heat-exchanger-design

name	heat-exchanger-design
description	Specialized skill for heat exchanger sizing, rating, and optimization per TEMA standards including shell-and-tube, plate, and air-cooled configurations
allowed-tools	["Read","Write","Glob","Grep","Bash"]
metadata	{"specialization":"mechanical-engineering","domain":"science","category":"thermal-fluid-analysis","priority":"high","phase":6,"tools-libraries":["HTRI Xchanger Suite","Aspen Exchanger Design and Rating"]}
graph	{"domains":["domain:mechanical-engineering"],"skillAreas":["skill-area:physics-simulation","skill-area:mathematical-reasoning","skill-area:motion-planning"],"roles":["role:systems-integration-engineer","role:research-engineer"]}

Heat Exchanger Design Skill

Purpose

The Heat Exchanger Design skill provides comprehensive capabilities for sizing, rating, and optimizing heat exchangers according to TEMA standards, enabling systematic thermal-hydraulic design of shell-and-tube, plate, and air-cooled heat exchanger configurations.

Capabilities

• Shell-and-tube heat exchanger design and rating
• Plate heat exchanger sizing
• Air-cooled heat exchanger configuration
• LMTD and effectiveness-NTU methods
• Fouling factor consideration
• Pressure drop calculations
• HTRI Xchanger Suite integration
• Thermal-hydraulic optimization

Usage Guidelines

Design Methods

LMTD Method

1. Log Mean Temperature Difference

   LMTD = (ΔT1 - ΔT2) / ln(ΔT1/ΔT2)
   
   Q = U × A × F × LMTD
   
   Where:
   F = Correction factor for non-counterflow
   U = Overall heat transfer coefficient
   A = Heat transfer area
   

2. LMTD Correction Factors

   • One shell pass, 2/4/6 tube passes
   • Two shell passes, 4/8 tube passes
   • Crossflow configurations

Effectiveness-NTU Method

1. Effectiveness Definition

   ε = Q_actual / Q_max
   Q_max = Cmin × (Th,in - Tc,in)
   

2. NTU Calculation

   NTU = UA / Cmin
   Cr = Cmin / Cmax
   

3. Effectiveness Relations

   • Counterflow: ε = (1-exp(-NTU(1-Cr)))/(1-Cr×exp(-NTU(1-Cr)))
   • Parallel flow: ε = (1-exp(-NTU(1+Cr)))/(1+Cr)
   • Shell-and-tube: Complex correlations by TEMA type

Shell-and-Tube Design

1. TEMA Designations

   Front End	Shell	Rear End
   A - Channel	E - One-pass	L - Fixed tubesheet
   B - Bonnet	F - Two-pass	M - Fixed tubesheet
   N - Channel	J - Divided flow	N - Fixed tubesheet
   -	X - Crossflow	P - Outside packed
   -	-	S - Floating head
   -	-	U - U-tube

2. Tube Layout

   • Triangular pitch (30°): Maximum tubes, poor cleaning
   • Square pitch (90°): Mechanical cleaning possible
   • Rotated square (45°): Higher turbulence

3. Baffle Design

   • Segmental: 20-45% cut
   • Double segmental: Reduced pressure drop
   • No-tubes-in-window: Vibration mitigation

Plate Heat Exchanger

1. Plate Selection

   • Chevron angle (25-65°): Trade-off h vs ΔP
   • Plate spacing: 2-5 mm typical
   • Pass arrangement: U or Z configuration

2. Design Considerations

   • Maximum pressure: 25-30 bar typical
   • Maximum temperature: 150-200°C (gaskets)
   • Fouling service: Not ideal

Air-Cooled Heat Exchanger

1. Configuration

   • Forced draft: Fan below bundle
   • Induced draft: Fan above bundle
   • Natural draft: No fan (limited duty)

2. Design Parameters

   • Face velocity: 2.5-3.5 m/s
   • Tube rows: 3-6 typical
   • Fin density: 275-435 fins/m

Fouling Considerations

Service	Fouling Factor (m²K/kW)
Cooling water	0.2-0.35
River water	0.35-0.5
Fuel oil	0.5-0.9
Heavy hydrocarbons	0.35-0.7
Light hydrocarbons	0.1-0.2
Steam (clean)	0.05-0.1

Process Integration

• ME-012: Heat Exchanger Design and Rating
• ME-011: Thermal Management Design

Input Schema

{
  "design_type": "sizing|rating",
  "exchanger_type": "shell_tube|plate|air_cooled",
  "hot_fluid": {
    "name": "string",
    "flow_rate": "number (kg/s)",
    "inlet_temp": "number (C)",
    "outlet_temp": "number (C, for sizing)"
  },
  "cold_fluid": {
    "name": "string",
    "flow_rate": "number (kg/s)",
    "inlet_temp": "number (C)",
    "outlet_temp": "number (C, for sizing)"
  },
  "pressure_constraints": {
    "hot_side_max_dp": "number (kPa)",
     
  
   
     
     
  

Output Schema

{
  "duty": "number (kW)",
  "geometry": {
    "type": "string (TEMA designation or plate type)",
    "area": "number (m2)",
    "shell_diameter": "number (mm)",
    "tube_count": "number",
    "tube_length": "number (m)"
  },
  "thermal": {
    "LMTD": "number (C)",
    "F_factor": "number",
    "U_clean": "number (W/m2K)",
    "U_dirty": "number (W/m2K)"
  },
  "hydraulic": {
    "shell_side_dp": "number (kPa)",
    "tube_side_dp" 
  
   
     
     
  

Best Practices

1. Always include fouling factors appropriate for the service
2. Verify pressure drop constraints are met on both sides
3. Check for vibration potential in shell-and-tube designs
4. Consider maintenance access in configuration selection
5. Apply TEMA tolerances for manufacturing variations
6. Use conservative correlations for preliminary sizing

Integration Points

• Connects with CFD Analysis for detailed flow distribution
• Feeds into HVAC System Design for system integration
• Supports Thermal Analysis for component-level design
• Integrates with Process Design for plant-level optimization