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TEMASheet
HeatExchangerSpecificationSheet
1
Company:
2
Location:
3
ServiceofUnit: OurReference:
4
ItemNo.: YourReference:
5
Date: RevNo.: JobNo.:
6
Size7.2441-118.1102 in Type: BEM Horizontal Connectedin:2 parallel 1 series
7
Surf/unit(eff.) 14355.9 ft2 Shells/unit 2 Surf/shell(eff.) 7178 ft2
8
PERFORMANCEOFONEUNIT
9
Fluidallocation
ShellSide
TubeSide
10
Fluidname
217
2
11
Fluidquantity,Total lb/h
47778
24432
12
Vapor(In/Out) lb/h
47778
47778
24432
24432
13
Liquid lb/h
0
0
0
0
14
Noncondensable lb/h
0
0
0
0
15
16
Temperature(In/Out) °C
38.47
71.95
300
292.01
17
Dew/Bubblepoint °F
18
Density Vapor/Liquid b/ft3
0.069/
0.055/
0.003/
0.003/
19
Viscosity cp
0.0107/
0.0118/
0.0139/
0.0138/
20
Molecularwt,Vap
26.04
26.04
2.02
2.02
21
Molecularwt,NC
22
Specificheat BTU/(lb-F)
0.4141/
0.4325/
3.4738/
3.4737/
23
Thermalconductivity BTU/(ft-h-F)
0.014/
0.016/
0.171/
0.169/
24
Latentheat BTU/lb
25
Pressure(abs) kPa
110
96.659
100
94.3
26
Velocity(Mean/Max) m/s
20.3/31.9
136.29/139.4
27
Pressuredrop,allow./calc. kPa
30
13.341
30
5.7
28
Foulingresistance(min) m2-K/W
0.00093
0.00093 0.00123Aobased
29
Heatexchanged 1220973 BTU/h MTD(corrected) 432.79 °F
30
Transferrate,Service 0.2 Dirty 6.66 Clean 8.88 BTU/(h-ft2-F)
31
CONSTRUCTIONOFONESHELL
Sketch
32
ShellSide
TubeSide
2
33
Design/Vacuum/testpressure psi
43.51/ /
43.51/ /
34
Designtemperature °F
197.6
608
35
Numberpassespershell
1
1
36
Corrosionallowance in
0.125
0.125
37
Connections
In in
1 12 / -
1 15.25/ -
38
Size/Rating
Out
1 12 / -
1 15.25/ -
39
ID
Intermediate
/ -
/ -
40
TubeNo.969 OD 0.9843TksAverage0.0591 inLength3000 mmPitch32 mm
41
TubetypeLowfintube 19 #/inMaterial CarbonSteel
Tubepattern 60
42
ShellCarbonSteel ID1200 OD1226 mm
Shellcover -
43
Channelorbonnet CarbonSteel
Channelcover -
44
Tubesheet-stationary CarbonSteel -
Tubesheet-floating -
45
Floatingheadcover -
Impingementprotection None
46
Baffle-crossCarbonSteel Type Singlesegmental Cut(%d) 15.09 HoriSpacing:c/c300 mm
47
Baffle-long- SealType
Inlet 25.3927 in
48
Supports-tube U-bend 0 Type
49
Bypassseal Tube-tubesheetjoint Expandedonly(2grooves)(App.A'i')
50
Expansionjoint - Type None
51
RhoV2-Inletnozzle 1028 Bundleentrance277 Bundleexit 284 lb/(ft-s2)
52
Gaskets-Shellside - Tubeside FlatMetalJacketFibe
53
Floatinghead -
54
Coderequirements ASMECodeSecVIIIDiv1 TEMAclassR-refineryservice
55
Weight/Shell 16903.5 Filledwithwater26961.2 Bundle 10911.3 lb
56
Remarks
57
58
OverallSummary
1
Size 47.2441 X118.1102 in Type BEMHor Connectedin 2parallel 1 series
2
Surf/Unit(gross/eff/finned) 4915.1 / 4693.9 /14355.9ft2Shells/unit 2
3
Surf/Shell(gross/eff/finned) 2457.6 / 2346.9 / 7178ft2
4
Rating/Checking PERFORMANCEOFONEUNIT
5
ShellSide TubeSide
HeatTransferParameters
6
ProcessData In Out In Out
Totalheatload BTU/h 1220973
7
Totalflow lb/h 47778 24432
Eff.MTD/1passMTD °F432.79/432.83
8
Vapor lb/h47778 47778 24432 24432
Actual/Reqdarearatio-fouled/clean 33.89/ 45.17
9
Liquid lb/h 0 0 0 0
10
Noncondensable lb/h 0 0
Coef./Resist. W/(m2-K) m2-K/W %
11
Cond./Evap. lb/h 0 0
Overallfouled 115.7 0.00864
12
Temperature °C38.47 71.95 300 292.01
Overallclean 154.1 0.00649
13
Dew/Bubblepoint °F
Tubesidefilm 268.5 0.00372 43.09
14
Quality 1 1 1 1
Tubesidefouling 814.6 0.00123 14.2
15
Pressure(abs) kPa 110 96.659 100 94.3
Tubewall 24438.1 4E-05 0.47
16
DeltaPallow/cal kPa 30 13.341 30 5.7
Outsidefouling 1075.3 0.00093 10.76
17
Velocity m/s25.04 31.44 133.32 139.4
Outsidefilm 367.4 0.00272 31.48
18
LiquidProperties
ShellSidePressureDrop psi %
19
Density lb/ft3
Inletnozzle 0.13 6.59
20
Viscosity cp
InletspaceXflow 0.2 10.48
21
Specificheat BTU/(lb-F)
BaffleXflow 1.16 59.94
22
Therm.cond. BTU/(ft-h-F)
Bafflewindow 0.11 5.66
23
Surfacetension lbf/ft
OutletspaceXflow 0.22 11.43
24
Molecularweight
Outletnozzle 0.11 5.9
25
VaporProperties
Intermediatenozzles
26
Density lb/ft30.069 0.055 0.003 0.003
TubeSidePressureDrop psi %
27
Viscosity cp0.0107 0.0118 0.0139 0.0138
Inletnozzle 0.3 36.06
28
Specificheat BTU/(lb-F)0.4141 0.4325 3.4738 3.4737
Enteringtubes 0.03 3.35
29
Therm.cond. BTU/(ft-h-F)0.014 0.016 0.171 0.169
Insidetubes 0.3 36.75
30
Molecularweight 26.04 26.04 2.02 2.02
Exitingtubes 0.05 5.53
31
Two-PhaseProperties
Outletnozzle 0.15 18.3
32
Latentheat BTU/lb
Intermediatenozzles
33
HeatTransferParameters
Velocity /Rho*V2 ft/s lb/(ft-s2)
Shellnozzleinlet 121.63 1028
ShellbundleXflow 82.14 103.14
Shellbafflewindow 83.36 104.67
Shellnozzleoulet 155.46 1314
Shellnozzleinterm
ft/s lb/(ft-s2)
Tubenozzleinlet 1013.32 2711
Tubes 437.39457.36
Tubenozzleoutlet 1071.6 2867
Tubenozzleinterm
34
ReynoldsNo.vapor 64611.17 58572 7660.447734.51
35
ReynoldsNo.liquid
36
PrandtlNo.vapor 0.79 0.78 0.69 0.69
37
PrandtlNo.liquid
38
HeatLoad BTU/h BTU/h
39
Vaporonly 1220973 -1220973
40
2-Phasevapor 0 0
41
Latentheat 0 0
42
2-Phaseliquid 0 0
43
Liquidonly 0 0
44
Tubes Baffles Nozzles:(No./OD)
45
Type Lowfintube Type Singlesegmental ShellSide TubeSide
46
ID/OD in0.8183 / 0.9843 Number 6 Inlet in1 /12.75 1 / 16
47
Lengthact/eff ft9.8425 / 9.3994 Cut(%d) 15.09 Outlet 1 /12.75 1 / 16
48
Tubepasses 1 Cutorientation H Intermediate / /
49
TubeNo. 969 Spacing:c/c mm 300 Impingementprotection None
50
Tubepattern 60 Spacingatinlet in25.3927
51
Tubepitch mm 32 Spacingatoutlet in28.3455
52
Insert None
53
Vibraionproblem(HTFS/TEMA) No / RhoV2violaion No
33
32
32
32
32
10
418
418
10
SettingPlan
ViewsonarrowA
A
217.3228Overall
T1
25.2913 24.315 12.0079 93.8976 265118
T1 S2
S2
S1
S1 T2
24.315 23.965228 70.8661 2.9528
PullingLength 69
T2
5.9055 5.9055
2Bolts 2Bolts
Fixed Sliding
NozzleData
DesignData
Units
Shell
Channel
Notes:
Filename:E0109
AspenShell&TubeverificationfileServiceofUnit:
ItemNo.:
Date:RevNo.:
Ref
OD
Wall
Standard
Notes
DesignPressure
psi
43.51
43.51
S1
12.75"
0.375"
Slipon
DesignTemperature
°F
197.6
608
S2
12.75"
0.375"
Slipon
FullVacuum
0
0
T1
16.0"
0.375"
Slipon
CorrosionAllowance
in
0.125
0.125
T2
16.0"
0.375"
Slipon
TestPressure
psi
CompanyName
City,State
NumberofPasses
1
1
Radiography
0
0
PWHT
0
0
InternalVolume
ft3
66.1361
128.3136
Scale:
Rev:
Date:
Description
Dwg.
Chk.
Appd
0
SettingPlan
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