Shell and Tube Heat Exchanger Design

The flow pattern in a shell and tube heat exchanger is typically not exactly counterflow or parallel flow, as with a double pipe heat exchanger. Rather, the flow pattern is typically some mix of counterflow, parallel flow and crossflow. The log mean temperature difference, which is used for shell and tube heat exchanger design, works for most of the varied flow patterns that occur in this type of heat exchanger. The general configuration and terminology for shell and tube heat exchangers is covered in 'Types of Shell and Tube Heat Exchangers'. This article will pick up from there.

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A straight tube shell and tube heat exchanger has a tube sheet and a plenum at both ends as shown in the lower two diagrams. The straight tube heat exchanger shown at the right has one tube pass and the one on the left has two tube passes.

The required heat transfer surface area for a shell and tube heat exchanger design is typically found from the basic heat exchanger equation: Q = UA ΔT_lm, where:

Q = rate of heat transfer between the two heat exchanger fluids, Btu/hr,

U = overall heat transfer coefficient, BTU/hr-ft²-^oF,

A = heat transfer surface area, ft²,

ΔT_lm = log mean temperature difference in ^oF, calculated from the inlet and outlet temperatures of the two fluids.

The basic heat exchanger equation, and the above parameters, are discussed in 'Fundamentals of Heat Exchanger Design'. An example calculation with the basic heat transfer equation is given in 'Preliminary Heat Exchanger Design Example'.

If the required flow rate and temperature change of one of the fluids is known along with the flow rate and one temperature for the other fluid (or both temperatures for the other fluid), an estimate for the heat transfer coefficient, and the shell and tube heat exchanger flow pattern to be used, then the required heat transfer area can be calculated using the basic heat exchanger equation.

After the needed heat transfer surface area is calculated, an appropriate diameter, length and number for the tubes can be determined and the shell can be sized and designed. The tube sheets and baffles will also need to be designed.

Shell and tube heat exchanger cutaway diagram - http://www.daviddarling.info/encyclopedia/H/AE_heat_exchanger.html

Shell and tube heat exchanger flow diagrams - http://en.wikipedia.org/wiki/Shell_and_tube_heat_exchanger

Dr. Harlan Bengtson is a registered professional engineer with 30 years of university teaching experience in engineering science and civil engineering. He holds a PhD in Chemical Engineering.

Types of Shell and Tube Heat Exchangers - The shell and tube heat exchanger is the most widely used industrial heat exchanger type. The wall of the heat exchanger tube is the heat transfer surface. It can have a U-tube heat exchanger or straight tube heat exchanger configuration. The tube side fluid can have one, two, or four passes.

Fundamentals of Heat Exchanger Design - The primary size parameter calculated in heat exchanger design is the area of the heat transfer surface. In order to make the heat exchanger calculations, the parameters needed are the overall heat transfer coefficient, the heat transfer rate, and the log mean temperature difference.

Combined Conduction Heat Transfer and Convection Heat Transfer - Heat transfer by a convection conduction combination can be analyzed using conductive thermal resistance and convective thermal resistance. These thermal resistances are functions of thermal conductivity, convective heat transfer coefficient, and geometrical parameters.