塔设备再沸器、冷凝器选型源文件

1、Heat Exchanger Thermal DesignSFile: E0301.EDR&TubeV8.4Heat Exchanger Specification Sheet12345678910111213141516171819202122232425262728293031323334353637383940414243444546474849505152535455565758Company:Location:Service of Unit:Our Reference:Item No.:Your Reference:Date:Rev No.:Job No.:Size1500 /600

2、0mm TypeBEMVerConnected in2parallel1seriesSurf/unit(eff.)1303.3m2Ss/unit2Surf/s(eff.)651.6m2PERFORMANCE OF ONE UNITFluid allocation SSideTube SideFluid name T0301冷凝器C3H6冷冻剂Fluidty, Total kg/h4564247795 Vapor (In/Out) kg/h45609970047795 Liquid kg/h044639477950 Noncondensable kg/h330 Temperature (In/O

3、ut) C3.86-37.82-43.99-43.62 Dew / Bubble po C3.83-52.39-43.99-43.99Density (Vap / Liq) kg/m317.54/ 548.89 / 612.612.72/Viscosity cp.0091/ .123 / .1758.0068/Molecular wt, Vap 36.6420.5142.08Molecular wt, NC 2.02Specific heat kcal/(kg*C).4137/ .5858 / .5166.3123/Thermal conductivity kcal/(h*m*C).017/.

4、11 /.117.01/Latent heat kcal/kg86.9191.88104.65104.69Prere (abs) kgf/cm29.6989.6881.2241.215Velocity m/s1.567.46Prere drop, allow./calc. kgf/cm2.265.009.245.009Fouling(min) m2*h*C/kcal.00021.00021.00027Ao based Heat exchanged5007612 kcal/h MTD corrected29.13CTransfer rate, Service131.9 Dirty 276Clea

5、n 317.6kcal/(h*m2*CCONSTRUCTION OF ONE SSketch SSide Tube Side Design/vac/test prere:g kgf/cm211.217 /3.059/Design temperatureC40 35Numbasses per s1 1Corroallowancemm3.18 3.18ConnectionsSize/rating NominalIn mm1 406.4 / -1152.4/-Out1 152.4 / -1508/-ermediate / - /-Tube No.1851OD19Tks- Avg 2 mmLength

6、 6000 mm Pitch32mmTube typePlain Material Carbon Steel Tube pattern 30SCarbon SteelID 1500OD 1526 mmScover -Channel or bonnetCarbon Steel Channel cover -Tubesheet-s ionaryCarbon Steel Tubesheet-floating-Floating head cover- Imement protectionNoneBaffle-cross Carbon SteelTypeSingle segmentalCut(%d)24

7、.13 VSpacing: c/c600mBaffle-long - Seal type Inlet548.98mSupports-tube U-bend Type Bypass seal Tube-tubesheet joExp. 2 grvExpanjo - Type RhoV2-Inlet nozzle165Bundle entrance 49Bundle exit16kg/(m*sGaskets - Sside- Tube Side Flat Metal Jacket Fibe Floating head- Code requirementsASME Code Sec VIII Div

8、 1 TEMA class R - refinery serviceWeight/S16583.7 Filled with water 28060.6 Bundle 11540.9kRemarks Heat Exchanger Thermal DesignS&TubeV8.4File:E0301.EDRSetting PlanT2Tube Layout9 008532 0000S he l ins de d ame ermm1500.Front head ins de d ame ermm1500.Outer tube lim tmm1 85 713Tube number (ca cs.)18

9、51Tube number ( ayout)1851Tube lengthmm6000.Tube O.D.mm19.Tube p tm32.Tube pattern30Tube passes1Tie rod number10Tie rod diametermm12.7S ea ing strips (pairs)5B aff e typeS ingle segmentalCentre to outer baff e cutmm387.9792Centre to inner baff e cutIm ement pro ectionNoneS he l S ide Inlet Nozzle In

10、side Diame ermm387.35S he l S ide Outlet Nozz e Inside Diametermm15 .051CompanyAspen S & Tubeoc ationSe vic e o UnitItem NoDesign CodesTube LayoutA S ME Code S ec VIII Div 1TE MA R - e inery serviceDrawing NumberCustomer S pecifica ionsRevis onDateDwg.A pp.2016/7/11113963963 963963A8630 Ove all599 5

11、08 2105 60729T712 0 mm632 0 mm1T5081800920Pul ing Length63Views on arrow AT1S1 S2Nozz le DataDesign DataUn tsShe l Channel Company:Ref OD WallStandardNotes Design Pre rebar11.3.Location:Aspen S& T ube ExchangerS1 406 mm 9.5 mm150 ANSI S ip onDesign TemperatureC40.35.Service of Unit:Our Refe ence:S2

12、168 mm 7.1 mm150 ANSI S ip onFull Vac uum00Item No.:Your Reference:T1 168 mm 7.1 mm150 ANSI S ip onCorro Allowance mm3.1753.175 Date:Rev No.: Job No.:Setting PlanT2 508 mm 9.5 mm150 ANSI S ip onTes t Pre ebarNumber of Pas ses11Design CodesBEM 1500 - 6000Radiography000PWHT00TEMA 0ernal Volumem? 10.2916 4.2072Drawing NumberCustomer Spec fica ionsWeight SummaryEmpty FloodedBundleRev