplate Dimensions (in.)1Seal Mfr.TypeModelBaseplate No.ANSIAPI2Mfr CodeAPI CodeApplicable Specifications3Jacketed BoxOtherAPI6104Gland TapQuenchDrainFlushVentANSIB73.1B73.25Auxiliary PipingUser's Spec.6CW PlanTotal CW Req'dgpmSight FI7CW Piping Mat'lsCuSSCSTubingPipeInspection and Tests8Packing Cooling Injectiongpm @psigShop InspectionReq'd9Seal Flush Piping PlanSSCSTubingPipeHydrostatic TestReq'dWitness10SF Fluidgpm @psigBoxpsigPerformance TestReq'dWitness11Auxiliary Seal PlanSSCSTubingPipeNPSH TestReq'dWitness12Auxiliary Seal Flush/Quench FluidInternal Insp'n After TestReq'dWitness13Seal Flush PipingThreadedSocket WeldFlangedOther:Req'dWitness14151617

MontemayorRev. No.

Orifice MeterMontemayorFLOWMETER SPECIFICATION, ORIFICE PLATESheetofRev. No.(English Units)CorporationProject No.1LocationEl Gallinero, Nuevo LeonUnitHuevos RanciosP.O. No.*$2Tag Number$3P&ID Number$4Line NumberPipe Size/Schedule Table$5Service or Associated EquipmentNom.Schedule$6SERVICE CONDITIONSDia.1010S20405S80160$7Fluid Name and Phase (l, v, g or 2)1"N/A1.097N/A1.0491.1850.9570.815$8Flow, Min.NominalMax.unitsgpmlb/min1"N/A1.682N/A1.6101.7701.5001.338$9Temp., Min.NominalMax.FFF2"N/A2.157N/A2.0672.2451.9391.689$10Press., Min.NominalMax.psigpsigpsig3"N/A3.260N/A3.0683.3342.9002.624$11Mol. Wt.CP/CVCompress. Factor4"N/A4.260N/A4.0264.3343.8263.438$12Fluid Density @ STP@ Op'g T&P6"N/A6.357N/A6.0656.4075.7615.189$13Viscosity, Min.NominalMax.cPSSU8"N/A8.3298.1257.9818.4077.6256.813$14Quality (%) or Superheat (F)1Dia.Sch.Col.$15Air or Gas Bubbles; NameNYNYNY0.000$16Size Range% by volume2Dia.Sch.Col.$17Suspended Solids; NameNYNYNY0.000$18Size Range% by weight3Dia.Sch.Col.$19Pipe DiameterScheduleMaterial0.000$20Liner MaterialInsulation Thk, Type$21ORIFICE PLATE AND FLANGE SPECIFICATIONS$22PlateManufacturerModel$23Plate TypeMaterial$24Bore Sized forDesign Std$25Bore Diam., dThicknessin.in.in.in.in.in.$26DP @ Max. Flow: Allow./Calc.Units*$27Pipe ID, Db = d/D0.0000.0000.0000.0000.00000.0000.0000.0000.0000.00000.0000.0000.0000.0000.0000$28FlangesFlanges & Taps: Supply by$29Flange TypeRatingMaterial$30Tap SizeLocation$31Ring Type (if appl.)MaterialDate5-May-99$32Vent, Drain, Other?Vent (top)Drain (btm)Vent (top)Drain (btm)Vent (top)Drain (btm)$33$34METER SELECTION, MEASUREMENT PARAMETERS$35ManufacturerModelRev.0$36Meter TypeSeal Sp. Gr. @ 60F$37Range: Diff. (Dry)StaticUnitsInstrument Form No.$38Chart or Scale RangeChart Multiplier$39Other:$40INSTALLATION, INTERFACE SPECIFICATIONS$41Area ClassificationClassGrDivClassGrDivClassGrDiv$42Output UnitsHousing Requirements$43Switches/AlarmsHiLoFaultHiLoFaultHiLoFault$44Other:Other:Other:$45Totalizer (check)Min. RangeUnits$46Cable Distance (Transducer to Console)feetOther:feetOther:feet$47Special Requirements:0 to0 to$48$49Remarks1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.$50$51RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.Full ScaleNEMA-4X4 to 20 mAlbIA1None"1"5Sgpmlb/ftReadingNEMA-7PulsekgIIB2H"1"10Sgphlb/galNEMA-4DigitalUS galIIICC1"2"10lb/hg/ccNEMA-12ftC&DPP1"3"20lb/minDAS2"4"40ft/seccPE2"6"80ft/minSSUF3"8"160ft/hcStConcentricMax. RateISApsiG10"Eccentric, BtmNearest 1/8"mm Hg12"Eccentric, Topin. WC18"Segmental20"24"%Mfr/Vendor125#WN"FlangesFCustomer150#Slip-on"Vena ContractaOthers300#Threaded"Pipe600#Elbow900#304SS1200#316SS1500#HastelloyMonel(l)Bellows(v)Diaphragm(g)Mercury(2Ph)

No entry required; pipe ID will beselected automatically from theNominal Size and Schedule.N/A means size/schedulecombination is unavailable.No entry required; b ratiois automatically calculated.

Coriolis MeterMontemayorFLOWMETER SPECIFICATION, CORIOLISSheetofRev. No.(English Units)CorporationProject No.1LocationChiclayo, PeruUnitCayaltiP.O. No.*$2Tag Number$3P&ID Number$4Line Number$5Service or Associated Equipment$6SERVICE CONDITIONS$7Fluid Name (l, v, g or 2)LiqVapGas$8Flow, Min.NominalMax.unitsgpmgphlb/min$9Temp., Min.NominalMax.FFF$10Press., Min.NominalMax.psigpsigpsig$11Fluid Density @STPOp'g T&Plb/ftg/cclb/gal$12Viscosity, Min.NominalMax.cPSSUcSt$13Air or Gas Bubbles; NameNYNYNY$14Size Range% by volume$15Suspended Solids; NameNYNYNY$16Size Range% by weight$17Pipe DiameterScheduleMaterial$18Liner MaterialInsulation Type, ThkNoneNoneA-Swt"Hot1"$19FLOWMETER SELECTION, MEASUREMENT PARAMETERS$20ManufacturerModel***$21Conn. SizeTypeRatingFace1"WN125#FF1"SW300#FF2"SO150#RF$22Material, Wetted PartsGaskets, Rings$23Meter MAWPMax. Allow. Temp.*psig*F*psig*F*psig*F$24DP @ Min.NominalMax. Flow***psi***psi***psi$25Velocity @ Min.NominalMax. Flow***fpsfps***fpsfps***fpsfps$26NRe @ Min.NominalMax. Flow*********$27Flow Acc'y @ Min./Nom./Max. FlowNom.Max. Flow***%***%***%$28Density Accuracy*g/cc*%*g/cc*%*g/cc*%Date5-May-99$29Required Accuracy% ofFull Scale% ofReading% ofFull Scale$30Required Repeatability% ofFull Scale% ofReading% ofReading$31Other:$32Rev.0$33INSTALLATION, INTERFACE SPECIFICATIONS$34Area ClassificationClassIIGrADiv2ClassIIGrBDiv1ClassIIIGrCDiv1Instrument Form No.$35Output UnitsHousing Requirements4 to 20 mANEMA-4XPulseNEMA-7DigitalNEMA-12$36Switches/AlarmsHiLoFaultHiLoFaultHiLoFault$37Other:Other:Other:$38Totalizer (check)Min. RangeUnits$39Cable Distance (Transducer to Console)feetOther:feetOther:feet$40Special Requirements:0 to0 to$41HiLoFaultHiLoFault$42Other:NROther:NR$43$44$45Remarks1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.$46$47$48RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.NoneFull ScaleNEMA-4X4 to 20 mAlbIA1None"Liqgpmlb/ftReadingNEMA-7PulsekgIIB2Hot"Vapgphlb/galNEMA-4DigitalUS galIIICCold1"Gaslb/hg/ccNEMA-12ftC&DPP1"2-Phlb/minft/lbDA-Swt2"ft/seccc/g"125#WNFFE2"ft/minm/kg"150#SORFF3"ft/h1"300#SWLJG1"600#Thr.RTJcP2"900#SSU3"1200#cSt4"1500#6"8"10"12"Fluid Density @Specific Volume @

Ultrasonic MeterMontemayorFLOWMETER SPECIFICATION, ULTRASONICSheetofRev. No.(English Units)CorporationProject No.1LocationPiura, PeruUnitL'Air LiquideP.O. No.*$2Tag Number$3P&ID Number$4Line Number$5Assoc. Equip./Service$6SERVICE CONDITIONS$7Fluid Name (l, v, g or 2)LiqGas2-Ph$8Flow, Min.NominalMax.unitsgpmgpmgpm$9Temp., Min.NominalMax.oFoFoF$10Press., Min.NominalMax.psigpsigpsig$11Fluid Density @ STP@ Op'g T&Plb/ft3lb/ft3lb/ft3$12Viscosity, Min.NominalMax.cPcPcP$13Air or Gas Bubbles; NameNYNYNY$14Size Range% by volume$15Suspended Solids; NameNYNYNY$16Size Range% by weight$17Pipe DiameterScheduleMaterial$18Liner MaterialInsulation Type, ThkHot1"NoneNoneCold1"$19FLOWMETER SELECTION, MEASUREMENT PARAMETERS$20ManufacturerModel**$21$22$23Max. Allow. Temp.*psig*FpsigFpsigF$24***psipsipsi$25Velocity @ Min.NominalMax. Flow***fpsfpsfpsfpsfpsfps$26NRe @ Min.NominalMax. Flow***$27Flow Acc'y @ Min./Nom./Max. FlowNom.Max. Flow***%%%$28Density Accuracy*g/cc*%g/cc%g/cc%Date5-May-99$29Required Accuracy% ofFull Scale% of% ofFull Scale% of% ofFull Scale$30Required Repeatability% ofReading% of% ofFull Scale% of% ofFull Scale$31Other:$32INSTALLATION, INTERFACE SPECIFICATIONSRev.0$33Area ClassificationClassGrDivClassGrDivClassIGrADiv2$34Housing RequirementsInstrument Form No.$35Output Units$36AlarmsHiLoFaultHiLoFaultHiLoFault$37Other:Other:Other:$38Totalizer (check)Min. RangeUnits$39Cable Distance (Transducer to Console)feetOther:feetOther:feet$40Special Requirements:0 to0 to$41HiLoFaultHiLoFault$42Other:NROther:NR$43$44$45Remarks1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.$46$47$48RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.Full ScaleNEMA-4X4 to 20 mAlbIA1Nonegpmlb/ftReadingNEMA-7PulsekgIIB2None"Liqgphlb/galNEMA-4DigitalUS galIIICHot"Vaplb/hg/ccNEMA-12C&DCold1"Gaslb/minft/lbDPP1"2-Phft/seccc/gEA-Swt2"ft/minm/kgF2"ft/hG3"cPSSUcSt

Mass MeterMontemayorFLOWMETER SPECIFICATION, MASSSheetofRev. No.(English Units)CorporationProject No.1LocationCaracas, VenezuelaUnitRbt. HumphriesP.O. No.*$2Tag Number$3P&ID Number$4Line Number$5Assoc. Equip./Service$6SERVICE CONDITIONS$7Fluid Name (l, v, g or 2)$8Flow, Min.NominalMax.unitsgpmgpmgpm$9Temp., Min.NominalMax.oFoFoF$10Press., Min.NominalMax.psigpsigpsig$11Fluid Density @ STP@ Op'g T&Plb/ft3lb/ft3lb/ft3$12Viscosity, Min.NominalMax.cPcPcP$13Air or Gas Bubbles; NameNYNYNY$14Size Range% by volume$15Suspended Solids; NameNYNYNY$16Size Range% by weight$17Pipe DiameterScheduleMaterial$18Liner MaterialInsulation Type, ThkNoneNoneHotNoneA-Swt1"$19FLOWMETER SELECTION, MEASUREMENT PARAMETERS$20ManufacturerModel**$21$22$23Max. Allow. Temp.*psig*FpsigFpsigF$24***psipsipsi$25Velocity @ Min.NominalMax. Flow***fpsfpsfpsfpsfpsfps$26NRe @ Min.NominalMax. Flow***$27Flow Acc'y @ Min./Nom./Max. FlowNom.Max. Flow***%%%$28Density Accuracy*g/cc*%g/cc%g/cc%Date5-May-99$29Required Accuracy% ofFull Scale% of% ofRdg% of% ofRdg$30Required Repeatability% ofReading% of% ofRdg% of% ofRdg$31Other:$32INSTALLATION, INTERFACE SPECIFICATIONSRev.0$33Area ClassificationClassIGrADiv2ClassIIGrBDiv1ClassIIIGrCDiv1$34Housing RequirementsNEMA-4XNEMA-7NEMA-4Instrument Form No.$35Output Units4 to 20 mAPulseDigital$36AlarmsHiLoFaultHiLoFaultHiLoFault$37Other:Other:Other:$38Totalizer (check)Min. RangeUnits$39Cable Distance (Transducer to Console)feetOther:feetOther:feet$40Special Requirements:0 to0 to$41HiLoFaultHiLoFault$42Other:NROther:NR$43$44$45Remarks1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.$46$47$48RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.Full ScaleNEMA-4X4 to 20 mAlbIA1Nonegpmlb/ftReadingNEMA-7PulsekgIIB2None"Liqgphlb/galNEMA-4DigitalUS galIIICHot"Vaplb/hg/ccNEMA-12C&DCold1"Gaslb/minft/lbDPP1"2-Phft/seccc/gEA-Swt2"ft/minm/kgF2"ft/hG3"cPSSUcSt

Turbine MeterMontemayorFLOWMETER SPECIFICATION, TURBINESheetofRev. No.(English Units)CorporationProject No.1LocationArica, ChileUnitAir ProductsP.O. No.*$2Tag Number$3P&ID Number$4Line Number$5Assoc. Equip./Service$6SERVICE CONDITIONS$7Fluid Name (l, v, g or 2)$8Flow, Min.NominalMax.unitsgpmgpmgpm$9Temp., Min.NominalMax.oFoFoF$10Press., Min.NominalMax.psigpsigpsig$11Fluid Density @ STP@ Op'g T&Plb/ft3lb/ft3lb/ft3$12Viscosity, Min.NominalMax.cPcPcP$13Air or Gas Bubbles; NameNYNYNY$14Size Range% by volume$15Suspended Solids; NameNYNYNY$16Size Range% by weight$17Pipe DiameterScheduleMaterial$18Liner MaterialInsulation Type, Thk$19FLOWMETER SELECTION, MEASUREMENT PARAMETERS$20ManufacturerModel**$21$22$23Max. Allow. Temp.*psig*F*psig*F*psig*F$24***psipsipsi$25Velocity @ Min.NominalMax. Flow***fpsfpsfpsfpsfpsfps$26NRe @ Min.NominalMax. Flow***$27Flow Acc'y @ Min./Nom./Max. FlowNom.Max. Flow***%***%***%$28Density Accuracy*g/cc*%*g/cc*%*g/cc*%Date5-May-99$29Required Accuracy% ofReading% of% ofRdg% of% ofRdg$30Required Repeatability% ofFull Scale% of% ofRdg% of% ofRdg$31Other:$32INSTALLATION, INTERFACE SPECIFICATIONSRev.0$33Area ClassificationClassIIGrADiv2ClassIGrADiv1ClassIGrCDiv1$34Housing RequirementsNEMA-4XNEMA-7NEMA-4Instrument Form No.$35Output Units4 to 20 mAPulsePulse$36AlarmsHiLoFaultHiLoFaultHiLoFault$37Other:Other:Other:$38Totalizer (check)Min. RangeUnitslbkgUS gal$39Cable Distance (Transducer to Console)feetOther:feetOther:feet$40Special Requirements:0 to0 to$41HiLoFaultHiLoFault$42Other:NROther:NR$43$44$45Remarks1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.$46$47$48RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.Full ScaleNEMA-4X4 to 20 mAlbIA1None"gpmlb/ftReadingNEMA-7PulsekgIIB2H"Liqgphlb/galNEMA-4DigitalUS galIIICC1"Vaplb/hg/ccNEMA-12C&DPP1"Gaslb/minft/lbDAS2"2-Phft/seccc/gE2"ft/minm/kgF3"ft/hGcPSSUcSt

VortexMontemayorFLOWMETER SPECIFICATION, VORTEXSheetofRev. No.(English Units)CorporationProject No.1LocationLa Paz, BoliviaUnitPepe MendiettaP.O. No.*$2Tag Number$3P&ID Number$4Line Number$5Assoc. Equip./Service$6SERVICE CONDITIONS$7Fluid Name (l, v, g or 2)$8Flow, Min.NominalMax.unitsgpmgpmgpm$9Temp., Min.NominalMax.oFoFoF$10Press., Min.NominalMax.psigpsigpsig$11Fluid Density @ STP@ Op'g T&Plb/ft3lb/ft3lb/ft3$12Viscosity, Min.NominalMax.cPcPcP$13Air or Gas Bubbles; NameNYNYNY$14Size Range% by volume$15Suspended Solids; NameNYNYNY$16Size Range% by weight$17Pipe DiameterScheduleMaterial$18Liner MaterialInsulation Type, Thk$19FLOWMETER SELECTION, MEASUREMENT PARAMETERS$20ManufacturerModel**$21$22$23Max. Allow. Temp.*psig*FpsigFpsigF$24***psipsipsi$25Velocity @ Min.NominalMax. Flow***fpsfpsfpsfpsfpsfps$26NRe @ Min.NominalMax. Flow***$27Flow Acc'y @ Min./Nom./Max. FlowNom.Max. Flow***%%%$28Density Accuracy*g/cc*%g/cc%g/cc%Date5-May-99$29Required Accuracy% of% of% ofRdg% of% ofRdg$30Required Repeatability% of% of% ofRdg% of% ofRdg$31Other:$32INSTALLATION, INTERFACE SPECIFICATIONSRev.0$33Area ClassificationClassIGrADiv1ClassIIGrBDiv2ClassIIIGrCDiv2$34Housing RequirementsNEMA-12NEMA-4NEMA-7Instrument Form No.$35Output Units4 to 20 mAPulseDigital$36AlarmsHiLoFaultHiLoFaultHiLoFault$37Other:Other:Other:$38Totalizer (check)Min. RangeUnitslbkgUS gal$39Cable Distance (Transducer to Console)feetOther:feetOther:feet$40Special Requirements:0 to0 to$41HiLoFaultHiLoFault$42Other:NROther:NR$43$44$45Remarks1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.$46$47$48RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.Full ScaleNEMA-4X4 to 20 mAlbIA1None"gpmlb/ftReadingNEMA-7PulsekgIIB2H"Liqgphlb/galNEMA-4DigitalUS galIIICC1"Vaplb/hg/ccNEMA-12C&DPP1"Gaslb/minft/lbDAS2"2-Phft/seccc/gE2"ft/minm/kgF3"ft/hGcPSSUcSt

Magnetic MeterMontemayorFLOWMETER SPECIFICATION, MAGNETICSheet1ofRev. No.(English Units)CorporationProject No.1LocationVictoria, TXUnitDuPont Nitric AcidP.O. No.*$2Tag Number$3P&ID Number$4Line Number$5Assoc. Equip./Service$6SERVICE CONDITIONS$7Fluid Name (l, v, g or 2)LiqGas2-Ph$8Flow, Min.NominalMax.unitsgpmlb/minlb/min$9Temp., Min.NominalMax.oCoCoC$10Press., Min.NominalMax.kPapsiaatm$11Fluid Density @ STP@ Op'g T&Plb/ftlb/ftlb/ft$12Viscosity, Min.NominalMax.cPSSUcSt$13Air or Gas Bubbles; NameNYNYNY$14Size Range% by volume$15Suspended Solids; NameNYNYNY$16Size Range% by weight$17Pipe DiameterScheduleMaterial$18Liner MaterialInsulation Type, Thk$19FLOWMETER SELECTION, MEASUREMENT PARAMETERS$20ManufacturerModel**$21$22$23Max. Allow. Temp.*psig*F*psig*F*psig*F$24***psipsipsi$25Velocity @ Min.NominalMax. Flow***fpsfpsfpsfpsfpsfps$26NRe @ Min.NominalMax. Flow***$27Flow Acc'y @ Min./Nom./Max. FlowNom.Max. Flow***%%%$28Density Accuracy*g/cc*%g/cc%g/cc%Date5-May-99$29Required Accuracy% ofFull Scale% of% ofReading% of% ofFull Scale$30Required Repeatability% ofReading% of% ofFull Scale% of% ofReading$31Other:$32INSTALLATION, INTERFACE SPECIFICATIONSRev.0$33Area ClassificationClassIGrADiv1ClassIIGrBDiv1ClassIIIGrCDiv2$34Housing RequirementsNEMA-4XNEMA-7NEMA-4Instrument Form No.$35Output Units4 to 20 mAPulseDigital$36AlarmsHiLoFaultHiLoFaultHiLoFault$37Other:Other:Other:$38Totalizer (check)Min. RangeUnitslbkgUS gal$39Cable Distance (Transducer to Console)feetOther:feetOther:feet$40Special Requirements:0 to0 to$41HiLoFaultHiLoFault$42Other:NROther:NR$43$44$45Remarks1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.$46$47$48RevDateDescriptionByChk.Appr.RevDateDescriptionByChk.Appr.Full ScaleNEMA-4X4 to 20 mAlbIA1None"gpmlb/ftReadingNEMA-7PulsekgIIB2H"Liqgphlb/galNEMA-4DigitalUS galIIICC1"Vaplb/hg/ccNEMA-12C&DPP1"Gaslb/minft/lboFDAS2"2-Phft/seccc/goCE2"ft/minm/kgF3"psiaft/hGpsigatmcPbargSSUkPacSt