heat exchangers design and construction

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Heat Exchangers Design and Construction. Chemicoz. Introduction:. Shell and tube heat exchangers are one of the most common equipment found in all plants. How it works?. What are they used for?. Classification according to service . . Heat Exchanger. - PowerPoint PPT Presentation

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Page 1: Heat Exchangers  Design and Construction

Chemicoz

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Page 2: Heat Exchangers  Design and Construction

Shell and tube heat exchangers are one of the most common equipment found in all plants

How it works?

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Page 3: Heat Exchangers  Design and Construction

Heat Exchanger

Cooler

Heater

Condenser

Reboiler

Both sides single phase and process stream

One stream process fluid and the other cooling water or air

One stream process fluid and heating utility as steam

One stream condensing vapor and the other cooling water or air

One stream bottom stream from a distillation column and the other a hot utilityor process stream

Classification according to service .

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Page 4: Heat Exchangers  Design and Construction

Code

Standard

Specifications

Is recommended method of doing something ASME BPV – TEMA

is the degree of excellence requiredAPI 660-ASME B16.5–ASME B36.10M–ASME B36.19-ASME B16.9–ASME B16.11

Is a detailed description of construction, materials,… etc Contractor or Owner specifications

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Page 5: Heat Exchangers  Design and Construction

2- Channel3- Channel Flange4- Pass Partition5- Stationary Tubesheet6- Shell Flange7- Tube

8- Shell9- Baffles 10- Floating Head backing Device11- Floating Tubesheet12- Floating Head13- Floating Head Flange14 –Shell Cover

1- Channel Cover

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Page 6: Heat Exchangers  Design and Construction

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Page 7: Heat Exchangers  Design and Construction

Front Head TypeFront Head Type

A - Type B - Type C - Type

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Page 8: Heat Exchangers  Design and Construction

Shell TypeShell Type

E - Type F - Type

J - TypeK - Type

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Page 9: Heat Exchangers  Design and Construction

Rear End Head TypesRear End Head Types

M - Type S - Type T - TypeFixed Tubesheet Floating Head Pull-Through

Floating Head

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Page 10: Heat Exchangers  Design and Construction

U-Tube Heat ExchangerU-Tube Heat Exchanger

Fixed Tubesheet Heat ExchangerFixed Tubesheet Heat Exchanger

Floating Tubesheet Heat exchangerFloating Tubesheet Heat exchanger

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Page 11: Heat Exchangers  Design and Construction

AES11

Page 12: Heat Exchangers  Design and Construction

AKT12

Page 13: Heat Exchangers  Design and Construction

Terminology Design data Material selection Codes overview Sample calculations Hydrostatic test Sample drawing

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Page 14: Heat Exchangers  Design and Construction

ASME TEMA API MAWP MDMT PWHT NPS – DN – NB – NPT Sch - BWG

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Page 15: Heat Exchangers  Design and Construction

Heat Exchanger Data Sheet :

Design pressure Design temperature Dimensions / passes Tubes ( dimensions, pattern) Nozzles & Connections

TEMA type

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Baffles (No. & Type)

Page 16: Heat Exchangers  Design and Construction

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Page 17: Heat Exchangers  Design and Construction

A – Yield StrengthA – Yield Strength

B – Tensile StrengthB – Tensile Strength

C – Rupture C – Rupture pointpoint

AB

C

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Page 18: Heat Exchangers  Design and Construction

Creep Strength a slow plastic strain increased by time and temperature

(time and temperature dependant) for stressed materials

Fatigue Strength The term “fatigue” refers to the situation where a

specimen breaks under a load that it has previously withstood for a length of time

Toughness The materials capacity to absorb energy, which, is

dependant upon strength as well as ductility

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Page 19: Heat Exchangers  Design and Construction

ASME code OverviewASME code Overview

ASME BPV code

Sec.I Power Boilers

Sec.II Materials

Sec.III Nuclear Fuel Containers

Sec.IV Heating Boilers

Sec. V Non Destructive Examination

Sec. VI Operation of heating boilers

Sec. VII Operation of power boilers

Sec. VIII Pressure vessels

Sec. IX Welding and Brazing

Sec. X Fiber-Reinforced plastic PV

Sec. XI Inspection of nuclear power plant

Sec. XII Transport tanks

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Page 20: Heat Exchangers  Design and Construction

ASME code overviewASME code overview Sec. II: Materials

Part A : Ferrous material specifications Part B : Non-Ferrous material specifications Part C : Specifications of welding rods, electrodes and filler

metals Part D : Properties

Sec. VIII: Rules of construction of pressure vessels Division 1 : 3 Subsections + mandatory Annex + non mandatory Annex Division 2: Alternative rules Division 3 : Alternative rules of high pressure

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Page 21: Heat Exchangers  Design and Construction

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ASME code overviewASME code overview

Page 22: Heat Exchangers  Design and Construction

TEMA code overviewTEMA code overview TEMA classes:

Class R: Generally severe requirements for petroleumand related processing applications

Class C: Generally moderate requirements of commercialand general processing applications

Class B: Chemical Process service

TEMA subsections 10 subsection

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Page 23: Heat Exchangers  Design and Construction

Sample CalculationsSample Calculations Shell thickness calculations under Internal Pressure:

t : Min. Required Shell Thickness P : Design Pressure of Shell Side S: Max. Allowable Stress of Shell Material R: Shell Inside Radius (corroded conditions) E : Joint Efficiency CA: Corrosion Allowance UT: Under Tolerance (if applicable)

PR .SE – 0.6 P + CAt = + UT

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Page 24: Heat Exchangers  Design and Construction

Sample CalculationsSample Calculations Channel thickness calculations under Internal Pressure:

t : Min. Required Channel Thickness P : Design Pressure of Tube Side S: Max. Allowable Stress of Channel Material R: Channel Inside Radius (corroded conditions) E : Joint Efficiency CA: Corrosion Allowance UT: Under Tolerance (if applicable)

PR .SE – 0.6 P + CAt = + UT

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Page 25: Heat Exchangers  Design and Construction

Sample CalculationsSample Calculations Body Flanges:

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Page 26: Heat Exchangers  Design and Construction

Sample CalculationsSample Calculations Body Flanges:

Trial and error calculations Gasket seating conditions

No. of bolts and size Bolt circle diameter Inside and outside diameters Check min. and max. bolt spacing

Detailed analysis of the flange Forces calculations Moment calculations Stresses calculations

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Operating conditions

Page 27: Heat Exchangers  Design and Construction

Sample CalculationsSample Calculations Precautions in body flanges design and installations: Pairs of flanges Bolt holes shall straddle center line Corrosion Allowance

Bolts shall be multiple of 4 Bolting shall be allowed to be removed from either side

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Calculated thickness not include the RF

Cladding

Page 28: Heat Exchangers  Design and Construction

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Sample CalculationsSample Calculations Nozzles and standard flanges:

Flange Rating (ASME B16.5)

Nozzle neck thickness calculations

Area replacement calculations

Sample

Impingement protection

Page 29: Heat Exchangers  Design and Construction

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Sample CalculationsSample CalculationsTubesheet:• Tubesheet is the principal barrier between shell side and tube

side

• Tubes shall be uniformly distributed

• Tubesheet thickness shall be designed for both sides

• Tubesheet shall be designed for bending stresses and shear stresses

• Corrosion allowance

• Made from around flat piece of metal with holes drilled for the tubes

Page 30: Heat Exchangers  Design and Construction

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Sample CalculationsSample CalculationsTubesheet:• Tubesheet thickness for bending

T: Effective tubesheet thicknessS: Allowable stressP: Design pressure corrected for vacuum if applicable at the other sideη: Ligament efficiency

For Square pattern

For Triangular pattern

G: Gasket effective diameterF: Factor

Page 31: Heat Exchangers  Design and Construction

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Sample CalculationsSample CalculationsTubesheet:• Tubesheet thickness for Shear:

T: Effective tubesheet thicknessDL: Effective diameter of the tube center parameter DL=4A/C C: Perimeter of the tube layout A: Total area enclosed by the Perimeter C P: Design pressureS: Allowable stressdo: Outside tube diameter

Page 32: Heat Exchangers  Design and Construction

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Tube-to-Tubesheet Tube-to-Tubesheet jointjointExpanded

Seal welded

Strength welded

Page 33: Heat Exchangers  Design and Construction

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Hydrostatic TestHydrostatic Test

Test pressure : 1.3 X MAWP

Test Procedure

Gasket change

Page 34: Heat Exchangers  Design and Construction

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Sample drawingSample drawingConstruction drawing is the design output

Sample drawing 1 Sample drawing 2