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OutputSummary
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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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WingTeam
SIUnits
XistEVer.6.00 2013/8/912:12SN:Vals100+
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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XistEVer.6.002013/8/912:12SN:Vals100+
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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WingTeam
XistEVer.6.00 2013/8/912:12SN:Vals100+
Wingteam
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
Page5
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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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ZJUT
WingTeam
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Wingteam
SIUnits
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
Page11
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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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SIUnits
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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SIUnits
WingteamHeatExchange
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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WingteamHeatExchange
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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WingteamHeatExchange
SIUnits
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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