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OutputSummary

ReleasedtothefollowingHTRIMemberCompany:

Page1

ZJUT

WingTeam

SIUnits

XistEVer.6.00 2013/8/912:12SN:Vals100+

Wingteam

HeatExchange

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

SeeDataCheckMessagesReportforWarningMessages.

SeeRuntimeMessageReportforWarningMessages.

3

ProcessConditions

ColdShellside

coolingwater

HotTubeside

T303w--T304

0.3075

Fluidname

Flowrate

Inlet/OutletY

Inlet/OutletT

InletP/Avg

dP/Allow.

(kg/s)(Wt.fracvap.)

(DegC)

(kPa)

(kPa)(m2-K/W)

6.8611

0.000

20.81

99.883

0.000

0.000172

0.000

20.00

101.331

2.897

0.000

136.70

101.331

0.368

0.000

108.00

101.147

0.000

0.000200

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

Fouling

ExchangerPerformance

ShellhTubehHotregime

ColdregimeEMTD

(W/m2-K)

(W/m2-K)

(--)

(--)

(DegC)

ShellGeometry

(--)

(mm)(--)

(--)

(deg)

TubeGeometry

(--)

(mm)

(m)(--)

(deg)(--)

(--)

1824.91

166.44

Sens.LiquidSens.Liquid

101.5

ActualURequiredUDuty

AreaOverdesign

(W/m2-K)

(W/m2-K)

(MegaWatts)

(m2)

(%)

BaffleGeometry

(--)

(PctDia.)

130.26

49.05

0.0209

4.188

165.56

BES325.000

1

1

0.00

TEMAtypeShellIDSeriesParallelOrientation

BaffletypeBafflecut

Single-Seg.

25.00

Perpend.300.000

3

BaffleorientationCentralspacingCrosspasses

(--)

(mm)(--)

Nozzles

(mm)

(mm)

(mm)

(mm)

(mm)

(mm)

77.927

77.927

30.562

30.562

26.645

26.645

TubetypeTubeODLengthPitchratioLayoutTubecountTubePass

Plain19.000

1.500

1.8421

60

48

2

ShellinletShelloutletInletheightOutletheightTubeinletTubeoutlet

ThermalResistance,%

Velocities,m/s

Shellside

FlowFractions

ShellTubeFoulingMetal

7.14

87.47

5.15

0.25

0.14

ABCEF

0.022

0.733

0.188

0.058

0.000

TubesideCrossflowWindow

6.753e-2

0.12

0.47

RunLog

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WingteamHeatExchange

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBafflesBeginningRun

1

2RunningXistUnit1,100

3RunCompleted.

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

SolutionReachedin00:00.

FinalResults

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WingteamHeatExchange

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

SIUnits

1

Fluidname

Fluidcondition4Totalflowrate

ProcessData

ColdShellside

coolingwater

Sens.Liquid

6.8611

HotTubeside

T303w--T304

Sens.Liquid

0.3075

ShellsidePerformance

Nomvel,X-flow/window

0.12/0.47

(kg/s)(--)

(DegC)

(DegC)

(DegC)

(kPa)

(kPa)

(m/s)(--)

(W/m2-K)

(--)

(m2-K/W)

Flowfractionsforheattransfer

0.879

Weightfractionvapor,In/Out

Temperature,In/Out

Temperature,Average/Skin8Walltemperature,Min/Max

Pressure,In/Average

Pressuredrop,Total/Allowed

Velocity,Mid/Maxallow12Molefractioninert

Averagefilmcoef.

Heattransfersafetyfactor

Foulingresistance16

Overallcoef.,Reqd/Clean/Actual

Heatduty,Calculated/Specified

0.000

20.00

20.41

24.84

101.331

2.897

0.14

0.000

20.81

27.66

34.79

99.883

0.000

136.70

122.35

25.02

101.331

0.368

6.753e-2

0.000

108.00

33.12

35.12

101.147

A=0.0219B=0.7329C=0.1876E=0.0576F=0.0000

ShellsideHeatTransferCorrections

Total0.963

Beta0.919

Gamma1.047

End0.783

Fin1.000

PressureDrops(PercentofTotal)

Cross1.00MOMENTUM

Window

3.71

Ends6.39

0.00

NozzleInletOutlet

Shell44.44

44.46

Tube55.32

33.71

1824.91

1.000

0.000172

166.44

1.000

0.000200

Two-PhaseParameters

OverallPerformanceData

(W/m2-K)

Method

Inlet

Center

Outlet

MixF

49.05

/

/

137.33

/

130.26

(MegaWatts)

(DegC)

(DegC)

0.0209

101.5

101.51

Effectiveoveralltemperaturedifference

EMTD=(MTD)*(DELTA)*(F/G/H)21

22

SeeRuntimeMessagesReportfor

warnings.

25

H.T.Parameters

Overallwallcorrection

Shell

1.023

6.40

7976

1365

1867

Tube

1.000

6.16

2697

3247

2009

*

1.0000

*

1.0000

MidpointMidpointBundleinletBundleoutletFoulinglayer

Prandtlno.Reynoldsno.Reynoldsno.Reynoldsno.

(mm)

325

mm

26

ExchangerFluidVolumes

ThermalResistance

27Approximateshellside(L)28Approximatetubeside(L)29

TEMAshelltype

ShellsSeries

PassesShell

Shellorientationangle(deg)

Impingementpresent

Pairssealstrips

Shellexpansionjoint

103.1

72.8

Shell7.14

Tube87.47

Fouling5.15

Metal0.25

OverDes

165.56

3.953e-4

0.01271

1.5

m

ShellConstructionInformation

TotalfoulingresistanceDifferentialresistance

ShellNozzlesInletatchannelend-NoNumberateachpositionDiameter

VelocityPressuredrop

HeightundernozzleNozzleR-V-SQShellent.

BES

1Parallel

1Tube

0.00

No1

No

ShellIDTotalareaEff.area

(mm)

(m2)

(m2/shell)

325.000

4.298

4.188

1

2

LiquidOutlet

0

Inlet

1

77.927

1.44

1.287

30.562

2071.95

505.32

Outlet

1

77.927

1.44

1.288

30.562

2073.57

505.71

(mm)

(m/s)

(kPa)

(mm)(kg/m-s2)

(kg/m-s2)

Passlanesealrods(mm)0.000

No.0

Rearheadsupportplate

No

37WeightestimationWet/Dry/Bundle38

39

666.88/

491.01

/

57.59(kg/shell)

BaffleInformation

40Type

Perpend.Single-Seg.

Bafflecut(%dia)25.00

Crosspasses/shellpass

Centralspacing

Inletspacing

Outletspacing

Bafflethickness46

47

48

Tubetype

Overalllength

Effectivelength

Totaltubesheet

Arearatio54Tubemetal

3

300.000

665.501

496.384

3.175

No.(PctArea)

(mm)toC.L

81.250

0.000

InletRADIAL26.645

0.67

0.204

370.61

OutletRADIAL26.645

0.64

0.124

354.84

LiquidOutlet

(mm)

(mm)

(mm)

(mm)

1

2

21.02

0.00

TubeNozzle

DiameterVelocityPressuredropNozzleR-V-SQ

(mm)

(m/s)

(kPa)(kg/m-s2)

TubeInformation

AnnularDistributor

LengthHeightSlotarea

Inlet

Outlet

Plain1.500

1.462

38.100

1.1176

Tubecountpershell

Pcttubesremoved(both)Outsidediameter

Wallthickness

48

(mm)

(mm)

(mm2)

(m)

(m)

(mm)(out/in)

(mm)

(mm)

19.000

1.000

1.8421

60

DiametralClearances(mm)

Pitch(mm)

35.0000Ratio

Baffle-to-shell

3.1750

Bundle-to-shell

53.6455

Tube-to-baffle

0.7938

Carbonsteel

Tubepattern(deg)

SupplementaryResults

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SIUnits

HeatExchange

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

1

2Type

ExternallyEnhancedTubeGeometry

Plain

InternallyEnhancedTubeGeometry

None

Type

Findensity

Finheight

Finthickness

Rootdiameter

Area/length

8

9

(fin/meter)

(mm)

(mm)

(mm)

(m2/m)

ThicknessPitch

(mm)

(L/D)

MeanMetalTemperatures

10Meanshelltemperature

11

20.36

(C)

Meantubemetaltemperatureineachtubepass,(C)

12

13

14

15

TubePass

1

2

Inside

31.45

28.88

Outside

31.17

28.67

Radial

31.31

28.77

ShellsideIncrementalMonitor

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WingteamHeatExchange

Rating-HorizontalMultipassFlo

SIUnits

WithSingle-SegmentalBaffles

ShellsideFlowRegion

Pointnumber

Shellpass

Lengthfromtubeinlet

Massfractionvapor6Bulktemperature

Skintemperature

MTD

DeltaMTDcorrection10Pressure

Pressuredrop

Frictionloss

Staticheadloss14Momentumloss

Shearstressattubewall

Crossflow

Longitudinalflow18Area

Cumulativearea

Duty

Cumulativeduty

Heatflux

Calculatedheatflux

Criticalheatflux25OverallU

Shellsideh

Sensibleliquidh

Sensiblevaporh29Condensatefilmh

30Vaporphaseh31Nucleateboilingh

Conv.boilingh

Filmboilingh

Boilingthinfilmh35Naturalconvectiveh

36LocalReynolds37VaporReynolds38LiquidReynolds39VaporPrandtl40LiquidPrandtl

41Flowregimeparam.42Condensateregime

Boilingregime

Boilingmechanism

1

(--)

(--)

(mm)(--)(C)

(C)

(C)(--)

(kPa)

(kPa)

(kPa)

(kPa)

(kPa)

6.8611kg/s

1

1

2

1

3

1

646.384

0.0000

20.43

25.41

101.0

1.000

100.532

0.136

0.136

0.000

0.000

4

1

248.192

0.0000

20.65

28.01

103.2

1.000

100.415

0.098

0.098

0.000

0.000

5

1

0.000

0.0000

20.81

1461.89

1129.13

0.0000

20.00

0.0000

20.21

28.39

100.3

1.000

100.644

0.088

0.088

0.000

0.000

101.331

1.287

98.434

1.288

(Pa)

(Pa)

(m2)

(m2)

(MegaWatts)(MegaWatts)

(W/m2)

(W/m2)

(W/m2)(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(--)

(--)

(--)

(--)

(--)

(--)

(--)

(--)

(--)

0.00

2.18

1.907

1.907

0.0093

0.0093

4878.52

12338.6

0.00

128.89

1892.56

1892.56

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

6039

0

6039

0.00

6.44

0.0000

0.28

2.18

0.860

2.766

0.0043

0.0136

4953.80

12533.2

0.00

130.03

2754.42

2754.42

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

7976

0

7976

0.00

6.40

0.0000

0.00

2.18

1.422

4.188

0.0073

0.0209

5128.21

12989.5

0.00

132.22

2104.59

2104.59

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

6243

0

6243

0.00

6.38

0.0000

1365

0

1365

0.00

6.47

1867

0

1867

0.00

6.35

SensLiqSensLiq

SensLiqSensLiq

SensLiqSensLiq

wTEM

ABESShell

TubesideIncrementalMonitor

Page6

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WingteamHeatExchange

SIUnits

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

Pointnumber

TubePass

Lengthfromtubeinlet

Massfractionvapor5Bulktemperature

Skintemperature

MTD

Pressure

Pressuredrop

Enhancedpressuredropmult

Frictionloss12Staticheadloss13Momentumloss

Maximumvelocity

Averagevelocity

Shearstressattubewall17Area

18Cumulativearea

(--)

(--)

(mm)(--)(C)

(C)

(C)

(kPa)

(kPa)(--)

(kPa)

(kPa)

(kPa)

(m/s)

(m/s)

(Pa)

(m2)

(m2)

1

1

0.000

0.0000

136.70

2

1

248.192

0.0000

133.54

37.67

112.8

101.121

5.319e-3

3

1

646.384

0.0000

128.69

32.62

108.3

101.118

3.665e-3

4

1

1129.13

0.0000

123.85

33.65

103.5

101.110

7.206e-3

5

2

1129.13

0.0000

117.46

33.75

97.3

101.100

0.010

6

2

646.384

0.0000

112.91

29.20

92.4

101.096

3.845e-3

7

2

248.192

0.0000

109.82

29.68

89.3

101.089

7.132e-3

8

2

0.000

0.0000

108.00

101.331

0.205

100.963

0.126

5.319e-3

0.000

0.000

6.856e-2

6.856e-2

0.33

0.711

0.711

0.0047

0.0047

6642.93

16870.3

3.665e-3

0.000

0.000

6.799e-2

6.798e-2

0.24

0.430

1.141

0.0025

0.0072

5752.72

14579.9

7.206e-3

0.000

0.000

6.754e-2

6.753e-2

0.46

0.953

2.094

0.0046

0.0118

4832.85

12221.1

0.010

0.000

0.000

6.689e-2

6.688e-2

0.38

0.953

3.048

0.0047

0.0165

4924.18

12456.4

3.845e-3

0.000

0.000

6.638e-2

6.637e-2

0.25

0.430

3.477

0.0018

0.0183

4154.88

10487.3

7.132e-3

0.000

0.000

6.610e-2

6.609e-2

0.45

0.711

4.188

0.0026

0.0209

3613.48

9110.11

Duty

Cumulativeduty

Heatflux

Calculatedheatflux

Criticalheatflux24OverallU

25Tubesideh

(MegaWatts)(MegaWatts)

(W/m2)

(W/m2)

(W/m2)(W/m2-K)

(W/m2-K)

158.48

208.65

141.87

178.54

123.59

158.75

134.20

174.62

118.19

145.67

105.96

131.74

Enhancedheattransfermult

Sensibleliquidh

Sensiblevaporh29Condensatefilmh

30Vaporphaseh31Nucleateboilingh

Conv.boilingh

Filmboilingh

Boilingthinfilmh35Naturalconvectiveh

36LocalReynolds37VaporReynolds38LiquidReynolds39VaporPrandtl40LiquidPrandtl

41Flowregimeparam.42Condensateregime

Boilingregime

Boilingmechanism

(--)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(W/m2-K)

(--)

(--)

(--)

(--)

(--)

(--)

(--)

(--)

(--)

208.65

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

3248

0

3248

0.00

5.37

0.0000

SensLiq

178.54

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

2937

0

2937

0.00

5.78

0.0000

SensLiq

158.75

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

2697

0

2697

0.00

6.16

0.0000

SensLiq

174.62

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

2378

0

2378

0.00

6.78

0.0000

SensLiq

145.67

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

2137

0

2137

0.00

7.36

0.0000

SensLiq

131.74

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

2010

0

2010

0.00

7.72

0.0000

SensLiq

3247

0

3380

0.00

5.21

2009

0

1958

0.00

8.02

VibrationAnalysis

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HeatExchange

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

1Shellsidecondition2Axialstressloading3Beta

Sens.Liquid

0.000

4.434

Inlet

0.965

0.635

2

56.1+

(Level2.3)

Addedmassfactor

(MPa)

1.276

4

PositionInTheBundle

Center

0.600

0.394

2

145.2

Outlet

0.796

0.524

2

82.4

5Lengthfornaturalfrequency6Length/TEMAmaximumspan7Numberofspans

8Tubenaturalfrequency9Shellacousticfrequency

(m)(--)

(--)(Hz)

(Hz)

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

50

51

52

53

FlowVelocitiesWindowparallelvelocityBundlecrossflowvelocityBundle/shellvelocity

Inlet

0.46

4.687e-2

3.609e-2

Inlet

0.055

1.84

0.0358

0.0331

Inlet

Center

0.46

0.11

8.095e-2

Center

0.038

3.96

0.0374

0.0345

Center

Outlet

0.46

6.289e-2

4.842e-2

Outlet

0.043

2.38

0.0371

0.0343

Outlet

(m/s)

(m/s)

(m/s)

FluidelasticInstabilityCheck

LogdecrementCriticalvelocity

BaffletipcrossvelocityratioAveragecrossflowvelocityratio

HTRI

(m/s)(--)

(--)

AcousticVibrationCheck

VortexsheddingratioChennumberTurbulentbuffetingratio

TubeVibrationCheck

Vortexsheddingratio

(--)

(--)

(--)

Inlet

0.014

0.002

0.001

16.000

3.71

Center

0.032

0.001

0.000

16.000

18.66

Outlet

0.019

0.002

0.000

16.000

6.68

(--)

ParallelflowamplitudeCrossflowamplitudeTubegap

CrossflowRHO-V-SQ

(mm)

(mm)

(mm)(kg/m-s2)

BundleEntrance/Exit(analysisatfirsttuberow)

FluidelasticinstabilityratioVortexsheddingratioCrossflowamplitudeCrossflowvelocity

Tubesheettoinlet/outletsupport

ShellEntrance/ExitParameters

ImpingementplateFlowarea

VelocityRHO-V-SQ

Entrance

0.028

0.033

0.00064

0.11

None

Entrance

No9.658e-3

0.71

505.32

Exit

0.024

0.044

0.00035

0.15

None

Exit

(--)

(--)

(mm)

(m/s)

(mm)

(m2)

(m/s)(kg/m-s2)

9.658e-3

0.71

505.71

Single-Seg.Perpend.19.000

Carbonsteel

ShelltypeTubetypePitchratioLayoutangle

BES

Plain1.8421

60

BaffletypeBafflelayout

Tubediameter,(mm)TubematerialSupports/bafflespaceProgramMessages

+Frequencyratiosarebaseduponlowestnaturaloracousticfrequency

*Itemswithasteriskexceedaconservativelowerlimitforvibration-freedesign.

Reviewyourcase

usingtheproceduredescribedinOnlineHelp;Youmayfindthatavibrationproblemisunlikely.

1

2

3

4

Page8

SIUnits

HEATEXCHANGERRATINGDATASHEET

5ServiceofUnit

ItemNo.

ConnectedIn1Parallel

6Type

BES

OrientationHorizontal

Shell/Unit1

1Series

7Surf/Unit(Gross/Eff)4.30/4.19m2

8

9FluidAllocation10FluidName

Surf/Shell(Gross/Eff)4.30/4.19m2

PERFORMANCEOFONEUNIT

ShellSide

coolingwater

TubeSide

T303w--T304

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

FluidQuantity,TotalVapor(In/Out)Liquid

Temperature(In/Out)Density

ViscositySpecificHeat

ThermalConductivityCriticalPressureInletPressureVelocity

PressureDrop,Allow/CalcAverageFilmCoefficientFoulingResistance(min)

HeatExchanged

kg/swt%wt%C

kg/m3mN-s/m2kJ/kg-CW/m-CkPa

kPam/skPa

W/m2-Km2-K/W

0.0209

49.05

6.8611

0.3075

0.0

100.0

20.00

998.77

1.0214

3.7946

0.5993

0.0

100.0

20.81

997.99

1.0025

3.8000

0.6005

0.0

100.0

136.70

820.48

0.2837

2.4844

0.1354

0.0

100.0

108.00

856.93

0.5017

2.3116

0.1446

101.331

101.331

0.14

2.897

6.753e-2

0.368

1824.91

0.000172

MegaWattsMTD(Corrected)

166.44

0.000200

Overdesign165.56

101.5C

%

26TransferRate,Service27

28

DesignPressure

DesignTemperature

NoPassesperShell

FlowDirection

W/m2-K

Calculated

130.26W/m2-K

Clean137.33W/m2-K

Sketch(Bundle/NozzleOrientation)

CONSTRUCTIONOFONESHELL

ShellSide

TubeSide1034.21

136.70

2

Downward1@26.645

1@26.645

@

Length

kPaGC

1034.21

136.70

1

Upward1@77.927

1@77.927

@

Thk(Avg)1.000mm

325

mm

33

34

35

ConnectionsSize&Rating

InOut

mmmm

1.5

m

Liq.Outmm

48OD19.000mm

36TubeNo.

1.500

m

Pitch35.000mm Layout60

37TubeTypePlain

MaterialCARBONSTEEL

Pairssealstrips

1

38ShellID

325.000mm

KettleID

mm

%Cut(Diam)25.00

PasslaneSealRodNo.0

ImpingementPlateNo.ofCrosspasses

39CrossBaffleTypePERPEND.SINGLE-SEG.

None3

kg/m-s2

40Spacing(c/c)300.000

mm

Inlet

665.501 mm

ShellEntrance

BundleEntrance

41Rho-V2-InletNozzle2071.95kg/m-s2

42

505.32

11.85

ShellExit

505.71

BundleExitBundleVelocities,m/sShellside

21.31

57.59kg

kg/m-s2

Weight/Shell

Notes:45

46

47

48

49

491.01

FilledwithWater

666.88

ThermalResistance,%

FlowFractionsA

BCE

F

ShellTubeFouling

Metal

7.14

87.47

5.15

0.25

0.14

0.022

0.733

0.188

0.058

0.000

TubesideCrossflow

Window

6.753e-2

0.12

0.47

1

2

3

4

HEATEXCHANGERSPECIFICATIONSHEET

Page9

SIUnits

JobNo.

Customer

Address

PlantLocation

ServiceofUnit

Size

ReferenceNo.

ProposalNo.Date

ItemNo.

Horz. ConnectedIn

2013/8/9

Rev

325.000x1499.98mm

TypeBESShell/Unit

1Parallel

1Series

10Surf/Unit(Gross/Eff)4.30/4.19m2

11

FluidAllocation

FluidName

1

Surf/Shell(Gross/Eff)4.30/4.19m2

PERFORMANCEOFONEUNIT

ShellSide

coolingwater

24700.1

TubeSide

T303w--T304

14FluidQuantity,Total

kg/hr

1106.90

15

16

17

18

19

Vapor(In/Out)Liquid

SteamWater

Noncondensables

24700.1

1106.90

1106.90

24700.1

Temperature(In/Out)

SpecificGravity

Viscosity

MolecularWeight,Vapor

C

20.00

0.9992

1.0214

20.81

0.9984

1.0025

136.70

0.8208

0.2837

108.00

0.8573

0.5017

mN-s/m2

24MolecularWeight,Noncondensables

SpecificHeat

ThermalConductivity

LatentHeat

InletPressure

Velocity

PressureDrop,Allow/Calc

FoulingResistance(min)

HeatExchangedW33TransferRate,Service34

35

Design/TestPressure

DesignTemperature

NoPassesperShell39CorrosionAllowance

kJ/kg-CW/m-CkJ/kgkPam/skPa

m2-K/W

20853.4

3.7946

0.5993

3.8000

0.6005

2.4844

0.1354

2.3116

0.1446

101.331

0.14

101.331

6.753e-2

2.897

0.368

0.000172

MTD(Corrected)

0.000200

101.5C

Actual

49.05W/m2-K

Clean

137.33W/m2-K

130.26W/m2-K

CONSTRUCTIONOFONESHELL

ShellSide

Sketch(Bundle/NozzleOrientation)

TubeSide1034.21/

136.70

2

kPaGC

1034.21/

136.70

1

325

mm

mmmmmm

40

41

42

ConnectionsSize&Rating

InOut

1@77.927

1@77.927

@

Thk(Avg)1.000mm

1@26.645

1@26.645

@

Length1.500m

1.5

m

Intermediate

OD19.000mm

Plain

ID325.000mm

TubeNo.

TubeType

Shell

ChannelorBonnet

Pitch35.000mm

Layout60

48

MaterialCARBONSTEEL

OD

mm

ShellCoverChannelCoverTubesheet-FloatingImpingementPlate

47Tubesheet-Stationary

48

49

50

51

52

53

54

55

56

57

58

59

60

61

62

FloatingHeadCoverBaffles-CrossBaffles-LongSupports-Tube

BypassSealArrangementExpansionJoint

Rho-V2-InletNozzleGaskets-ShellSide

-FloatingHeadCodeRequirementsWeight/Shell491.01Remarks:

None

TypeSINGLE-SEG.

%Cut(Diam)25.00 Spacing(c/c)300.000

Inlet665.501mm

SealTypeU-Bend

Tube-TubesheetJoint

Type

Type

BundleEntranceTubeSide

2071.95kg/m-s2

11.85

BundleExit 21.31

kg/m-s2

TEMAClassBundle57.59

FilledwithWater666.88

kg

ReprintedwithPermission(v6)

PropertiesProfileMonitor

Page10

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SIUnits

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

1PhysicalPropertiesProfile:HotTubeside(T303w--T304)

2Referencepressure,(kPa)3

Temperature,(C)

Heatduty/flowrate,(kJ/kg)

Weightfractionvapor7LiquidProperties

Density,(kg/m3)

Viscosity,(mN-s/m2)

Thermalconductivity,(W/m-C)

Enthalpy,(kJ/kg)

Specificheat,(kJ/kg-C)13Surfacetension,(mN/m)

(P1=101.331)

(P)

1

1

1

1

136.70

0.0000

0.0000

2

134.18

6.1998

0.0000

3

131.63

12.5000

0.0000

4

129.08

18.6998

0.0000

5

126.50

25.0000

0.0000

6

123.91

31.1998

0.0000

7

121.30

37.5000

0.0000

8

118.68

43.7997

0.0000

9

116.03

50.0001

0.0000

10

113.37

56.2998

0.0000

1

1

1

1

1

1

1

1

820.480

0.2837

0.1354

-5031.7

2.4844

18.6510

0.000

0.0000

823.790

0.2973

0.1362

-5037.9

2.4684

18.9040

0.000

0.0000

827.100

0.3118

0.1370

-5044.2

2.4525

19.1590

0.000

0.0000

830.410

0.3273

0.1379

-5050.4

2.4366

19.4160

0.000

0.0000

833.730

0.3439

0.1387

-5056.7

2.4208

19.6730

0.000

0.0000

837.040

0.3618

0.1395

-5062.9

2.4051

19.9320

0.000

0.0000

840.350

0.3809

0.1404

-5069.2

2.3894

20.1930

0.000

0.0000

843.660

0.4015

0.1412

-5075.5

2.3738

20.4550

0.000

0.0000

846.980

0.4238

0.1421

-5081.7

2.3582

20.7180

0.000

0.0000

850.290

0.4477

0.1429

-5088.0

2.3426

20.9830

0.000

0.0000

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

Criticalpressure,(kPa)Latentheat,(kJ/kg)

PropertiesProfileMonitor

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SIUnits

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

1PhysicalPropertiesProfile:HotTubeside(T303w--T304)

2Referencepressure,(kPa)3

Temperature,(C)

Heatduty/flowrate,(kJ/kg)

Weightfractionvapor7LiquidProperties

Density,(kg/m3)

Viscosity,(mN-s/m2)

Thermalconductivity,(W/m-C)

Enthalpy,(kJ/kg)

Specificheat,(kJ/kg-C)13Surfacetension,(mN/m)

(P1=101.331)

(P)

1

1

1

11

110.70

62.5001

0.0000

12

108.00

68.7998

0.0000

1

1

1

1

1

1

1

1

853.610

0.4736

0.1438

-5094.2

2.3271

21.2490

0.000

0.0000

856.930

0.5017

0.1446

-5100.5

2.3116

21.5160

0.000

0.0000

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

Criticalpressure,(kPa)Latentheat,(kJ/kg)

PropertiesProfileMonitor

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SIUnits

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

1PhysicalPropertiesProfile:ColdShellside(coolingwater)

2Referencepressure,(kPa)3

Temperature,(C)

Heatduty/flowrate,(kJ/kg)

Weightfractionvapor7LiquidProperties

Density,(kg/m3)

Viscosity,(mN-s/m2)

Thermalconductivity,(W/m-C)

Enthalpy,(kJ/kg)

Specificheat,(kJ/kg-C)13Surfacetension,(mN/m)

(P1=101.331)

(P)

1

1

1

1

20.81

-15873

0.0000

2

20.52

-15874

0.0000

3

20.30

-15875

0.0000

4

20.00

-15876

0.0000

1

1

1

1

1

1

1

1

997.990

1.0025

0.6005

-15873

3.8000

73.4990

0.000

0.0000

998.270

1.0093

0.6000

-15874

3.7980

73.5570

0.000

0.0000

998.480

1.0145

0.5997

-15875

3.7966

73.6010

0.000

0.0000

998.770

1.0214

0.5993

-15876

3.7946

73.6590

0.000

0.0000

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

Criticalpressure,(kPa)Latentheat,(kJ/kg)

StreamProperties

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WingteamHeatExchange

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

HotTubesideFluid

Fluidname

Temperature

Pressure

Weightfractionvapor

Inlet

Outlet

T303w--T304

(C)

(kPa)

(--)

136.70

101.331

0.0000

108.00

100.963

0.0000

6

7Density

VaporProperties

(kg/m3)(mN-s/m2)

(W/m-C)

(kJ/kg-C)

(--)

--

--

--

--

--

--

--

--

--

--

Viscosity

Conductivity

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

HeatcapacityMolecularweight

LiquidProperties

DensityViscosityConductivityHeatcapacity

MolecularweightLatentheatSurfacetension

(kg/m3)(mN-s/m2)

(W/m-C)

(kJ/kg-C)

(--)

(kJ/kg)(mN/m)

820.480

0.2837

0.1354

2.4844

0

--18.6510

Liquid

856.930

0.5017

0.1446

2.3116

0

--21.5160

Liquid

MolarComposition

Vapor

K-Value

Vapor

K-Value

StreamProperties

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Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

ColdShellsideFluid

Fluidname

Temperature

Pressure

Weightfractionvapor

Inlet

Outlet

coolingwater

(C)

(kPa)

(--)

20.00

101.331

0.0000

20.81

98.434

0.0000

6

7Density

VaporProperties

(kg/m3)(mN-s/m2)

(W/m-C)

(kJ/kg-C)

(--)

--

--

--

--

--

--

--

--

--

--

Viscosity

Conductivity

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

HeatcapacityMolecularweight

LiquidProperties

DensityViscosityConductivityHeatcapacity

MolecularweightLatentheatSurfacetension

(kg/m3)(mN-s/m2)

(W/m-C)

(kJ/kg-C)

(--)

(kJ/kg)(mN/m)

998.770

1.0214

0.5993

3.7946

0

--73.6590

Liquid

997.990

1.0025

0.6005

3.8000

0

--73.4990

Liquid

MolarComposition

Vapor

K-Value

Vapor

K-Value

InputReprint

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SIUnits

Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

NOTE:Caseinputmodified.

ShellData

Valuesmaynotbeconsistentwithotheroutputreports.

3

4

5

6

7

8

9

10

11

12

ServicetypeTEMAtypeRunmode

Hotfluidlocation

NumberofshellsinseriesNumberofshellsinparallelShellinsidediameter

Flowin1sttubepassTrainflowdirection

GenericShellandTube

BES

RatingTubeside

1

1

325.000mmCountercurrentCountercurrent

ReboilerData

Reboilertype

Inletpressurelocation16

17TubeData

Nopipingspecified

Inletnozzle

18

19

20

21

22

23

24

25

26

27

28

29

Tubetype

TubeoutsidediameterTubewallthicknessTubepitch

TubepitchratioTubepassespershellTubepattern

NumberoftubespershellTubecountmethod

TubelengthTubematerial

Plain

19.000mm

1.000mm

35.000mm1.842

2

60degrees

48

Rigorous

1.500mCarbonsteel

30TubepassArrangementData

31

32

33

34

ForcesymmetriclayoutForcecleaninglanes

Tubestoremovefortierods

NoNoCalculated

35BaffleData

36

37

38

39

40

41

42

BaffletypeBaffleorientation

BafflecutpercentCentralbafflespacingVariablebafflespacingWindowcutfrombaffles

SinglesegmentalProgramsets

25%shellID

300.000mmNo

No

43ClearanceData

44

45

46

47

48

49

50

NumberofsealstrippairsBaffleclearancetypeBlockAstream

BlockEstreamBlockFstream

Numberofpasslanesealrods

Calculated

TEMA

NoNoNo

Calculated

InputReprint

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Rating-HorizontalMultipassFlowTEMABESShellWithSingle-SegmentalBaffles

NOTE:Caseinputmodified.Valuesmaynotbeconsistentwithotheroutputreports.

NozzleData

3

4

5

6

7

8

9

10

11

12

13

14

NumberofshellsideinletnozzlesNumberofshellsideoutletnozzlesNumberoftubesideinletnozzlesNumberoftubesideoutletnozzlesRadialpositiononshellinletnozzle

LongitudinalpositiononshellofinletnozzleRadialpositiononshelloutletnozzleTubesideentrytype

TubesideinletpositionTubesideexittypeFrontheadlocation

1

1

1

1

BottomAtrearheadProgramdecides

RadialFronthead

Radial

Left

ImpingementData

Impingementdevicepresent

Impingementtype18

19OptionalGeometryData

IfrequiredbyTEMA

Circularplate

20

21

22

23

24

25

SmallexchangerTubesheettypeShellexpansionjoint

FloatingheadsupporttypeInsulatedlongitudinalbaffle

NoSingle

NoNone

No

26ProcessConditionsData

HotFluid

Sensibleliquid

0.3075

0

0

136.70

108.00

101.330

ColdFluid

Sensibleliquid

6.8611kg/s

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