00

435.21368.3

R - refinery service

Flat Metal Jacket Fibe

ASME Code Sec VIII Div 1Flat Metal Jacket FibeFlat Metal Jacket Fibe

Single segmentalSS 304-

Exp.-

mm

Company:Location:Service of Unit: Our Reference:Item No.: Your Reference:Date: Rev No.: Job No.:

736 4880 AES 1 198.7 m? 1 98.7 m?

water in->water out 32->33187176 55000kg/h

0 0kg/h 0 0187176 187176kg/h 55000 55000

kg/h 0

25 39.09?C 98.33 46.43100 100?C

kg/m?cp

kJ/(kg K)W/(m K)

kJ/kg1.01325 31.28325bar

1.06 1.04m/s0.3798 0.19391bar 0.36953 0.25007

0.00022 0.0002m? K/WkW3097.7 ?C33.34

941.3 941.6 W/(m? K)1661.4

bar 3575 135?C1 60 0mm

101.6 -203.2 - 88.9 -

- -

mm

4941 7277.2 kg2256.8

1037 1048 kg/(m s?)1060

23.31mmmm

276 31.2525 2 4.88mm m mmPlain SS 304 30

mm746.6SS 304SS 304SS 304 None

SS 304SS 304SS 304

SS 304

Hor

H

Avg

-

736.6

0 0

0.81934 31.03318

3

1007.34 996.65 920.19 965.450.8904 0.6629 0.5751 1.1911

4.202 4.228 3.928 3.8970.611 0.6304 0.5988 0.5685

T1

T2 S1S2

0.00024

#/m

Nominal

254 -11

11

None

Us

Size/rating

Ao based

Vapor/Liquid

--

Remarks

TEMA class

Intermediate

BundleFilled with waterWeight/ShellCode requirements

Floating headTube SideGaskets - Shell side

Bundle exitBundle entranceTypeExpansion jointTube-tubesheet jointBypass seal

TypeU-bendSupports-tube

Impingement protectionTubesheet-floatingChannel cover

Floating head coverTubesheet-stationaryChannel or bonnet

OutIn

Surf/shell (eff.)Shells/unitSurf/unit(eff.)seriesparallelConnected inTypeSize

OD

Sketch

1234567

PERFORMANCE OF ONE UNIT8Fluid allocation9Fluid name10Fluid quantity, Total11

Vapor (In/Out)12Liquid13Noncondensable14

Temperature (In/Out)15

Dew / Bubble point16171819202122232425262728

Heat exchanged29Transfer rate, Service30

CONSTRUCTION OF ONE SHELL31

Design/vac/test pressure:g32

Design temperature33

Number passes per shell34

Corrosion allowance35

Connections363738

Tube No.39

Tks-4041

Length

42

Pitch

43

Tube type

44

Material

45

Shell

46

ID

47

OD

48

Shell Side

49

Tube Side

50

Shell cover

51

Tube pattern

52

Baffle-cross

53

Type

54

Cut(%d)

55

Spacing: c/c

56

Baffle-long

57

Seal type

58

Inlet

RhoV2-Inlet nozzle

Shell Side Tube Side

Fouling resistance (min)Pressure drop, allow./calc.VelocityPressure (abs)Latent heatThermal conductivitySpecific heatMolecular wt, NCMolecular wt, VapViscosityDensity

MTD correctedDirty Clean

Heat Exchanger Specification Sheet

Heat Exchanger Thermal Design Shell&Tube V Page 2File: Printed: 6/9/2014 at 7:09:49 PM

187176

0

55000

0

dynes/cm0.611 0.6304

0.8904 0.66294.202 4.228

1007.34 996.65

0 00 0187176 187176 55000 55000

W/(m? K)

kg/h

?C

m/s

kg/m?cp

kJ/(kg K)W/(m K)

23845.32 32031.63

6.12 4.45

25 39.09 98.33 46.43

1.01325 0.81934 31.28325 31.033180.25007

0.84 0.85 1.04 0.99

0 0bar

kPa

kPa

kg/m?cp

kJ/(kg K)W/(m K)

kJ/kg

4200

4504.57341.4

6428.8

941.61661.43224.2

0.00024

0.000220.00014

0.00016

0.001060.0006

0.0003122.42

20.912.83

14.65

29.2

m? K/W

1.8981.541

18.0222.1551.443

6.1571.92

8.6

7.57

5.76

0 0

0.5988 0.5685

0.5751 1.19113.928 3.897

920.19 965.45

35014.44 16906.12

3.77 8.16

0 0kW

0 00 0

33.34?C 37.21

0.8521.809

10.6673.0191.762

9.3455.0415.58

4.39

9.091.268 6.54

m/s

1.04

1.010.841.04

1.62

2.02

2.48

18.02 18.02 22.93 22.93

0 03097.7 -3097.7

0 0

kg/(m s?)1037

2604

3760

5942

3097.7kW

1 1.76

mm

m

mm

11

11

627630

4.88

31.25

368.3435.21435.21

23.31

mm

mm

mm

H

1Hor736.6 14880 AES

114.3101.6

273.05219.08

Single segmental

105.81

98.798.7105.8 m?

mm

m?

114.5534

21 25Plain

mm

0.193910.3798 0.36953

100 100

None

NoNo No

0.851.06

0.99

Simulation

None

kg/hkg/hkg/h

?C

bar

kWm/s kg/(m s?)

Insert

//

/ Rho*V2

/Vibration problem RhoV2 violation

Impingement protection

//

Dew / Bubble point

/

x

//

Surf/Shell (gross/eff/finned)Shells/unit

seriesparallelConnected inType

Cut orientation//

//

//Tube SideShell Side

Spacing at outlet

Cut(%d)

Spacing: c/cSpacing at inlet

NumberType

Tube patternTube pitch

Length act/effTube passesTube No.

Actual/Reqd area ratio - fouled/clean

Total heat loadHeat Transfer Parameters

2-Phase liquidLiquid only

Molecular weight

Tube nozzle intermTube nozzle outletTubesTube nozzle inlet

Shell nozzle intermShell nozzle outletShell baffle window

VelocityShell nozzle inletShell bundle Xflow

Intermediate nozzle

Eff. MTD/ 1 pass MTD

Latent heat2-Phase vaporVapor only

Intermediate nozzle

/

Inlet space XflowInlet nozzle

1234

789

1011121314

Size

PERFORMANCE OF ONE UNIT

Total flowVaporLiquidNoncondensableCond./Evap.Temperature

2221201918171615 Quality

Pressure (abs)DeltaP allow/calVelocity

Liquid PropertiesDensityViscosity

3029282726252423 Specific heat

Therm. cond.Surface tension

Vapor PropertiesDensityViscositySpecific heat

3837363534333231 Therm. cond.

Latent heat

Molecular weight

Reynolds No. vaporReynolds No. liquidPrandtl No. vapor

4645444342414039

Prandtl No. liquid

5453525150494847

TubesTypeID/OD

65

Shell Side

Tube side foulingTube wallOutside foulingOutside film

Overall fouledOverall clean

Tube Side Pressure DropInlet nozzleEntering tubesInside tubesExiting tubesOutlet nozzle

Shell Side Pressure Drop

Baffle XflowBaffle windowOutlet space XflowOutlet nozzle

Heat Load

Coef./Resist.

Tube side film

Tube SideIn Out In Out

Surf/Unit (gross/eff/finned)

555657

Baffles

OtherOutletInlet

Nozzles: (No./OD)

%

Two-Phase Properties

Heat Transfer Parameters

Process Data

%

%

Heat Exchanger Thermal Design Shell&Tube V Page 3File: Printed: 6/9/2014 at 7:09:50 PMBasic Geometry

mm

736.6

11Hor

AES

736.6746.6 760.6

708.02732.02

64.88m276

Plain25mm

31.25mm30

368.3mm

Single segmental11

435.21mm

Shell Side Tube SideNozzle type Inlet Outlet Inlet OutletNumber of nozzles 1 1 1 1Actual outside diameter mm 273.05 219.08 114.3 101.6Inside diameter mm 254.51 202.72 102.26 90.12Height under nozzle mm 77.98 77.98Dome inside diameter mmVapor belt inside diameter mmVapor belt inside width mmVapor belt slot area mm?Impingement protection No

impingementNo

impingementDistance to tubesheet mm 4365 335

mm

Spacing at inletSpacing (center-center)Baffle numberBaffle type

Tube patternTube pitchTube O.D.Tube type

Tube number (calcs.)Tube length actualTube passes

Unit Configuration

ArrangementPosition

Rear headFront headKettleShellOutside diameterInside Diameter

serpar

Exchanger Type

Heat Exchanger Thermal Design Shell&Tube V Page 4File: Printed: 6/9/2014 at 7:09:50 PMTubes

Default#/mmm

mm

mm

mm

3031.25

2

25

74.53

4.88

mm

mm

mm

m

1.19

16SS 304

Plain0

276

W/(m K)

214.5534

mm

m

#/mmm

mm

mm

mm

0mm

mm

mm

mm

mm

74.53

Tube number

Internal enhancementExternal enhancementPatternPitchArea ratio: Ao/AiWall thickness

Outside diameter

High Fin FrequencyHigh Fin Thick

High Fin Tip DiameterHigh Fin Type

Type

Other (high) fins

Rear TubesheetThickness

Tube inside diameter under fins

Fin numberFin thicknessFin heightFin spacingCut and twist length

Longitudinal finsLow fins

Fin densityFin heightFin thicknessTube root diameterTube wall thickness under fin

Inside diameter

Front TubesheetThicknessTube length effectiveTube length actual

Thermal conductivityMaterial

Number of tubes plugged

Tubes

Heat Exchanger Thermal Design Shell&Tube V Page 5File: Printed: 6/9/2014 at 7:09:50 PMBaffles

7.94435.21435.21

368.311

mmmm

mm

mm

H

YesSingle segmental

135.5

512.74mm684.26mm

mm

mm

0.794.76

mm

mm

17.71

23.3125

Baffle spacing mmBaffle cut percent, outerBaffle cut percent, innerNumber of baffle spacesBaffle region length mmBaffle cut area percent, outerBaffle cut area percent, inner

VariableBaffles

Baffle cut: inner / outer / interm

Baffle hole - tube od diam clearanceShell id - baffle od diam clearance

Spacing at center of H shellSpacing at central in/out for G,H,I,J shells

End length at rear headEnd length at front head

Nominal (% diameter)

Baffles

TypeTubes in window Actual (% diameter)

Actual (% area)Cut orientation

NumberSpacing (center-center)Spacing at inletSpacing at outlet Thickness

Tube rows in baffle windowTube rows in baffle overlap

Supports Misc. Baffles

Yes0

0

0

0mm

mm

mm

mm

000

NoSpecial support at inlet nozzle

Support blanking baffleSupports between bafflesSupports in endspace at rear headSupports in endspace at front head

Supports at U-bend

ThicknessWindow length at front headWindow length at centerWindow length at rear head

Longitudinal BaffleSupports-tube

Supports for K, X shellsSupports at center of H shellSupports at each G,H,J shell inlet and I shell outlet

Heat Exchanger Thermal Design Shell&Tube V Page 6File: Printed: 6/9/2014 at 7:09:50 PMBundle

m?

mm

mm

No

695.32

15.8815.88

4

Nonemm

Exp.3mm3mm

23.85mm

77.9822.8622.86

mm

26.09

98.700

mm 41.28

6Mixed (H)

Standard (horizontal)

12.7mm

Undefined

6

mm

mm

mm

mm

98.7105.8

m?m?m?m?

Horizontal pass lane widthVertical pass lane widthInterpass tube alignment

Outer tube limit

Sealing strips (pairs)

Tie rod number

Impingement protectionImpingement distance

Tube to tubesheet jointTube projection from front tshtTube projection from rear tsht

Shell ID to center 1st tube rowFrom topFrom bottomFrom rightFrom Left

Deviation in tubes/pass

Bare tube area per shellFinned area per shellU-bend area per shell

Shell id - bundle otl diam clearance

Bundle

Tube passesTube pass layoutTube pass orientation

Tie rod diameter

U-bend orientation

Impingement plate diameterImpingement plate widthImpingement plate lengthImpingement plate thickness

Effective surface area per shellGross surface area per shell

Enhancements

None

mm

mm

hiTRAN part number

Internal enhancements

Tube insert type

Twisted tape thicknessTwisted tape 360 deg twist pitch

Heat Exchanger Thermal Design Shell&Tube V Page 7File: Printed: 6/9/2014 at 7:09:50 PMSetting Plan

150 2 Bolts

Fixed

75

64716

2

150 2 BoltsSliding

7564

7 162

5873 Overall

319 243 335 4030

243 976 2928

Pulling Length 4420

T1

T2 S1S2

A

Nozzle DataRef OD Wall Standard NotesS1 273 mm 9.3 mm 150 ANSI Slip onS2 219 mm 8.2 mm 150 ANSI Slip onT1 114 mm 6. mm 150 ANSI Slip onT2 102 mm 5.7 mm 150 ANSI Slip on

Empty 4941 kg

Flooded 7277 kg

Bundle 2257 kg

Weight Summary

Internal Volume m? 2.1569 0.2931PWHTRadiographyNumber of Passes 1 6Test Pressure barCorrosion Allowance mm 0. 0.Full VacuumDesign Temperature C 75. 135.Design Pressure bar 3. 35.

Design Data Units Shell Channel

Customer Specifications

Design CodesASME Section VIII Div. 1

TEMA R

Date: Rev No.: Job No.:Item No.: Your Reference:Service of Unit: Our Reference:Location:Company:

Revision Date6/9/2014

Dwg. Chk. App.

Aspen Shell & Tube Exchanger

Setting Plan

AES 737 - 4880

Drawing Number

530

530

T1

T2

523

S1 S2

560

Views on arrow A

Heat Exchanger Thermal Design Shell&Tube V Page 8File: Printed: 6/9/2014 at 7:09:50 PMTube Layout

331.

95 m

m27

7.82

m

m

Company:Location:Service of Unit: Item No.:

Tube Layout

Aspen Shell & Tube

Drawing Number

Design CodesASME Code Sec VIII Div 1TEMA R - refinery service

Customer Specifications

Revision Date Dwg. App.6/9/2014

Shell inside diameter mm 736.6

Front head inside diameter mm 736.6

Outer tube limit mm 695.325

Tube number (calcs.) 276Tube number (layout) 370Tube length mm 4880.

Tube O.D. mm 25.

Tube pitch mm 31.25

Tube pattern 30

Tube passes 6

Tie rod number 6

Tie rod diameter mm 12.7

Sealing strips (pairs) 4Baffle type Single segmental

Centre to outer baffle cut mm 196.6289

Centre to inner baffle cut

Impingement protection None

Shell Side Inlet Nozzle Inside Diameter mm 254.508

Shell Side Outlet Nozzle Inside Diameter mm 202.7174

55

57 57

61 61

79

25.00

31.2500

Heat Exchanger Thermal Design Shell&Tube V Page 9File: Printed: 6/9/2014 at 7:09:50 PMCost/Weight

88657

Dollar(US)kg

39973

3262216063

49417277.2

2256.8

1093.11110.6480.4

88657Total cost (all shells)

Cost dataWeights

Total cost (1 shell)

Labor cost

Material cost (except tubes)Tube material cost

Total weight - emptyTotal weight - filled with water

Bundle

ShellFront headRear headShell cover