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Shell and Tubes Heat Exchanger
     
 

Screenshot from INSTED Thermodynamic Analysis program

Capabilities

Rating (Performance Analysis)
Calculation of the heat transfer rate
Calculation of the outlet temperatures
Preliminary Design
The program optimizes with respect to a number of parameters including shell diameter, number of shell passes, tube length, and number of tube passes. Criteria considered include minimum heat transfer area, minimum pressure drop, and minimum power or a combination of these factors.
Options for Shell-Side Analysis
Kern's integral method
Bell-Delaware method
Stream analysis method
System Configuration
Multiple tube passes, multiple shell passes, multiple shells in series, shells in parallel.
Phase Change Capabilities
Single-phase analysis
Two-phase analysis

Boiling in tube, boiling in shell, condensation in tube,
    condensation in shell, multi-component analysis
Non-condensable

Module Integration
INSTED/Database modules used:

Fluid thermophysical properties
Exchanger material conductivity
Tube counts
Fouling resistance
Roughness data
Friction factor calculation

Links to the Fin Analysis program for calculation of fin resistance and efficiency
Tube Types
 Plain tubes, Integral low, Finned tubes
Tube Layout
 Triangle, rotated triangle, square, rotated square
Baffle Types
 Segmented, no tubes in window, strip baffles
Baffle Options
 Even baffle spacing, Uneven baffle spacingf
Shell and Tube Dimenions
 No limit
Exchanges in Series and Parallel
 No limit

Program Interaction

Required Input for Rating Analysis
Method for shell analysis
Tube configuration
Number of tubes
Number of tube passes
Number of shell passes
Tube length
Tube bundle diameter
Sealing strip pairs
Shell pass partition
Baffle spacing, baffle cut, baffle-shell leakage, baffle-tube leakage.
For each fluid:
 Density, specific heat, viscosity, thermal conductivity (or selection of a fluid from the Database)
Tube/shell mass or volume flow rate
Tube/shell diameter
Absolute roughness of tube inner and outer walls
Thermal conductivity of tubes
Fouling resistance in inner and outer tube walls
Results from Rating Analysis
 Heat transfer rate, heat transfer area, U, UA, effectiveness, LMTD, NTU
For each stream:
 Velocity, Reynolds number, heat transfer coefficient, Nusselt number, friction factor, pressure loss, power
Results from Design Analysis
 Several design realizations as a function of the number of tube and shell passes, number of tubes, length of tubes, heat transfer rate, pressure drops, and flow rates

Shell and Tube Heat Exchanger Module

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