Assembly Design Shell And Tube Heat Exchanger ASME TEMA

Heat Exchanger Manufacturer, Assembly and Design of Shell and Tube Heat Exchanger as per ASME and TEMA

What is shell and tube heat exchanger (STHE)?

A shell and tube heat exchanger (STHE) is the most widely used type of heat exchanger in industrial applications due to its robustness, versatility, and ability to handle high pressures and temperatures. It consists of a shell (a large pressure vessel) with a bundle of tubes inside. One fluid flows through the tubes (tube side), and the other flows outside the tubes within the shell (shell side). Heat is transferred between the two fluids through the tube walls.

STHEs are governed by two key standards:

1.ASME Boiler and Pressure Vessel Code (BPVC), Section VIII, Division 1: Ensures pressure vessel safety.

2.TEMA (Tubular Exchanger Manufacturers Association) Standards: Defines mechanical design, tolerances, and fabrication practices.

Key Technical Details as per ASME and TEMA

1.Design Standards

ASME BPVC Section VIII, Div. 1:

 -Covers pressure boundary design (shell, tubesheets, channels).

 -Requires calculations for minimum thickness, nozzle reinforcement, and hydrostatic testing.

TEMA Standards (Classes R, C, B):

 -Class R: Severe refinery and process applications (high pressures/temperatures).

 -Class C: General commercial/industrial service.

 -Class B: Chemical process service (corrosive environments).

2. Components & Configuration

TEMA Designation Example:

AES:

 -A: Front head (bolted cover).

 -E: One-pass shell.

 -S: Floating rear head (pull-through bundle).

3. Thermal Design

Heat Duty (Q):Q=U⋅A⋅ΔTLMTD​

 -U: Overall heat transfer coefficient (W/m²·K).

 -A: Heat transfer area (tube OD × length × number of tubes).

 -ΔTLMTD​: Log Mean Temperature Difference (corrected for flow arrangement).

Flow Arrangements:

 -Counterflow: Highest thermal efficiency.

 -Parallel Flow: Simpler but lower efficiency.

 -Crossflow: Common in condensers.

Effectiveness-NTU Method:
 -Used for complex flow arrangements or variable fluid properties.

4. Mechanical Design

Shell & Tube Dimensions:

 -Shell ID: Determined by tube bundle layout (triangular, square, rotated square).

 -Tube pitch: Minimum 1.25 × tube OD (to allow cleaning).

Baffle Design:

 -Segmental baffles (20–50% cut) with spacing per TEMA (min 1/5 shell ID or 2").

 -No-Tubes-In-Window (NTIW): Eliminates dead zones.

Pressure Drop:

 -Shell side: Optimized via baffle spacing/cut.

 -Tube side: Function of fluid velocity and tube length.

5. Material Selection

6. ASME Compliance & Testing

Hydrostatic Test:

 -1.5 × design pressure (ASME VIII-1 UG-99).

 -Test both shell and tube sides separately.

Pneumatic Test:

 -1.1 × design pressure (if hydrostatic testing is impractical).

NDT Requirements:

 -RT (radiographic testing) for welds.

 -PT (dye penetrant) or MT (magnetic particle) for surface cracks.

7. Common Applications

Oil & Gas: Preheaters, coolers, condensers.

Power Plants: Steam condensers, feedwater heaters.

Chemical Industry: Reactor cooling, distillation.

HVAC: Chillers, district heating.

Advantages & Limitations