thermal design calculation procedure (rev 00)

8/17/2019 Thermal Design Calculation Procedure (Rev 00)

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Heat Exchanger Thermal Design Hetran 2006 Page 1

File: cchp hex design2.EDR Date: 6/12/2015 Time: 11:18:13 PM

Description

Company:Location: Mashhad Passenger TerminalService of Unit: CCHP Our Reference:Item No.: Your Reference:Date: 6/12/2015 Rev No.: 00 Job No.: 01

Exhaust Gas Water

Remarks

Cold SideHot SideFluid name

Heading

Application Options

Gas, no phase change

Specified in inputNormal

Liquid, no phase changeSpecified in inputForced circulation

Tube sideRatingProgram mode

Location of hot fluid

Vaporizer typeVaporization curveCold side application

Condenser typeCondensation curve

Hot side application

Process Data

2.2386

450 180 120 140

1.03 7

0.14 0.340.00018 0.00035

kg/skg/s

°C°C

bar

bar m² K/W

kg/s

Program Program

kW

OutIn OutIn

Heat Load Balance Options

Heat exchanged

Cold SideHot Side

Fouling resistance

Allowable pressure drop

Operating pressure (absolute)

Dew / Bubble pointTemperature

Liquid quantityVapor quantityFluid quantity, total

Databanks

Use properties from the following:Use properties from the following:

Weight flowrate or %Weight flowrate or %Cold side composition specification

Hot side composition specification

Aspen Plus or Aspen Properties run file

Cold SideHot Side


2/24



Hot Side - ComponentComponents Source Vapor in Liquid in Liquid out Component

type

Carbondioxide

Databank 14 Program

Carbonmonoxide

Databank 0.45 Program

Oxygen Databank 0.5 ProgramNitrogen Databank 72 Program

Nitrogendioxide

Databank 0.35 Program

Water Databank 12.7 Program

Hot Side - Vapor PropertiesTemperature Specific heat Thermal

cond.Viscosity Density Molecular

weightDiffusivity

°C kJ/(kg K) W/(m K) mPa s kg/m³ m²/s


3/24



Cold Side - ComponentComponents Source Liquid in Vapor in Vapor out Component

type

Water Databank Program

Cold Side - Liquid PropertiesTemperature Specific heat Thermal

cond.Viscosity Density Surface

tension

°C kJ/(kg K) W/(m K) mPa s kg/m³ N/m


4/24



Tubes

mmPlain

20

Triangular

mm

mm

mmmm#/mm

mm

mmTube wall roughness

Tapered tube ends for knockback condensers

Twisted tape widthTwisted tape ratio

Outside/Inside surface area ratioSurface area per unit lengthFin densityFin thicknessFin height

Tube pitchTube pattern

Tube wall specificationTube wall thicknessTube outside diameter Tube type

Bundle

Program will optimize

Program

0

ProgramProgram

mm

mmmmmm

mmmmmm

mmmm

mmmm

mmmmmmmmmmmm

mmmmSpacer diameter

Tie rod diameter

Impingement plate perforated area %Impingement plate clearance to tube edgeImpingement plate distance in from shell IDImpingement plate thicknessImpingement plate width (normal to tube axis)Impingement plate length (parallel to tube axis)Impingement plate diameter

to hor. center line, D2to vert. center line, D1

Distance from tube center

Minimum u-bend diameter Number of sealing strip pairs

Number of tie rodsMaximum % deviation in tubes per passDesign symmetrical tube layout

Pass partition lane width

Baffle tube hole to tube ODBaffle OD to outer tube limitShell ID to baffle OD

Diametric clearances

Shell exit constructionShell entrance construction

Percent of shell diameter for disengagementProvide disengagement space in shell

Pool boiler options

at sides, S3at bottom, S2at top, S1

DistancePercShellIDOpen space between shell ID and outermost tube

Outer tube limit diameter

Impingement protection type

Pass layout


5/24



Baffles

Program

Program

Programmmmmmm

mmmmmmmmTotal length of support rods per baffle

Support rod diameter Inside diameter of ringInside diameter of ring

U-bend mean radiusDistance between partial supports at u-bendDistance from nearest support/baffle to tangent of u-bendType U-bend support

between bafflesat outletat inlet

Number of intermediate supports

Baffle cut orientationBaffle cut (% of diameter)Baffle type

Rating/Simulation

609.6

152.4206.25206.25

112000

446211

mmmmmmmmmm

mm

mmmm

mmmmmm

mmmmmmmmmm

Shell outside diameter Shell inside diameter Baffle spacing center-center Baffle spacing at inletBaffle spacing at outletBaffle number Tube lengthTube number Tube passesShells in seriesShells in parallel

Kettle outside diameter Kettle inside diameter

Vapor belt outside diameter Vapor belt inside diameter Vapor belt length

Shell cylinder thicknessFront head cylinder thicknessFront tubesheet thicknessRear tubesheet thicknessBaffle thickness

Nozzles

Diameter Quantity Orientation Dome OD

mm mmHot Side Inlet Program

Hot Side Outlet Program

Hot Side Condensate

Cold Side Inlet

Cold Side Outlet


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Nozzles

ProgramProgram

Program

ProgramProgram

Program

mm

mm

mmmm

mmManifold inside diameter Type of valveNumber of 90 degree elbows (R/D = 1.0)Number of 90 degree elbows (R/D = 1.5)Horizontal pipe straight lengthVertical pipe straight lengthPipe inside diameter

OutletInlet

Equivalent length of outlet piping (D)Equivalent length of inlet piping (C)

of outlet piping back to column (B)of liquid level in column (A)

Height above vessel center line

Nozzle flange ratingNozzle flange type

Flow direction for first tube pass

Hot Side Cold Side

Location of nozzle at u-bend

Design Constraints

Program

ProgramProgram

Program

ProgramProgram

0.14 0.34

mmmm

mm

bar bar

m/s m/sm/s m/s

Maximum % of allowable pressure drop for each nozzle

Shell diameter Tube length

Tube passesBaffle spacing

Increment Minimum Maximum

Use shell ID or OD as referenceUse pipe or plate for small shellsMinimum shells in seriesMinimum shells in parallel

Allowable number of baffles Allow baffles under nozzlesUse proportional baffle cut

Allowable pressure drop

Minimum fluid velocityMaximum fluid velocity

Hot Side Cold Side

Minimum % excess surface area required


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MaterialsSA-204 K11820 Grd A PlateSA-516 K02700 Grd 70 PlateSA-204 K11820 Grd A Plate

SA-204 K11820 Grd A PlateSA-179 K01200 Smls. tube

W/(m K)

Cylinder - hot sideCylinder - cold sideTubesheetDouble tubesheet (inner)BafflesTube material

Thermal conductivity of tube material

Tubesheet cladding - hot sideTubesheet cladding - cold sideGaskets - hot sideGaskets - cold side

Specifications

ASME Code Sec VIII Div 1

Program

ProgramProgram

bar °Cbar bar mm

Design Code

Service classTEMA classMaterial standardDimensional standard

Design pressureDesign temperatureVacuum design pressureTest pressureCorrosion allowance

Hot Side Cold Side

Thermal Analysis Options

Program

Program

Program

W/(m² K)

°C

kW/m²

°C

0

ProgramHot / Cold side fouling ratioFouling calculation options

Maximum number of design mode iterations

Hot Side Cold SideHeat transfer coefficientHeat transfer coefficient multiplierPressure drop multiplier

Percent of u-bend area used for heat transfer Maximum rating for thermosiphons

Mean temperature differenceMinimum allowable temperature approachMinimum allowable MTD Ft correction factor Maximum allowable heat fluxFlow direction for first tube pass

Simulation mode area convergence toleranceNumber of calculation intervalsType of interval calculation


8/24



Correlations

Program

ProgramProgram

°C

ProgramProgramProgram

ProgramProgramProgram

Program

Program

Cold SideHot Side

Outlet NozzleInlet Nozzle

Exiting tubesEntering tubes

VelocityHeadsForPressureDrop

Pressure Drop Options

Tube side two phase pressure drop correlation

Shell side flow analysis calculation method

Mist flow heat transfer calculation methodTube side two phase heat transfer correlationShell side two phase heat transfer correlation

Vaporization Options

Liquid subcooling heat transfer methodTube side two phase heat transfer correlationShell side two phase heat transfer correlation

Condensation Options

Shell side two phase pressure drop correlation

Minimum temperature difference for nucleate boilingSuppress nucleate boiling coefficient

Condensation heat transfer modelDesuperheating heat transfer method

Change Codes


9/24



Warnings and MessagesDescription

Note 23 Cold side flowrate has been set at 8.5747 kg/s to balance heat loads.

Note 588 A TEMA E shell with an odd number of horizontal cut single segmental baffles implies that theinlet and outlet nozzles should both be on the same side of the exchanger (top or bottom).

Warning 47 The databank has been referenced for HOT Side fluid physical properties. The temperaturerange for which properties were stored in the databank has been exceeded by one or more ofthe components. ALL properties for that component will be taken at the limit of the range exceptfor vapor pressure and viscosity which will be extrapolated.


10/24



Optimization Path

Shell Tube Length Pressure Drop Baffle Tube Units Total

Size Actual Reqd. Shell Tube Spacing No. Pass No. P S Price

mm mm mm bar bar mm Dollar(US)

1 609.6 2000 1346.3 0.0604 0.09712 152.4 11 2 446 1 1 27690


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Thermal Details - General

590

20

2000

8.57478.5747

kg/s

kg/s

°C

°C

W/(m² K)

m² K/W

m/s

bar

kW

W/(m² K)

m²°C

mm

mm

2.23862.2386

180450140120

177.45401.6

0.000180.00035

73.660.22

0.097120.140.06040.34

724.1

138.7

54.3145.18

0.95

BEM

2

single seg446

hor 1 1

24 hor %

Gases (in/out)

Liquids (in/out)

Temperature (in/out)

Dew point or bubble point

Film coefficient

Fouling resistance

Velocity

Pressure drop (allow./calc.)

Total heat exchanged

Overall coef. - dirty

Effective surface areaMTD corrected

MTD Ft correction factor

Shell Side Tube Side

Type

Shell size

Tube No-ODBaffles

Tube passes

ser par

Thermal Details - Thermal Resistances

33.2m²

63.56

150.3

0.00665

W/(m² K)

m² K/W

m² K/W

2.78

0.41

35.9

50.96

138.7

0.00721

0.00035

0.00018

2.57

4.86

0.38

2.85

54.3

91.9

0.01088

0.00266

0.00137

1.7

24.48

0.25

14.38

96.8 89.34 59.19

0.00003

%Tube side film

Tube side fouling

Max. foulSpec. foulClean

%

%

%

%

Tube wall

Shell side fouling

Shell side film

Distribution of overall resistance

Tube side fouling (at tube ID)

Shell side fouling

Overall resistance

Overall coefficient

%Excess surface

Area reqd.

0.0

0.0

0.0

0.0


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Thermal Details - Coefficients

W/(m² K)

°C

177.4

1

177.4

26113.95

144.21

5401.6

18097.49

1

130.01

177.4

5401.6

1

5401.6

Gamma factor

Beta factor

Tube SideShell Side

Mean metal temperature

Fin efficiency factor

Reynolds number Liquid cooling coefficient

Boiling coefficient

Liquid sensible coefficient

Condensing coefficient

Desuperheating coefficient

As used in design

User specified multiplier

As specified by user in input

As calculated by programFilm coefficients

Vapor sensible coefficient

Thermal Details - MTD and Flux

°C

145.18

152.23

0.95

145.18

13.3

kW/m²

MTD delta correction factor

Flux

Actual flux

Boiling fluid

Nucleate maximum flux

Program maximum flux

Specified maximum flux

Controlling maximum flux

Mean temperature difference

Corrected MTD used in design

LMTD

MTD Ft correction factor

Long. baffle efficiency factor

Calculated corrected MTD

User specified corrected MTD

Flow direction


13/24



Thermal Details - Pressure Drop

0.34

bar

m/s m/s

0.06040.07423

1

0.14

0.097120.098

1

0.86

0.22

0.17

0.88

1.14

17.31

43.6

4.7

14.7

4.98

88.42

73.66

55.39

40.77

9.47

76.27

5.93

3.21

bar

0.01046

0.02633

0.00284

0.00888

0.00301

0.0092

0.07407

0.00576

0.00312

bar

1.12 0.00888 14.7 65.08 0.00498 5.12

Outlet piping

Inlet piping

Pressure Drop

Allowable

Calculated, cleanCalculated, dirty

User specified bundle multiplier

Inlet nozzle

Velocity and pressure drop

Entering bundle

Crossflow

Through baffle windows

Through tubes

Exiting bundle

Outlet nozzle

Shell Side Tube Side

%dp %dp

Thermal Details - Shell Side Stream Analysis

1188

3058

712

3116

42.19

25.94

24.28

7.6

699

2232

5953

5953

5953

5953

0.79

4.76

11.11

mm

kg/(m s²)kg/(m s²)

1208Outlet nozzle

Stream F: Pass lanes

Diametric clearancesFlow fraction

Shell exit

Bundle exit

Bundle entrance

Shell entrance

Rho*V2 analysis

Inlet nozzle

Stream E: Shell ID - bundle OTL

Stream C: Baffle OD - shell ID

Stream A: Baffle hole - tube OD

Stream B: Crossflow

TEMA limitRho*V2

Shell Side Stream Analysis%


14/24



Mechanical Details - Setting Plan

3080

845 2000 235

0

3 3 7

3 3 7

6 0 0

1 4 0 0

1 8 1 6

1 8 4

Front Head 6 1 0

Shell 6 1 0

Rear Head 6 1 0

Mechanical Details - Tube Layout

1 32 103 134 145 176 187 198 209 2110 2211 2112 2213 23

14 2315 2216 2117 2218 2119 2020 1921 1822 1723 1424 1325 1026 3

446

Shell IDO.T.L.

590.5 mm579.4 mm

Baffle cut to C/L 147.8 mm

25

12.5

21.65

223

223


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Mechanical Details - Shell

609.6mm

590.55

101.6

101.6

609.6

590.55

304.8

304.8

1

1

1

1

1 1 1

BEM

mm

mm

mm

mm

mm

mm

mm

mm

mm

27690Dollar(US)Total price

TEMA type:

Cylinder outside diameter

Cylinder inside diameter

Kettle outside diameter

Vapor belt outside diameter

Vapor belt length

Inlet nozzle

Outlet nozzle

Drain

Inlet dome

Distributor belt

Nozzles - nominal OD / quantity

Arrangement - total shells: Connected in parallel series

Shell Side

Shell Front head

Tube Side

Mechanical Details - Bundle

mm

single seg

206.25

152.4206.25

11

24

3.18

11.11

0.79

4.766.35

None

579.44

7.53

7.53

hor

mm

mm

mm

mmmm

mm

mm

mm

15.88mm

2000

31.75

mm

mm

mm

mm

Tube length

Tubesheet thickness (est.)

Pass partition lane widthNumber of baffles

Inlet spacing

C-C spacingOutlet spacing

Baffle type

Supports

Triple segmental intermediate cut

Baffle thickness

Impingement protection

Sealing strips (pairs)

Outer tube limit

Open distance at top

Baffle hole - tube od clearance

Shell id - baffle od clearanceBaffle od - bundle otl clearance

Shell id - bundle otl clearance

Double/triple segmental outer cut

Baffle cut %

%

%

Open distance at bottom


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Mechanical Details - Tubes

mm

mm 20

1.24

avgPlain

1.14

mm

mm

mm

mm

mm

mm

#/m

mm

2000

446

2530

2

31.75

exp./seal wld

15.88

RibbonTube pass layout

Twist ratio

Twisted tape insert width

%

Tube o.d.

Tube wall thickness

Tube wall specificationTube type

Fin height

Fin thickness

Fin density

Area ratio Ao/Ai

Deviation in tubes/pass

Pass partition lane width

Tube-tubesheet joint

Tubesheet thickness (est.)

Tube passes

Tube patternTube pitch

Number of tubes

Tube length


17/24



Mechanical Details - Vibration Analysis

0.4

000

0.4

mm

no

358.650.86

13.04

0.07

459.9

no

304.80.22

11.62

0.02

409.9

no

358.650.88

13.1

0.07

461.9

no

m/s

m/s

Hz

mm

mm

Turbulent buffeting amplitude limit

Vortex shedding amplitude limit

Turbulent buffeting amplitude

Vortex shedding amplitude

Vibration Indication

Tube unsupported span

Tube natural frequency

Crossflow velocity

Critical velocity

Vibration indicated if > 1.0

Inlet Bundle Outlet U-bend

Crossflow/critical velocity

v

vc

v/vc

fn

For liquids and gases

Mechanical Details - Acoustic Analysis

mm

no

358.650.86

no

304.80.22

no

358.650.88

no

9.6 2.4 9.8

m/s

Hz

Hz

Hz

m/s

m/s

and Condition "c" > 2000Resonance indicated if v > "c" velocity

For gases only

Resonance indicated if v > "b" velocity

Vortex shedding frequency

U-bendOutletBundleInlet

Turbulent buffeting frequency

Shell acoustic frequency

Crossflow velocityTube unsupported span

Condition "b" velocity

Resonance indicated if 0.8 - 1.2

Condition "a" ratio

Acoustic resonance indication

Condition "c"-

Condition "c" velocity

lv

fa

fs

ftb

fa/fs

fa/ftb


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19/24



Recap of Designs

A

Shell size mm 609.6

Tube length - actual mm 2000

Tube length - required mm 1346.3

Pressure drop, SS bar 0.0604

Pressure drop, TS bar 0.09712

Baffle spacing mm 152.4

Number of baffles 11

Tube passes 2

Tube number 446

Number of units in series 1

Number of units in parallel 1

Total price Dollar(US) 27690

RhoV2 problem no

Vibration problem no


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Calculation Details - Shell Side - Liquid Properties

Temperature Density Specific Thermal Viscosity

bulk wall heat conductivity bulk wall

°C °C kg/m³ kJ/(kg K) W/(m K) mPa s mPa s120 136.26 942.78 4.209 0.687 0.242 0.215

121.83 137.18 941.19 4.211 0.687 0.239 0.214

123.64 138.69 939.61 4.213 0.687 0.235 0.211

125.46 140.37 938.02 4.215 0.687 0.232 0.209

127.29 142.04 936.44 4.217 0.687 0.229 0.207

129.11 143.71 934.86 4.22 0.688 0.226 0.204

130.93 145.38 933.28 4.222 0.688 0.223 0.202

132.75 147.05 931.7 4.224 0.688 0.22 0.2

134.57 148.72 930.12 4.226 0.688 0.218 0.198

136.38 150.38 928.54 4.228 0.688 0.215 0.195

138.19 152.7 926.96 4.23 0.689 0.212 0.193

140 925.39 4.232 0.689 0.21

Calculation Details - Shell Side - Heat Load

Temp. Flow rate Sensible heat Total

Liquid Liquid load

°C kg/s kW kW120 8.5747

121.83 8.5747 65.8 65.8

123.64 8.5747 131.7 131.7

125.46 8.5747 197.5 197.5

127.29 8.5747 263.3 263.3129.11 8.5747 329.1 329.1

130.93 8.5747 395 395

132.75 8.5747 460.8 460.8

134.57 8.5747 526.6 526.6

136.38 8.5747 592.4 592.4

138.19 8.5747 658.3 658.3

140 8.5747 724.1 724.1


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Calculation Details - Shell Side - Performance

Temp. Heat load Overallcoefficient

Area reqd. Temperaturedifference

Pressuredrop

°C % W/(m² K) % °C %

Inlet 120 32.02121.83 9.09 138.1 9.13 145.18 2

123.64 9.09 138.7 9.09 145.18 4.34

125.46 9.09 138.8 9.09 145.18 4.94

127.29 9.09 138.8 9.08 145.18 4.94

129.11 9.09 138.9 9.08 145.18 4.94

130.93 9.09 138.9 9.08 145.18 4.94

132.75 9.09 138.9 9.08 145.18 4.94

134.57 9.09 138.9 9.08 145.18 4.94

136.38 9.09 138.9 9.08 145.18 4.94

138.19 9.09 138.9 9.08 145.18 4.94

140 9.09 138.4 9.12 145.18 2.45Outlet 140 19.68

Calculation Details - Shell Side - Coefficients

Temp. Flow rate Velocity Coefficients

bulk Pr Re regime X-flow Window free forced Actual

°C m/s m/s W/(m² K) W/(m² K) W/(m² K)120.91 1.47 12506.18 Turbulent 0.22 0.17 1263.5 4579.5 4579.5

122.73 1.45 16237.94 Turbulent 0.22 0.17 1267.8 5328.3 5328.3

124.55 1.43 17390.66 Turbulent 0.22 0.17 1271.1 5538 5538

126.38 1.42 17625.58 Turbulent 0.22 0.17 1272.3 5558.8 5558.8

128.2 1.4 17861.51 Turbulent 0.22 0.17 1277.6 5579.5 5579.5

130.02 1.38 18097.49 Turbulent 0.22 0.17 1280.8 5600.1 5600.1

131.84 1.36 18334.42 Turbulent 0.22 0.17 1284 5620.6 5620.6

133.66 1.34 18572.3 Turbulent 0.22 0.17 1287.1 5641 5641

135.48 1.33 18811.1 Turbulent 0.22 0.17 1290.3 5661.3 5661.3

137.29 1.31 19049.89 Turbulent 0.22 0.17 1295.4 5681.4 5681.4

139.09 1.3 15023.24 Turbulent 0.22 0.17 1296.3 4895.3 4895.3


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Calculation Details - Tube Side - Vapor Properties

Temperature Density Specific Thermal Viscosity

bulk wall heat conductivity bulk wall

°C °C kg/m³ kJ/(kg K) W/(m K) mPa s mPa s450 155.72 0.47 1.24 0.053 0.032 0.023

426.22 153.45 0.49 1.232 0.051 0.032 0.023

402.28 151.2 0.5 1.225 0.049 0.031 0.023

378.19 148.99 0.52 1.217 0.048 0.03 0.023

353.95 146.81 0.54 1.209 0.046 0.029 0.023

329.54 144.67 0.57 1.201 0.044 0.028 0.023

305 142.56 0.59 1.194 0.042 0.028 0.023

280.29 140.5 0.62 1.186 0.04 0.027 0.023

255.43 138.48 0.65 1.179 0.039 0.026 0.023

230.43 136.5 0.68 1.172 0.037 0.025 0.023

205.27 134.57 0.71 1.166 0.035 0.024 0.023

180 0.75 1.161 0.033 0.023

Calculation Details - Tube Side - Heat Load

Temp. Total

Vapor Vapor load

°C kg/s kW kW450 2.2386

426.22 2.2386 65.8 65.8

402.28 2.2386 131.7 131.7

378.19 2.2386 197.5 197.5

353.95 2.2386 263.3 263.3329.54 2.2386 329.1 329.1

305 2.2386 395 395

280.29 2.2386 460.8 460.8

255.43 2.2386 526.6 526.6

230.43 2.2386 592.4 592.4

205.27 2.2386 658.3 658.3

180 2.2386 724.1 724.1


23/24



Calculation Details - Tube Side - Performance

Temp. Heat load Overallcoefficient

Area reqd. Temperaturedifference

Pressuredrop

°C % W/(m² K) % °C %

Inlet 450 14.59426.22 9.09 148.4 8.5 145.18 7.57

402.28 9.09 146.6 8.61 145.18 7.46

378.19 9.09 144.7 8.71 145.18 7.34

353.95 9.09 142.9 8.83 145.18 7.22

329.54 9.09 141 8.94 145.18 7.09

305 9.09 139.1 9.07 145.18 6.96

280.29 9.09 137.2 9.2 145.18 6.82

255.43 9.09 135.2 9.33 145.18 6.68

230.43 9.09 133.3 9.46 145.18 6.53

205.27 9.09 131.3 9.6 145.18 6.38

180 9.09 129.4 9.75 145.18 6.21Outlet 180 9.14

Calculation Details - Tube Side - Coefficients

Temp. Flow Velocity Coefficients

bulk Pr Re regime free forced Actual

°C m/s W/(m² K) W/(m² K) W/(m² K)438.11 0.76 22816.72 Turbulent 86.94 191.2 191.2

414.25 0.76 23388.01 Turbulent 84.01 188.6 188.6

390.24 0.77 23998.21 Turbulent 81.06 186 186

366.07 0.77 24652.08 Turbulent 78.1 183.3 183.3

341.74 0.77 25355.15 Turbulent 75.12 180.6 180.6

317.27 0.78 26113.95 Turbulent 72.13 177.9 177.9

292.64 0.78 26936.6 Turbulent 69.12 175.1 175.1

267.86 0.78 27832.5 Turbulent 66.09 172.4 172.4

242.93 0.79 28812.61 Turbulent 63.05 169.6 169.6

217.85 0.79 29892.12 Turbulent 59.99 166.8 166.8

192.64 0.8 31088.71 Turbulent 56.9 164.1 164.1


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Calculation Details -

°C

°C

°Cm²

W/(m² K)

kW

°C

815.1

150.3

54.3

99.92

120 142.53

450 146.93

804.7

138.7

54.3

106.88

120 142.24

450 150.81

212.43146.93

218.98150.81

876

54321Outlet temperature for pass

Exchanger Clean Dirty

Heat exchanged

Transfer rateEffective surface area

Corrected MTD

Shell side temperature in/out

Tube side temperature in/out

thermal design calculation procedure (rev 00)

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