ATV Primary Heat Exchanger

Heat Exchanger Thermal Design Shell&Tube V7.3.1 CP1

File: MOLVE.EDR Date: 24.3.2014. Time: 19:18:13

Description

Company:

Location:

Service of Unit: Our Reference:

Item No.: Your Reference:

Date: Rev No.: Job No.:

Heading

Remarks

Application Options

Liquid, no phase change

Set default

Liquid, no phase change

Set default

Shell side

Rating / Checking

Set default

Set default

US

Set default

Advanced method

Application

Condenser type

Application

Vaporizer type

Location of hot fluid

Calculation mode

Simulation calculation

Simulation calculation

Select geometry based on this dimensional standard

Thermosiphon circuit calculation

Calculation Method

Process Data

3,8727 14,9408

75 25 17,96 55

1 0,89 35 34,55

0,11 0,49987

0 0

kg/s

°C

bar

bar

m˛ K/W

Heat load Heat load

kW

0 0 0 0

bar

0 0bar

Geothermal fluid from production well->Geothermal fluid in injection welluid in injection well

Mass flow rate (total)

Temperature

Operating pressure (absolute)

Allowable pressure drop

Fouling resistance

Hot Side Cold Side

Heat exchanged

Heat Load Balance Options

In OutIn Out

Vapor mass fraction

Pressure at liquid surface in column

Estimated pressure drop

Fluid name



Hot Side Databank

Ideal

Integral

User specified properties

Weight flowrate or %

Pressures

bar

1

1

BL1(273)

BL1(313)

BL1(314)

Vapor-Liquid-Liquid

B-JAC calculation method

B-JAC calculation type

Hot side composition specification

Aspen Plus or Aspen Properties run file

Physical property package

Aspen property method

Aspen free-water method

Aspen water solubility

Aspen flash option

Hot Side - Component

Components Composition Component type

Hot Side - Stream Properties

Temperature Specificenthalpy

Vapor massfraction

°C kJ/kg

25 0 0

29,56 19,7 0

34,11 39,3 0

38,67 59 0

43,22 78,6 0

47,78 98,3 0

52,32 117,9 0

56,87 137,6 0

61,41 157,3 0

65,95 176,9 0

70,48 196,6 0

75 216,2 0

Hot Side - Stream Properties


Vapor massfraction

°C kJ/kg

25 0 0

29,56 19,7 0

34,11 39,3 0

38,67 59 0

43,22 78,6 0

47,78 98,3 0

52,32 117,9 0

56,87 137,6 0

61,41 157,3 0

65,95 176,9 0

70,48 196,6 0

75 216,2 0



Hot Side - Liquid Properties

TemperatureLiquid specificheat

Liquid thermalcond.

Liquidviscosity

Liquiddensity

Liquid surfacetension

°C kJ/(kg K) W/(m K) mPa s kg/mł N/m

25 4,313 0,611 0,8904 1007,34 0,0721

29,56 4,313 0,6176 0,8049 1003,9 0,0713

34,11 4,314 0,6239 0,7315 1000,45 0,0705

38,67 4,315 0,6298 0,6683 996,97 0,0697

43,22 4,317 0,6355 0,6133 993,48 0,0689

47,78 4,32 0,6408 0,5654 989,97 0,0681

52,32 4,323 0,6458 0,5233 986,44 0,0673

56,87 4,327 0,6504 0,4862 982,88 0,0665

61,41 4,331 0,6548 0,4533 979,31 0,0657

65,95 4,336 0,6589 0,424 975,72 0,0649

70,48 4,342 0,6627 0,3978 972,11 0,0641

75 4,349 0,6662 0,3743 968,47 0,0633

Hot Side - Liquid Properties


Liquid thermalcond.

Liquidviscosity

Liquiddensity



25 4,313 0,611 0,8904 1007,34 0,0721

29,56 4,313 0,6176 0,8049 1003,9 0,0713

34,11 4,314 0,6239 0,7315 1000,45 0,0705

38,67 4,315 0,6298 0,6683 996,97 0,0697

43,22 4,317 0,6355 0,6133 993,48 0,0689

47,78 4,32 0,6408 0,5654 989,97 0,0681

52,32 4,323 0,6458 0,5233 986,44 0,0673

56,87 4,327 0,6504 0,4862 982,88 0,0665

61,41 4,331 0,6548 0,4533 979,31 0,0657

65,95 4,336 0,6589 0,424 975,72 0,0649

70,48 4,342 0,6627 0,3978 972,11 0,0641

75 4,349 0,6662 0,3743 968,47 0,0633

Hot Side - Vapor Properties

TemperatureVapor specificheat

Vapor thermalcond.

Vaporviscosity

Vapor density Vaporweight

°C kJ/(kg K) W/(m K) mPa s kg/mł

25

29,56

34,11

38,67

43,22

47,78

52,32

56,87

61,41

65,95

70,48

75



Hot Side - Vapor Properties


Vapor thermalcond.

Vaporviscosity


°C kJ/(kg K) W/(m K) mPa s kg/mł

25

29,56

34,11

38,67

43,22

47,78

52,32

56,87

61,41

65,95

70,48

75

Hot Side - 2-Phase liquid

Temperature Liquid 2heat

Liquid 2cond.

Liquid 2viscosity

Liquiddensity

Liquid 2tension


25

29,56

34,11

38,67

43,22

47,78

52,32

56,87

61,41

65,95

70,48

75

Hot Side - 2-Phase liquid


Liquid 2cond.

Liquid 2viscosity

Liquiddensity

Liquid 2tension


25

29,56

34,11

38,67

43,22

47,78

52,32

56,87

61,41

65,95

70,48

75



Cold Side Databank

User specified properties

Weight flowrate or %

Ideal

Pressures

bar

35

35

BL1(316)

BL1(317)

BL1(318)

Vapor-Liquid-Liquid

B-JAC calculation methods

Aspen Plus or Aspen Properties run file

Cold side composition specification

Physical property package

Aspen flash option

Aspen water solubility

Aspen free-water method

Aspen property method

Cold Side - Component

Components Composition Component type

Cold Side - Stream Properties


Vapor massfraction

°C kJ/kg

17,96 0 0

21,58 5,1 0

25,15 10,2 0

28,68 15,3 0

32,15 20,4 0

35,58 25,5 0

38,95 30,6 0

42,27 35,7 0

45,54 40,8 0

48,75 45,9 0

51,9 51 0

55 56 0

Cold Side - Stream Properties


Vapor massfraction

°C kJ/kg

17,96 0 0

21,58 5,1 0

25,15 10,2 0

28,68 15,3 0

32,15 20,4 0

35,58 25,5 0

38,95 30,6 0

42,27 35,7 0

45,54 40,8 0

48,75 45,9 0

51,9 51 0

55 56 0



Cold Side - Liquid Properties


Liquid thermalcond.

Liquidviscosity

Liquiddensity



17,96 1,399 0,0887 0,2161 1245,98 0,0095

21,58 1,417 0,0869 0,2074 1233,28 0,0089

25,15 1,436 0,085 0,1993 1220,5 0,0085

28,68 1,456 0,0832 0,1916 1207,63 0,008

32,15 1,477 0,0813 0,1844 1194,66 0,0075

35,58 1,499 0,0795 0,1775 1181,58 0,007

38,95 1,522 0,0776 0,1709 1168,38 0,0066

42,27 1,547 0,0757 0,1647 1155,05 0,0062

45,54 1,573 0,0739 0,1587 1141,57 0,0057

48,75 1,6 0,072 0,1531 1127,93 0,0053

51,9 1,63 0,0701 0,1477 1114,1 0,0049

55 1,663 0,0682 0,1425 1100,06 0,0045

Cold Side - Liquid Properties


Liquid thermalcond.

Liquidviscosity

Liquiddensity



17,96 1,399 0,0887 0,2161 1245,98 0,0095

21,58 1,417 0,0869 0,2074 1233,28 0,0089

25,15 1,436 0,085 0,1993 1220,5 0,0085

28,68 1,456 0,0832 0,1916 1207,63 0,008

32,15 1,477 0,0813 0,1844 1194,66 0,0075

35,58 1,499 0,0795 0,1775 1181,58 0,007

38,95 1,522 0,0776 0,1709 1168,38 0,0066

42,27 1,547 0,0757 0,1647 1155,05 0,0062

45,54 1,573 0,0739 0,1587 1141,57 0,0057

48,75 1,6 0,072 0,1531 1127,93 0,0053

51,9 1,63 0,0701 0,1477 1114,1 0,0049

55 1,663 0,0682 0,1425 1100,06 0,0045

Cold Side - Vapor Properties


Vapor thermalcond.

Vaporviscosity


Diffusivity

°C kJ/(kg K) W/(m K) mPa s kg/mł m˛/s

17,96

21,58

25,15

28,68

32,15

35,58

38,95

42,27

45,54

48,75

51,9

55



Cold Side - Vapor Properties


Vapor thermalcond.

Vaporviscosity


Diffusivity

°C kJ/(kg K) W/(m K) mPa s kg/mł m˛/s

17,96

21,58

25,15

28,68

32,15

35,58

38,95

42,27

45,54

48,75

51,9

55

Cold Side - 2-Phase liquid


Liquid 2cond.

Liquid 2viscosity

Liquiddensity

Liquid 2tension


17,96

21,58

25,15

28,68

32,15

35,58

38,95

42,27

45,54

48,75

51,9

55

Cold Side - 2-Phase liquid


Liquid 2cond.

Liquid 2viscosity

Liquiddensity

Liquid 2tension


17,96

21,58

25,15

28,68

32,15

35,58

38,95

42,27

45,54

48,75

51,9

55



Exchanger Type

Normal

Expanded only (no groove)(App.A 'k')

None

B - bonnet bolted or integral with tubesheet

E - one pass shell

M - bonnet

Horizontal

Ellipsoidal

Yes

Ellipsoidal (M,P,S,T,W types)

Yes

Set default

Hub

Hub

Set default

Near rear head

336,55 355,6mm

mm

mm

mm

336,55

336,55

9,52 2 1

mm

42,86

42,86

mm

mm

3,18

3,18

mm

mm

9,52

9,52

Flange type - cold side

Flange type - hot side

Include expansion joint

Tubesheet type

Shell cover type

Rear cover welded to a cylinder

Rear cover type

Front cover welded to a cylinder

Front cover type

Exchanger position

Rear head type

Shell type

Front head type

Location of front head for vertical units

"E" shell flow direction (inlet nozzle location)

Shell(s)

Front head

Rear head

Kettle

ODID Thickness series parallel

Distance from U-bend center to shell cover

Front tubesheet thickness

Rear tubesheet thickness

Tube projection from front tubesheet

Tube projection from rear tubesheet

Tubes

mm

Plain

19,05

2,11

Average

30-Triangular

23,81

mm

mm

mm

mm

#/m

mm

mm

143

0

mm 6096 Carbon Steel

Smooth

As specified

2,11mm

mm

mm

mm

mm

mm

None

mm

mm

mm

Set default

None

mm

mm

3,18mm

60

UnspecifiedTube internal enhancement

Tube wall roughness

Twisted tape 360 degree twist pitch

Outside/Inside surface area ratio

Fin density

Fin thickness

Fin height

Tube pitch

Tube pattern

Wall specification

Tube wall thickness

Tube outside diameter

Tube type

Number of tubes (total)

Number of tubes plugged

Tube length Tube material

Tube surface

Tube cut angle (degrees)

Lowfin Tube type

Tube wall thickness under fin

Tube root diameter

Distance unfinned at baffle

Longitudinal fins per tube

Longitudinal fin height

Longitudinal fin thickness

Longitudinal root spacing

Tube insert type

Twisted tape thickness

Longitudinal fin cut and twist length

Twisted tube twist pitch

Shell type: within shroud (convert to)

Shroud inlet location

Shroud inlet gap length

Shroud outlet gap length

Shroud thickness

Skid bar angle (deg)



Baffles

Single segmental

37,74

Horizontal

mm

Yes

3,18mm

158,75mm

36

223,84mm

269,88mm

269,88mm

mm

mm

3,18mm

0,79mm

no

no

mm

mm

mm

mm

mm

Set default

mm

0

YesAlign baffle cut with tubes

Support/baffle to tangent of U-bend distance

Baffle cut orientation

Baffle cut (% of diam.) outer

Baffle type

Tubes are in baffle window

Baffle thickness

Baffle spacing center-center

Number of baffles

Baffle spacing at inlet

End length at front head (tube end to closest baffle)

End length at rear head (tube end to closest baffle)

Distance between baffles at central in/out for G,H,I,J shells

Distance between baffles at center of H shell

Baffle OD to shell ID diametric clearance

Baffle tube hole to tube OD diametric clearance

Special inlet nozzle support

Support or blanking baffle at rear end

Length of tube beyond support/blanking baffle

Number of extra supports for U-bends

Number of supports at center of H shell

Number of supports at inlet/outlet for G, H, I, J shells

Number of supports between central baffles

Number of supports at front head end space

Number of supports at rear head end space

Window length at rear head for F, G, H shells

Window length at front head for G, H shells

Window length at center for H shells

Baffle thickness

Percent leakage across longitudinal baffle

Multi-segmental baffle starting baffle

Longitudinal Baffle

Number of supports for K, X shells

Deresonating Baffles

Number of deresonating baffles

Largest deresonating baffle-baffle or baffle-shell distance

Baffles

Number of baffle spaces

Baffle spacing mm

Baffle cut percent, outer

Baffle cut percent, inner

Baffle cut percent,intermediate

One regionNumber of regions for variable baffle pitch

Variable baffle pitch: First to last pitch ratio



Bundle

Use Layout value (warning)

35,02

35,02

Standard symmetry

1

mm

mm

mm

9,55mm

15,88mm

Use existing layout

Ribbon (single band)

Normal bundle

30-Triangular

23,81mm

1

Standard (horizontal)

Undefined

15,88mm

15,88mm

12,7mm

323,85mm

mm

mm

0

0

Unaligned

Main input / Tube layout inconsistencies

Open distance at top of layout

Open distance at bottom of layout

Tube layout symmetry

Number of tie rods

Number of sealing strip pairs

Minimum U-bend diameter

Tie rod diameter

Spacer diameter

Tube layout option

Pass layout

Tube layout design

Tube pattern

Tube pitch

Tube passes

Pass layout orientation

Orientation of U-bends

Open distance on left side of layout

Open distance on right side of layout

Shell ID to outer tube limit diametric clearance

Outer tube limit diameter

Horizontal pass partition width

Vertical pass partition width

Number of horizontal pass partition lanes

Number of vertical pass partition lanes

Cleaning lane or tube alignment



Nozzles

-

Slip on Slip on

-

no

no

NozSizeSS

Nominal diameter mm

Actual OD mm 88,9 88,9 88,9

Actual ID mm 77,93 77,93 77,93

Wall thickness mm 5,49 5,49 5,49

Nozzle orientation Top Bottom Bottom

Distance to front tubesheet mm

Number of nozzles 1 1 1

Multiple nozzle spacing mm

Nozzle / Impingement type No impingement No impingement No impingement

Remove tubes below nozzle Equate areas Equate areas Equate areas

Maximum nozzle RhoV2 kg/(ms˛)Nozzle ignore options

NozSizeTS

Nominal diameter mm

Actual OD mm 168,28 101,6 101,6

Actual ID mm 154,05 90,12 90,12

Wall thickness mm 7,11 5,74 5,74

Nozzle orientation Bottom Top Top

Distance to tubesheet mm

Centerline offset distance mm

Maximum nozzle RhoV2 kg/(ms˛)Nozzle ignore options

Dome OD mm

Vapor belt diametric clearance mm

Vapor belt slot area m˛

Vapor belt axial length mm

unspecified

Set default

ID

Shell side nozzle flange rating

Shell side nozzle flange type

Shell Side Tube Side

Use separate outlet nozzles for hot side liquid/vapor flows

Use separate outlet nozzles for cold side liquid/vapor flows

Shell Side

Tube Side

Shell side nozzle location options

Location of nozzle at U-bend

Nozzle diameter displayed on TEMA sheet

Impingement protection

None

mm

mm

mm

mm

mm

mm

Impingement protection device

Impingement plate diameter

Impingement plate length (parallel to tube axis)

Impingement plate width (normal to tube axis)

Impingement plate thickness

Impingement plate distance in from shell ID

Impingement plate clearance to tube edge

Impingement plate perforated area %



Thermosiphon Piping

mm

mm

mm

Inlet circuit element

Internal diameter mm

Length (pipe) or Radius (arc) mm

Velocity heads (general element)

Elements in series

Elements in parallel

Outlet circuit element

Internal diameter mm

Length (pipe) or Radius (arc) mm

Velocity heads (general element)

Elements in series

Elements in parallel

Set default

Height of column liquid level

Height of heat transfer region inlet

Height of return line to column

Percent head loss in outlet pipe

Percent head loss in inlet pipe

Pipework loss calculation

Materials

Carbon Steel

Carbon Steel

Carbon Steel

Carbon Steel

Carbon Steel

Flat metal jacketed fiber

W/(m K)

kg/mł

N/mm˛

Gaskets - cold side

Gaskets - hot side

Tubesheet cladding - cold side

Tubesheet cladding - hot side

Tube material thermal conductivity

Tube material

Baffles

Double tubesheet (inner)

Tubesheet

Cylinder - cold side

Cylinder - hot side

Tube material density

Tube material modulus of elasticity

Specifications

ASME Code Sec VIII Div 1

Normal

R - refinery service

ASME

ANSI - American

3,44738

110

3,18

38,61066

93,33

3,18

bar

°C

bar

bar

mm

Spot Spot

Cold SideHot Side

Corrosion allowance

Test pressure (gauge)

Vacuum design pressure (gauge)

Design temperature

Design pressure (gauge)

Dimensional standard

Material standard

TEMA class

Service class

Radiography



Design Options

Set default

Set default

No

Set default

mm

mm

mm

m/s

m/s

15 15

unspecified

Set default

Set default

mm

Set default

Set default

0

One region

Previous

Highest cost or area ratio considered

Cold SideHot Side

Maximum fluid velocity

Minimum fluid velocity

Use proportional baffle cut

Allow baffles under nozzles

Shells in parallel

Shells in series

Use shell ID or OD as reference

MaximumMinimumIncrement

Tube passes

Tube length

Shell diameter

Target%AllowPresDropForNoz

Shell side nozzle location options

Location of nozzle at U-bend

Number of tube rows between sealing strips

Percent of tubes to be plugged

Percent of shell diameter for disengagement

Remove tubes for vapor disengagement space in flooded evaporator

Baffle cut (% of diameter)

Use pipe for shells below this diameter

Maximum exit entrainment ratio (mass liquid/vapor) (pool boilers only)

Allow local temperature cross

Basis for design optimization

Minimum % excess surface area required

Show units that meet maximum actual/allowed hot side pressure drop ratio

Show units that meet maximum actual/allowed cold side pressure drop ratio

Optimisation item number to repeat

Number of regions for variable baffle pitch

Variable baffle pitch: First to last pitch ratio

Design search thoroughness options



Thermal Analysis Options

1 1

1 1

Set default

W/(m˛ K)

mm

Adjust both sides based on fouling input

W/(m˛ K)

W/(m˛ K)

1 1

1 1

mm

W/(m K)

Fraction of tube area submerged for shell side condensers

Falling film evaporator distributor velocity heads for pressure loss calculation

Weir height above bundle for kettle reboiler

U-bend area will be considered effective for heat transfer

Pressure drop multiplier

Liquid heat transfer coefficient multiplier

Liquid heat transfer coefficient

Cold SideHot Side

Fouling calculation options

Two phase heat transfer coefficient

Vapor heat transfer coefficient

Two phase heat transfer coefficient multiplier

Vapor heat transfer coefficient multiplier

Minimum allowable MTD Ft correction factor

Hot Side Cold Side

Fouling layer thickness

Fouling thermal conductivity

Correlations

HTFS - Silver-Bell

Wet wall

friction+acceleration

friction+acceleration

Full HTFS analysis

12,49N/mm˛

Use vapor shear enhancement

Not Used

Heat transfer & pressure drop

yes

kW/m˛

°C

Boiling curve not used

HTFS / ESDU

HTFS recommended method


Vapor-GasPriority for condenser outlet temperature (mixtures)

Desuperheating heat transfer method

Condensation heat transfer model

Condensation Options

Vaporization Options

Hot side pressure drop calculation options

Cold side pressure drop calculation options

Vibration analysis method

Tube axial stress

Vapor shear heat transfer enhancement


Subcooled boiling accounted for in

Post dryout heat transfer determined

BoilingCurveCorrection

Heat flux reference point

Temperature difference (Delta T) reference point

Boiling curve exponent on Delta T

Correction to boiling curve

Lowfin tube calculation method

Effective cross flow fraction

Single phase tubeside heat transfer method

Falling film evaporation method



Enhancements

BL1(305)

Reynolds number

Colburn J-factor

Friction factor

BL1(307)

Reynolds number

Colburn J-factor

Friction factor

Enhancement identification

Shell side enhancements

Tube side enhancements

Enhancement identification

CalculationOptions

Outlet, to max.pr.drop

Outlet, to max.pr.drop

100

0

Full HTFS analysis

0,5

Stop when fully converged

Medium

0,2Calculation step size

Calculation grid resolution

Convergence criterion

Relaxation parameter

Convergence tolerance - pressure

Cold side pressure drop calculation options

Maximum number of Iterations

Pressure drop calculation options - cold side

Pressure drop calculation options - hot side



Warnings and MessagesDescription

1828 Physical properties data for Stream 1 have been supplied at two identical, or near identical pressures. Only the first set of data, at pressure 1 bar, has been accepted.

1828 Physical properties data for Stream 2 have been supplied at two identical, or near identical pressures. Only the first set of data, at pressure 1 bar, has been accepted.

1860 The consolidated process conditions for Stream 1, prior to the main calculations, give a heat load of -837,4 kW, for a flow of 3,8727 kg/s, with outlet temperature 25 C and quality (vapor mass fraction) 0.

1860 The consolidated process conditions for Stream 2, prior to the main calculations, give a heat load of 837,4 kW, for a flow of 14,9408 kg/s, with outlet temperature 55 C and quality (vapor mass fraction) 0.

1446 The Advanced calculation has converged after 24 iterations



Optimization Path

Shell Tube Length Pressure Drop Baffle Tube Units Total

Item Size Actual Reqd. Arearatio

Shell Dp Ratio Tube Dp Ratio Pitch No. TubePass

No. P S Price Design Status

mm mm mm bar bar mm Dollar(US)

1 336,55 6096 6086,4 1 0,08507 0,77 0,08105 0,16 158,75 36 1 143 1 2 48540 OK

1 336,55 6096 6086,4 1 0,08507 0,77 0,08105 0,16 158,75 36 1 143 1 2 48540 OK



Recap of Designs

A B

Shell size mm 336,55 336,55

Tube length - actual mm 6096 6096

Tube length - required mm 6086,4 6086,4

Pressure drop, SS bar 0,08507 0,08507

Pressure drop, TS bar 0,08105 0,08105

Baffle spacing mm 158,75 158,75

Number of baffles 36 36

Tube passes 1 1

Tube number 143 143

Number of units in series 2 2

Number of units in parallel 1 1

Total price Dollar(US) 48540 48540

Program mode Design Rating /Checking

0

223,84

158,75

R - refinery service

Flat Metal Jacket Fibe


-

-

Single segmentalCarbon Steel

-

Exp.

-

mm

Company:

Location:




330,2 6096 BEM 1 2

102,8 m˛ 2 51,4 m˛

Geothermal fluid from production well->G uid in injection well

3,8727 14,9408kg/s

0 0kg/s 0 0

3,8727 3,8727kg/s 14,9408 14,9408

kg/s 0

75 25°C 17,96 55

°C

kg/mł

mPa s

kJ/(kg K)

W/(m K)

kJ/kg

1 35bar

0,36 0,55m/s

0,11 0,08507bar 0,49987 0,08105

0 0m˛ K/W

kW837,4 °C11,93

683,2 684,2 W/(m˛ K)684,2

bar 38,61066

110 93,33°C

1 1

3,18 3,18mm

154,05 -

77,93 - 90,12 -

77,93 - 90,12 -

mm

1676,4 2169,8 kg893,1

681 53 kg/(m s˛)51

37,74

mm

mm

143 23,8119,05 2,11 6096mm mm mm

Plain Carbon Steel 30

mm355,6

Carbon Steel

Carbon Steel

- None

-

-

-

Carbon Steel

Hor

H

Avg

-

336,55

0 0

0,91493 34,91895

3,44738

968,47 1007,34 1245,98 1100,06

0,3743 0,8904 0,2161 0,1425

4,349 4,313 1,399 1,663

0,6662 0,611 0,0887 0,0682

T1

S1

S2

T2

0

#/m

ID

77,93 -1

1

1

1

1

1

None

Size/rating

Ao based

Vapor/Liquid

--

Remarks

TEMA class

Intermediate

BundleFilled with waterWeight/Shell

Code requirements

Floating head

Tube SideGaskets - Shell side

Bundle exitBundle entrance

TypeExpansion joint

Tube-tubesheet jointBypass seal

TypeU-bendSupports-tube


Tubesheet-floating

Channel cover

Floating head cover

Tubesheet-stationary

Channel or bonnet

Out

In

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

seriesparallelConnected inTypeSize

OD

Sketch

1

2

3

4

5

6

7

PERFORMANCE OF ONE UNIT8

Fluid allocation9

Fluid name10

Fluid quantity, Total11

Vapor (In/Out)12

Liquid13

Noncondensable14

Temperature (In/Out)

15

Dew / Bubble point

16

17

18

19

20

21

22

23

24

25

26

27

28

Heat exchanged29

Transfer rate, Service30

CONSTRUCTION OF ONE SHELL31

Design/vac/test pressure:g

32

Design temperature

33

Number passes per shell

34

Corrosion allowance

35

Connections

36

37

38

Tube No.

39

Tks-40

41

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-crossing

53

Type

54

Cut(%d)

55

Spacing: c/c

56

Baffle-long

57

Seal type

58

Inlet

RhoV2-Inlet nozzle


Fouling resist. (min)

Pressure drop, allow./calc.

Velocity

Pressure (abs)

Latent heat

Thermal conductivity

Specific heat

Molecular wt, NC

Molecular wt, Vap

Viscosity

Density

MTD corrected

Dirty Clean

Heat Exchanger Specification Sheet



3,8727

0

14,9408

0

N/m

0,6662 0,611

0,3743 0,8904

4,349 4,313

968,47 1007,34

0 00 0

3,8727 3,8727 14,9408 14,9408

W/(m˛ K)

kg/s

°C

m/s

kg/mł

mPa s

kJ/(kg K)

W/(m K)

17750,15 7461,44

2,44 6,29

75 25 17,96 55

1 0,91493 35 34,91895

0,08105

0,36 0,35 0,49 0,55

0 0

bar

bar

bar

kg/mł

mPa s

kJ/(kg K)

W/(m K)

kJ/kg

21722,5

3150,6

684,2

684,2

910,7

0

0

0,00005

0,00032

0,00146

0,00146

0,0011

0

0

3,15

21,72

75,13

m˛ K/W

0,00246

0,00147

0,02662

0,00245

0,01206

1,83

33,01

3,04

3,05

14,95

0 0

0,0887 0,0682

0,2161 0,1425

1,399 1,663

1245,98 1100,06

41508,97 62934,14

3,41 3,47

0,03559 44,12

0 0

kW

0 0

0 0

11,93°C 11,92

0,00664 7,81

0,00401

0,00243

0,0473

0,01941

0,00259

2,85

55,6

22,82

4,71

3,04

0,0027 3,17

m/s

0,49

0,84

0,36

0,23

0,81

0,82

0,64

2,13

1,99

18,02 18,02 102,03 102,03

0 0

-837,4 837,4

0 0

kg/(m s˛)

681

655

664

516

4987

4670

837,4kW

1 1

mm

mm

mm

1

1

1

1

1

11

143

30

6096

23,81

158,75

223,84

223,84

37,74

mm

mm

mm

H

1Hor336,55 26096 BEM

168,28

101,6

101,6

88,9

88,9

88,9

Single segmental

52,2

2

51,4

102,8104,3 m˛

mm

m˛

36

6003,9

14,83 19,05

Plain

mm

0,085070,11 0,49987

None

NoNo No

0,35

0,22

0,55

Rating / Checking

None

kg/s

kg/s

kg/s

°C

bar

kW

m/s kg/(m s˛)

Insert

/

/

/ Rho*V2

/Vibration problem RhoV2 violation


/

/

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/c

Spacing at inlet

Number

Type

Tube pattern

Tube pitch

Length act/eff

Tube passes

Tube No.

Actual/Reqd area ratio - fouled/clean

Total heat load

Heat Transfer Parameters

2-Phase liquid

Liquid only

Molecular weight

Tube nozzle interm

Tube nozzle outlet

Tubes

Tube nozzle inlet

Shell nozzle interm

Shell nozzle outlet

Shell baffle window

Velocity

Shell nozzle inlet

Shell bundle Xflow

Intermediate nozzle

Eff. MTD/ 1 pass MTD

Latent heat

2-Phase vapor

Vapor only

Intermediate nozzle

/

Inlet space Xflow

Inlet nozzle

1

2

3

4

7

8

9

10

11

12

13

14

Size

PERFORMANCE OF ONE UNIT

Total flow

Vapor

Liquid

Noncondensable

Cond./Evap.

Temperature

22

21

20

19

18

17

16

15 Quality

Pressure (abs)

Delta P allow/calc

Velocity

Liquid Properties

Density

Viscosity

30

29

28

27

26

25

24

23 Specific heat

Therm. cond.

Surface tension

Vapor Properties

Density

Viscosity

Specific heat

38

37

36

35

34

33

32

31 Therm. cond.

Latent heat

Molecular weight

Reynolds No. vapor

Reynolds No. liquid

Prandtl No. vapor

46

45

44

43

42

41

40

39

Prandtl No. liquid

54

53

52

51

50

49

48

47

Tubes

Type

ID/OD

6

5

Shell Side

Tube side fouling

Tube wall

Outside fouling

Outside film

Overall fouled

Overall clean

Tube Side Pressure Drop

Inlet nozzle

Entering tubes

Inside tubes

Exiting tubes

Outlet nozzle

Shell Side Pressure Drop

Baffle Xflow

Baffle window

Outlet space Xflow

Outlet nozzle

Heat Load

Coef./Resist.

Tube side film

Tube Side

In Out In Out

Surf/Unit (gross/eff/finned)

55

56

57

Baffles

Other

Outlet

Inlet

Nozzles: (No./OD)

%

Two-Phase Properties


Process Data

%

%



Thermal Details - General

0,36

Dollar(US)48540No

1

bar 34,91895350,914931

kg/s

0000

14,94083,8727

Single segmental

30

330,2

19,05

6096

14,940814,94083,87273,8727

kg/s

kg/s

°C

°C

W/(m˛ K)

m˛ K/W

m/s

bar

kW

W/(m˛ K)

m˛

°C

mm

mm

0000

5517,962575

910,73150,6

00

0,55

0,081050,499870,085070,11

837,4

684,2

11,93

BEM 1

Hor

2 1

1

143 2,11

23,81 mm

Plain

37,74No

102,8

W/(m˛ K) 684,2

Rating / Checking

NoneInsert

RhoV2 problem

Overall dirty coef (plain/finned)

Cut(%d)

No.

PitchPattern

Baffles

TksOD

Shell size

Unit

Total cost

Vibration problem

Actual/required area ratio(dirty/clean)

Operating pressures

Vapor mass quality

Total mass flow rate

Tubes

pass

Vapor mass flow rate (In/Out)

Liquid mass flow rate

Temperatures

Dew / Bubble point

Film coefficient (mean)

Fouling resistance (OD based)

Velocity (highest)

Pressure drop (allow./calc.)

Total heat exchanged

Overall clean coef (plain/finned)

Effective area (plain/finned)

Effective MTD


ser par

Shell side / Fouling / Wall / Fouling / Tube side



1,28

75,13 75,13

0

3,15 3,15

0

21,72 21,72

0,0011

0

0,00005

0

0,00032

m˛ K/W

910,7

21722,5

3150,6

W/(m˛ K)

1 1

102,6 102,6m˛

0,00146 0,00146m˛ K/W

W/(m˛ K) 684,2 684,2

102,8

0,00146

683,2

75,01

0,08

3,14

0,08

21,68

m˛ K/W 0

0

0

0

DirtyCleanOverall Coefficient/Resistance Summary

Overall coefficient

Overall resistance

Area required

Area ratio: actual/required

Resistance Distribution

Shell side film

Shell side fouling

Tube wall

Tube side fouling*

Tube side film *

* Based on outside surface - Area ratio: Ao/Ai =

Max Dirty

1.0

Shell side fouling

Tube side fouling*

0.0

0.0

% % %

Thermal Details

Thermal Details - Hot Side

Stream mass fractions

Liquid mass fractions at inlet

Liquid mass fractions at outlet

Vapor mass fractions at inlet

Vapor mass fractions at outlet

Liquid 2 mass fractions at inlet

Liquid 2 mass fractions at outlet

Stream mole fractions

Liquid mole fractions at inlet

Liquid mole fractions at outlet

Vapor mole fractions at inlet

Vapor mole fractions at outlet

Liquid-2 mole fractions at inlet

Liquid-2 mole fractions at outlet

Stream mass flow kg/s

Liquid mass flow at inlet kg/s

Liquid mass flow at outlet kg/s

Vapor mass flow at inlet kg/s

Vapor mass flow at outlet kg/s

Liquid 2 mass flow at inlet kg/s

Liquid 2 mass flow at outlet kg/s



Thermal Details - Cold Side

Stream mass fractions

Liquid mass fractions at inlet

Liquid mass fractions at outlet

Vapor mass fractions at inlet

Vapor mass fractions at outlet

Liquid 2 mass fractions at inlet

Liquid 2 mass fractions at outlet

Stream mole fractions

Liquid mole fractions at inlet

Liquid mole fractions at outlet

Vapor mole fractions at inlet

Vapor mole fractions at outlet

Liquid-2 mole fractions at inlet

Liquid-2 mole fractions at outlet

Stream mass flow kg/s

Liquid mass flow at inlet kg/s

Liquid mass flow at outlet kg/s

Vapor mass flow at inlet kg/s

Vapor mass flow at outlet kg/s

Liquid 2 mass flow at inlet kg/s

Liquid 2 mass flow at outlet kg/s



Thermal Details - Coefficients

3,473,416,292,44

62934,1441508,977461,4417750,15

3150,6 910,7

3150,6 910,7

W/(m˛ K)

1169,6

1169,6

Bare area (OD) / ID areaBare area (OD) / Finned area

Reynolds numbers

Film Coefficients

Vapor Nominal

Liquid Nominal

Tube SideShell Side

Liquid

Vapor


Prandtl numbers

Overall film coefficients

Vapor sensible

Two Phase

Liquid sensible

In Out In Out

°C kW/m˛

1512,41

11,93

11,92

0,96

8,2

°C

45,2

42,49

71,32 23,45

Tube mean metal temperature

Tube wall temperatures (highest / lowest)

Shell mean metal temperature

Wall Temperatures

Heat Flux (based on tube O.D.)Temperature Difference

Highest ratio, actual/critical flux

Highest actual flux

Critical heat flux (at highest ratio)

LMTD based on end points

Overall actual fluxOverall Effective MTD

One pass counterflow MTD

Effective MTD correction factor

837,4

0

0

0

0

0

0

0

0

0

0

0

0

-837,4

-837,4

0

0

0

kWkW

0

100 837,4 100

Tube SideShell SideHeat Load Summary

% total % total

Vapor only

2-Phase vapor

Latent heat

2-Phase liquid

Total

Liquid only

100 100



Thermal Details - Pressure Drop

0,00039-0,00002

0,11

bar

m/s m/s

0,08507

0

0,08509

0,49987

0,08105

0

0,08066

0,23

0,35

0,22

0,22

0,81

55,6

22,82

3,17

0,49

0,49

0,55

2,13

1,83

33,01

3,04

14,95

bar

0,0473

0,01941

0,0027

0,00147

0,02662

0,00245

0,01206

bar

0,84 0,00401 4,71 0,64 0,00246 3,05

0,26 2,850,00243

0,25 3,040,00259

0,36

0,55

0,23

0,82 7,81 1,99 44,120,00664 0,03559Intermediate nozzles

Vapor outlet nozzle

Liquid outlet nozzle

%dp%dp

Tube SideShell Side

Outlet nozzle

Exiting bundle

Baffle windows

Bundle Xflow

Entering bundle

Pressure drop distribution

Inlet nozzle

Frictional

Gravitational

Total calculated

Maximum allowed

Pressure Drop

Momentum change

Inlet space Xflow

Outlet space Xflow

Inside tubes



Thermal Details - Shell Side Stream Analysis

968,470,84

kg/młm/smm˛

4769

8928

5953

5953

5953

5953

2232

kg/(m s˛)kg/(m s˛)

4987

293

516

655

117

51

53

121

681

12,7

3,18

0,79

mm

0

0,1

0,1

0,19

0,71

0,61

0

0,07

0,17

0,32

0,5

0,43

0

0,09

0,1

0,19

0,71

0,61

11299

18639

4769

11299

17088

17088

6379

24713

2,13

0,49

0,64

0,81

0,34

0,22

0,23

0,35

1100,06

1245,98

1245,98

1007,34

1007,34

1007,34

968,47

968,47

33224713 0,55 1100,06

mm˛ m/s kg/mł kg/(m s˛) kg/(m s˛)

Tube outlet

TEMA limitDensityVelocityFlow Area Rho*V2Rho*V2 analysis

Diam. ClearanceOutletMiddleInletShell Side Flow Fractions

Tube outlet nozzle

Tube inlet

Tube inlet nozzle

Shell outlet nozzle

Shell exit

Bundle exit

Bundle entrance

Shell entrance

Shell inlet nozzle

Pass lanes

Shell ID - bundle OTL

Baffle OD - shell ID

Baffle hole - tube OD

Window

Crossflow

Thermosiphons

Thermosiphon stability

Vertical Tube Side Thermosiphons

Kutateladze Number in axial nozzle

Fraction of tube length flooded

Flooding criterion - top of tubes (should be > 1.0)

Flow reversal criterion - top of tubes (should be > 0.5)

Kettles

Entrainment fraction

Quality at top of bundle

Recirculation ratio



Thermal Details - Vibration Analysis - Fluid Elastic Instability (HTFS)

7841,74kg/mł

12,49N/mm˛

200446,5N/mm˛

mm

Tube LocationTube naturalfrequency

Natural frequencymethod

Tube effectivemass

Dominantspan

cycle/s kg/m

1 373,1 Exact Solution 1,55




W/Wc W/Wc

Tube Location Vibration for heavy (LDec=0.1)

for medium(LDec=0.03)

for light (LDec=0.01)

Estimated logDec

for estimateddamping

1 No 0 0,01 0,01 0,04 0,01

2 No 0,01 0,03 0,05 0,04 0,02

4 No 0 0,01 0,01 0,04 0,01

5 No 0 0,01 0,01 0,04 0,01

1/10Region number:

4 - 1st row inside baffle overlap

3 - Top row inside baffle overlap

2 - 1st row outside baffle overlap

1 - 1st row in bundle at inlet

5 - Bottom row in bundle

Tube Locations:

Fluid Elastic Instability Analysis

U-bend longest unsupported length

Tube material Young's Modulus

Tube axial stress


1/2Shell number:



Thermal Details - Vibration Analysis - Fluid Elastic Instability (HTFS)

7841,74kg/mł

12,49N/mm˛

200446,5N/mm˛

mm

Tube LocationTube naturalfrequency

Natural frequencymethod

Tube effectivemass

Dominantspan

cycle/s kg/m





W/Wc W/Wc

Tube Location Vibration for heavy (LDec=0.1)

for medium(LDec=0.03)

for light (LDec=0.01)

Estimated logDec

for estimateddamping

1 No 0 0,01 0,01 0,04 0,01

2 No 0,01 0,03 0,04 0,04 0,02

4 No 0 0,01 0,01 0,04 0,01

5 No 0 0,01 0,01 0,04 0,01

1/10Region number:

4 - 1st row inside baffle overlap

3 - Top row inside baffle overlap

2 - 1st row outside baffle overlap

1 - 1st row in bundle at inlet

5 - Bottom row in bundle

Tube Locations:

Fluid Elastic Instability Analysis

U-bend longest unsupported length

Tube material Young's Modulus

Tube axial stress


2/2Shell number:

Thermal Details - Vibration Analysis - Resonance Analysis (HTFS)

Location inshell

TubeLocation

Vibration Spanlength

Fv/Fn Fv/Fa Ft/Fn Ft/Fa Vortexamplitude

Turbulentamplitude

TEMAlimit

mm mm mm mm

Inlet 1 No 223,84 0,02 0 0,01 0

Inlet 2 No 382,59 0,01 0 0,01 0

Inlet 4 No 223,84 0 0 0 0

Inlet 5 No 382,59 0 0 0 0

Midspace 1 No 317,5 0 0 0 0

Midspace 2 No 317,5 0,01 0 0,01 0

Midspace 4 No 158,75 0 0 0 0

Midspace 5 No 317,5 0 0 0 0

Outlet 1 No 382,59 0 0 0 0

Outlet 2 No 223,84 0,01 0 0,01 0

Outlet 4 No 223,84 0 0 0 0

Outlet 5 No 223,84 0,01 0 0,01 0



Location inshell

NaturalFn

AcousticFa

Flowvelocity

X-flowfraction

RhoV2 Strouhal No.

cycle/s cycle/s m/s kg/(m s˛)

Inlet 373,1 2617,85 0,23 1 53 0,46

Inlet 373,1 2617,85 0,2 0,52 40 0,46

Inlet 1207,95 2617,85 0,2 0,52 40 0,46

Inlet 373,1 2617,85 0,04 0,52 2 0,46

Midspace 373,1 2598,98 0,04 0,52 2 0,46

Midspace 373,1 2598,98 0,2 0,52 40 0,46

Midspace 1207,95 2598,98 0,2 0,52 40 0,46

Midspace 373,1 2598,98 0,04 0,52 2 0,46

Outlet 373,1 2584,45 0,04 0,52 2 0,46

Outlet 373,1 2584,45 0,2 0,52 39 0,46

Outlet 1207,95 2584,45 0,2 0,52 39 0,46

Outlet 373,1 2584,45 0,23 1 52 0,46

Thermal Details - Vibration Analysis - Resonance Analysis (HTFS)

Location inshell

TubeLocation

Vibration Spanlength

Fv/Fn Fv/Fa Ft/Fn Ft/Fa Vortexamplitude

Turbulentamplitude

TEMAlimit

mm mm mm mm

Inlet 1 No 223,84 0,01 0 0,01 0

Inlet 2 No 382,59 0,01 0 0,01 0

Inlet 4 No 223,84 0 0 0 0

Inlet 5 No 382,59 0 0 0 0

Midspace 1 No 317,5 0 0 0 0

Midspace 2 No 317,5 0,01 0 0,01 0

Midspace 4 No 158,75 0 0 0 0

Midspace 5 No 317,5 0 0 0 0

Outlet 1 No 382,59 0 0 0 0

Outlet 2 No 223,84 0,01 0 0,01 0

Outlet 4 No 223,84 0 0 0 0

Outlet 5 No 223,84 0,01 0 0,01 0



Location inshell

NaturalFn

AcousticFa

Flowvelocity

X-flowfraction

RhoV2 Strouhal No.

cycle/s cycle/s m/s kg/(m s˛)

Inlet 370,48 2584,4 0,23 0,52 52 0,46

Inlet 370,48 2584,4 0,2 0,52 38 0,46

Inlet 1199,48 2584,4 0,2 0,52 38 0,46

Inlet 370,48 2584,4 0,04 0,52 2 0,46

Midspace 370,48 2574,8 0,04 0,52 2 0,46

Midspace 370,48 2574,8 0,2 0,52 39 0,46

Midspace 1199,48 2574,8 0,2 0,52 39 0,46

Midspace 370,48 2574,8 0,04 1 2 0,46

Outlet 370,48 2566,92 0,04 1 2 0,46

Outlet 370,48 2566,92 0,2 0,52 39 0,46

Outlet 1199,48 2566,92 0,2 0,52 39 0,46

Outlet 370,48 2566,92 0,22 0,52 51 0,46



Thermal Details - Methods

No No

No No

No No

friction+acceleration friction+acceleration

Wet wall

HTFS - Silver-Bell

Yes

Not Used

Set default

No

Boiling curve not used



HTFS / ESDU

Advanced method

1Tube pass multiplier

Calculation method

Lowfin Calculation Method

Single phase tubeside heat transfer method

Falling film evaporation method

Correction to user-supplied boiling curve

Post dryout heat transfer accounted for

Subcooled boiling accounted for in

Liquid subcooling heat transfer (vertical shell)

Vapor shear enhanced condensation

Multicomponent condensing heat transfer method


Pressure drop calculation option

Pressure drop multiplier

Heat transfer coefficient specified

Cold SideHot Side

Heat transfer coefficient multiplier



Basic Geometry

mm

336,55

21

Hor

BEM

336,55

355,6 355,6

336,55

355,6

1

6096mm

143

Plain

19,05mm

23,81mm

30

158,75mm

Single segmental

36

223,84mm


Nozzle type Inlet Outlet Intermediate Inlet Outlet Intermediate

Number of nozzles 1 1 1 1 1 1

Actual outside diameter mm 88,9 88,9 88,9 168,28 101,6 101,6

Inside diameter mm 77,93 77,93 77,93 154,05 90,12 90,12

Height under nozzle mm 35,02 35,02 35,02

Dome inside diameter mm

Vapor belt inside diameter mm

Vapor belt inside width mm

Vapor belt slot area mm˛

Impingement protection Noimpingement

Noimpingement

Noimpingement

Distance to tubesheet mm 5930,9 5930,9 158,75

mm

Spacing at inlet

Spacing (center-center)

Baffle number

Baffle type

Tube pattern

Tube pitch

Tube O.D.

Tube type

Tube number (calcs.)

Tube length actual

Tube passes

Unit Configuration

Arrangement

Position

Rear headFront headKettleShell

Outside diameter

Inside Diameter

serpar

Exchanger Type



Tubes

30

23,81

2,11

19,05

42,86

6096

mm

mm

mm

mm

mm

1,28

51,7623

Carbon Steel

Plain

0

143

W/(m K)

14,83

6003,9

mm

mm

#/m

mm

mm

mm

mm

0

mm

mm

mm

mm

mmTube inside diameter under fins

Fin number

Fin thickness

Fin height

Fin spacing

Cut and twist length

Low longitudinal finsLow circumferential fins

Fin density

Fin height

Fin thickness

Tube root diameter

Tube wall thickness under fin

Pattern

Pitch

Wall thickness

Inside diameter

Outside diameter

Tubesheet thickness

Tube length effective

Tube length actual

Area ratio Ao/Ai

Thermal conductivity

Material

Internal enhancementExternal enhancement

Type

Number of tubes plugged

Total number

Tubes



Baffles

3,18223,84

223,84

158,75

36

mmmm

mm

mm

H

Yes

Single segmental

4

4,5

269,88mm

269,88mm

mm

mm

0,79

3,18

mm

mm

34,56

37,74

37,74

Baffle spacing mm

Baffle cut percent, outer

Baffle cut percent, inner

Number of baffle spaces

Baffle region length mm

Baffle cut area percent, outer

Baffle cut area percent, inner

VariableBaffles

Baffle cut: inner / outer / interm

Baffle hole - tube od diam clearance

Shell id - baffle od diam clearance

Spacing at center of H shell

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

End length at rear head

End length at front head

Nominal (% diameter)

Baffles

Type

Tubes in window Actual (% diameter)

Actual (% area)

Cut orientation

Number

Spacing (center-center)

Spacing at inlet

Spacing at outlet Thickness

Tube rows in baffle window

Tube rows in baffle overlap

Supports Misc. Baffles

No

0

0

0

0

mm

mm

mm

mm

0

0

0

NoSpecial support at inlet nozzle

Support blanking baffle

Supports between baffles

Supports in endspace at rear head

Supports in endspace at front head

Supports at U-bend

Thickness

Window length at front head

Window length at center

Window length at rear head

Longitudinal BaffleSupports-tube

Supports for K, X shells

Supports at center of H shell

Supports at each G,H,J shell inlet and I shell outlet



Bundle

m˛

mm

mm

No

323,85

1

None

mm

Exp.

3,18mm

3,18mm

35,02

mm

35,02

15,88

15,88

mm

0

51,4

0

0

mm 12,7

1

Ribbon (single band)

Standard (horizontal)

9,55mm

Undefined

-1

mm

mm

mm

mm

51,4

52,2

m˛

m˛

m˛

m˛

Horizontal pass lane width

Vertical pass lane width

Interpass tube alignment

Outer tube limit

Sealing strips (pairs)

Tie rod number


Impingement distance

Tube to tubesheet joint

Tube projection from front tsht

Tube projection from rear tsht

Shell ID to center 1st tube row

From top

From bottom

From right

From Left

Deviation in tubes/pass

Bare tube area per shell

Finned area per shell

U-bend area per shell

Shell id - bundle otl diam clearance

Bundle

Tube passes

Tube pass layout

Tube pass orientation

Tie rod diameter

U-bend orientation

Impingement plate diameter

Impingement plate width

Impingement plate length

Impingement plate thickness

Effective surface area per shell

Gross surface area per shell



Mechanical Details

None

mm

mm

hiTRAN part number

Internal enhancements

Tube insert type

Twisted tape thickness

Twisted tape 360 deg twist pitch

Cost/Weight

24270

Dollar(US)kg

36161

7575

4804

1676,4

2169,8

893,1

589,6

107,6

86,2

48540Total cost (all shells)

Cost dataWeights

Total cost (1 shell)

Labor cost

Material cost (except tubes)

Tube material cost

Total weight - empty

Total weight - filled with water

Bundle

Shell

Front head

Rear head

Shell cover



Setting Plan

102

2 BoltsFixed

51

308

77

102

2 BoltsSliding

51

308

77

6915 Overall

246 164159 5772 329

164 1219 3658

Pulling Length 5710

T1

S1

S2

T2

A

Nozzle Data

Ref OD Wall Standard Notes

S1 89 mm 5,5 mm 150 ANSI Slip on

S2 89 mm 5,5 mm 150 ANSI Slip on

T1 102 mm 5,7 mm 150 ANSI Slip on

T2 102 mm 5,7 mm 150 ANSI Slip on

Empty

1676 kg

Flooded

2170 kg

Bundle

893 kg

Weight Summary

Internal Volume m³ 0,5295 0,068

PWHT

Radiography

Number of Passes 1 1

Test Pressure bar

Corrosion Allowance mm 3,175 3,175

Full Vacuum

Design Temperature C 110, 93,33

Design Pressure bar 3,45 38,61

Design Data Units Shell Channel

Customer Specifications

Design Codes

ASME Section VIII Div. 1

TEMA R




Location:

Company:

Revision Date

24.3.2014.

Dwg. Chk. App.

Aspen Shell & Tube Exchanger

Setting Plan

BEM 337 - 6096

Drawing Number

330

T1

330

330

S1

S2

368

330

T2

Views on arrow A



Tube Layout

12

3,7

3 m

m1

23

,73

mm

Company:

Location:

Service of Unit:

Item No.:

Design Codes


TEMA R - refinery service

Customer Specifications

Aspen Shell & Tube

Tube Layout

Drawing Number

Revision Date Dwg. App.

24.3.2014.

Shell inside diameter mm 336,55

Front head inside diameter mm 336,55

Outer tube limit mm 323,85

Tube number (calcs.) 143

Tube number (layout) 143

Tube O.D. mm 19,05

Tube pitch mm 23,8125

Tube pattern 30

Tube passes 1

Tie rod number -1

Tie rod diameter mm 9,55

Sealing strips (pairs) 1

Baffle type Single segmental

Impingement protection None

Tube length mm 6096,

Shell Side Inlet Nozzle Inside Diameter mm 77,9272

Shell Side Outlet Nozzle Inside Diameter mm 77,9272

143

19,05

19,05



U-bend Details



Calculation Details - Shell Side

PointNo.

ShellNo.

ShellNo.

DistanceEnd

SS BulkTemp.

SS FoulingTemp

Tube MetalTemp

SSPressure

SS Vaporfraction

SS voidfraction

SS HeatLoad

SS Heatflux

SS FilmCoef.

mm °C °C °C bar kW kW/m˛ W/(m˛ K)

1 1 1 6044 74,95 71,28 70,93 0,99596 0 0 -0,8 -15 4069,7

2 1 1 5832 73,37 69,77 69,44 0,99485 0 0 -27,4 -14,5 4038,9

3 1 1 5820 73,29 69,42 69,09 0,99499 0 0 -28,9 -14,3 3690,3

4 1 1 5316 69,76 66,08 65,77 0,99212 0 0 -88,2 -13,4 3626,8

5 1 1 4812 66,45 62,94 62,65 0,98925 0 0 -143,8 -12,5 3565,5

6 1 1 4308 63,34 59,98 59,71 0,98636 0 0 -196 -11,8 3507,2

7 1 1 3804 60,4 57,19 56,93 0,98345 0 0 -245,3 -11,1 3451,9

8 1 1 3300 57,64 54,55 54,31 0,98053 0 0 -291,7 -10,5 3398,4

9 1 1 2796 55,02 52,06 51,83 0,9776 0 0 -335,5 -9,9 3347,9

10 1 1 2292 52,54 49,7 49,48 0,97465 0 0 -377,1 -9,4 3298,9

11 1 1 1788 50,19 47,45 47,25 0,97169 0 0 -416,4 -8,9 3252,5

12 1 1 1284 47,96 45,32 45,13 0,96871 0 0 -453,8 -8,4 3207,6

13 1 1 780 45,83 43,3 43,11 0,96572 0 0 -489,3 -8 3165,1

14 1 1 276 43,81 41,36 41,19 0,96271 0 0 -523,1 -7,6 3123,6

15 1 1 264 43,76 41,49 41,31 0,96245 0 0 -523,8 -7,8 3415,9

16 1 1 52 42,93 40,69 40,51 0,96126 0 0 -537,8 -7,6 3397,1

17 2 1 7052 42,88 40,64 40,46 0,95455 0 0 -538,6 -7,6 3396

18 2 1 7264 42,07 39,86 39,68 0,95337 0 0 -552,2 -7,5 3377,6

19 2 1 7276 42,02 39,65 39,48 0,95349 0 0 -553 -7,3 3087,1

20 2 1 7780 40,18 37,89 37,73 0,95045 0 0 -583,8 -7 3049,1

21 2 1 8284 38,42 36,2 36,05 0,9474 0 0 -613,2 -6,7 3012,5

22 2 1 8788 36,73 34,59 34,45 0,94433 0 0 -641,3 -6,4 2977,6

23 2 1 9292 35,12 33,05 32,91 0,94124 0 0 -668,3 -6,1 2943,7

24 2 1 9796 33,58 31,57 31,44 0,93814 0 0 -694 -5,9 2911,1

25 2 1 10300 32,1 30,16 30,03 0,93502 0 0 -718,7 -5,6 2880,1

26 2 1 10804 30,69 28,8 28,67 0,93189 0 0 -742,4 -5,4 2850

27 2 1 11308 29,32 27,49 27,37 0,92874 0 0 -765,1 -5,2 2820,7

28 2 1 11812 28,02 26,24 26,12 0,92557 0 0 -787 -5 2792,8

29 2 1 12316 26,76 25,03 24,92 0,92239 0 0 -808 -4,8 2766,2

30 2 1 12820 25,55 23,87 23,76 0,91919 0 0 -828,2 -4,6 2740,9

31 2 1 12832 25,52 23,95 23,84 0,91893 0 0 -828,7 -4,7 2991,7

32 2 1 13044 25,01 23,46 23,36 0,91767 0 0 -837,2 -4,6 2980

Calculation Details - Shell Side - Properties

Temperature °C 75 70,48 65,95 61,41 56,87 52,32 47,78 43,22 38,67 34,11 29,56 25

Pressure bar 1 0,99227 0,98453 0,9768 0,96907 0,96133 0,9536 0,94586 0,93813 0,9304 0,92266 0,91493

Vapor fraction 0 0 0 0 0 0 0 0 0 0 0 0

Liquid density kg/mł 968,47 972,11 975,72 979,31 982,88 986,44 989,97 993,48 996,97 1000,45 1003,9 1007,34

Liquid specific heat kJ/(kg K) 4,349 4,342 4,336 4,331 4,327 4,323 4,32 4,317 4,315 4,314 4,313 4,313

Liquid thermal cond. W/(m K) 0,6662 0,6627 0,6589 0,6548 0,6504 0,6458 0,6408 0,6355 0,6298 0,6239 0,6176 0,611

Liquid viscosity mPa s 0,3743 0,3978 0,424 0,4533 0,4862 0,5233 0,5654 0,6133 0,6683 0,7315 0,8049 0,8904

Surface tension N/m

Latent heat kJ/kg

Vapor density kg/mł

Vapor specific heat kJ/(kg K)

Vapor thermal cond. W/(m K)

Vapor viscosity mPa s



Calculation Details - Tube Side

ShellNo.

TubeNo.

DistanceEnd

SS Bulk TempSS Foulingtemp.

Tube MetalTemp

TS Foulingtemp

TS BulkTemp.

TSPressure

TS Vaporfraction

TS voidfraction

TS HeatLoad

TS Heatflux

TS FilmCoef.

SS CleanCoef.

mm °C °C °C °C °C bar kW kW/m˛ W/(m˛ K) W/(m˛ K)

2 1 13044 25,01 23,46 23,36 23,25 17,98 34,9967 0 0 0,2 4,6 876,3 2980

2 1 12832 25,52 23,95 23,84 23,73 18,38 34,99624 0 0 8,7 4,7 877,2 2991,7

2 1 12820 25,55 23,87 23,76 23,65 18,4 34,99621 0 0 9,1 4,6 877,2 2740,9

2 1 12316 26,76 25,03 24,92 24,81 19,37 34,9951 0 0 29,4 4,8 879,3 2766,2

2 1 11812 28,02 26,24 26,12 26,01 20,36 34,994 0 0 50,4 5 881,6 2792,8

2 1 11308 29,32 27,49 27,37 27,25 21,4 34,99289 0 0 72,2 5,2 883,9 2820,7

2 1 10804 30,69 28,8 28,67 28,55 22,47 34,99178 0 0 95 5,4 886,3 2850

2 1 10300 32,1 30,16 30,03 29,9 23,58 34,99067 0 0 118,7 5,6 888,8 2880,1

2 1 9796 33,58 31,57 31,44 31,3 24,74 34,98956 0 0 143,4 5,9 891,3 2911,1

2 1 9292 35,12 33,05 32,91 32,77 25,94 34,98845 0 0 169,1 6,1 894 2943,7

2 1 8788 36,73 34,59 34,45 34,3 27,19 34,98734 0 0 196 6,4 896,7 2977,6

2 1 8284 38,42 36,2 36,05 35,9 28,48 34,98623 0 0 224,2 6,7 899,6 3012,5

2 1 7780 40,18 37,89 37,73 37,57 29,83 34,98512 0 0 253,6 7 902,6 3049,1

2 1 7276 42,02 39,65 39,48 39,31 31,24 34,98401 0 0 284,4 7,3 905,6 3087,1

2 1 7264 42,07 39,86 39,68 39,51 31,27 34,98398 0 0 285,1 7,5 905,9 3377,6

2 1 7052 42,88 40,64 40,46 40,29 31,89 34,98352 0 0 298,8 7,6 907,2 3396

1 1 52 42,93 40,69 40,51 40,33 31,93 34,94578 0 0 299,6 7,6 907,3 3397,1

1 1 264 43,76 41,49 41,31 41,13 32,56 34,94531 0 0 313,5 7,8 908,7 3415,9

1 1 276 43,81 41,36 41,19 41,01 32,6 34,94528 0 0 314,3 7,6 908,6 3123,6

1 1 780 45,83 43,3 43,11 42,93 34,12 34,94417 0 0 348,1 8 911,9 3165,1

1 1 1284 47,96 45,32 45,13 44,93 35,71 34,94305 0 0 383,6 8,4 915,4 3207,6

1 1 1788 50,19 47,45 47,25 47,04 37,37 34,94193 0 0 421 8,9 919 3252,5

1 1 2292 52,54 49,7 49,48 49,26 39,11 34,94082 0 0 460,3 9,4 922,8 3298,9

1 1 2796 55,02 52,06 51,83 51,6 40,92 34,9397 0 0 501,8 9,9 926,8 3347,9

1 1 3300 57,64 54,55 54,31 54,07 42,82 34,93857 0 0 545,7 10,5 931 3398,4

1 1 3804 60,4 57,19 56,93 56,68 44,82 34,93745 0 0 592,1 11,1 935,4 3451,9

1 1 4308 63,34 59,98 59,71 59,44 46,91 34,93632 0 0 641,3 11,8 940,1 3507,2

1 1 4812 66,45 62,94 62,65 62,36 49,1 34,93519 0 0 693,6 12,5 945 3565,5

1 1 5316 69,76 66,08 65,77 65,46 51,41 34,93405 0 0 749,2 13,4 950,2 3626,8

1 1 5820 73,29 69,42 69,09 68,76 53,83 34,93291 0 0 808,5 14,3 955,7 3690,3

1 1 5832 73,37 69,77 69,44 69,1 53,89 34,93288 0 0 810 14,5 956,2 4038,9

1 1 6044 74,95 71,28 70,93 70,59 54,97 34,9324 0 0 836,6 15 958,6 4069,7

Calculation Details - Tube Side - Properties

Temperature °C 17,96 21,58 25,15 28,68 32,15 35,58 38,95 42,27 45,54 48,75 51,9 55

Pressure bar 35 34,99263 34,98527 34,9779 34,97053 34,96316 34,95579 34,94843 34,94106 34,93369 34,92632 34,91895

Vapor fraction 0 0 0 0 0 0 0 0 0 0 0 0

Liquid density kg/mł 1245,98 1233,28 1220,5 1207,63 1194,66 1181,58 1168,38 1155,05 1141,57 1127,93 1114,1 1100,06

Liquid specific heat kJ/(kg K) 1,399 1,417 1,436 1,456 1,477 1,499 1,522 1,547 1,573 1,6 1,63 1,663

Liquid thermal cond. W/(m K) 0,0887 0,0869 0,085 0,0832 0,0813 0,0795 0,0776 0,0757 0,0739 0,072 0,0701 0,0682

Liquid viscosity mPa s 0,2161 0,2074 0,1993 0,1916 0,1844 0,1775 0,1709 0,1647 0,1587 0,1531 0,1477 0,1425

Surface tension N/m

Latent heat kJ/kg

Vapor density kg/mł

Vapor specific heat kJ/(kg K)

Vapor thermal cond. W/(m K)

Vapor viscosity mPa s

ATV Primary Heat Exchanger

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