A Study on the Performance Analysis in the Plate and Shell Heat Exchanger
Minwhan Seo, J.H. Park, Y.S. Kim
Abstract
Minwhan Seo, J.H. Park, Y.S. Kim
Abstract
Heat exchangers are called with important devices which have been widely used in industrial fields. Therefore, the design method for a heat exchanger is an important study in the aspect of energy saving. In this study, performance analyses for two types of plate and shell heat exchangers having a corrugated trapezoid shape of a chevron angle with , were executed and compared with experiments. For this study, the operation liquids were adopted with non-phase changing water. In the analysis, method was used for a plate and shell heat exchanger and a program was constructed. Independent variables for a plate and shell heat exchanger are flow rate and inlet temperature. Compared with experimental data, the accuracy of the developed are at the type A and type B in the heat transfer rate, respectively. In the pressure drop, the accuracy of the proposed program for a plate and shell heat exchanger is within and 5% error bounds for the type A and type B, respectively.
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Heat exchangers are called with important devices which have been widely used in industrial fields. Therefore, the design method for a heat exchanger is an important study in the aspect of energy saving. In this study, performance analyses for two types of plate and shell heat exchangers having a corrugated trapezoid shape of a chevron angle with , were executed and compared with experiments. For this study, the operation liquids were adopted with non-phase changing water. In the analysis, method was used for a plate and shell heat exchanger and a program was constructed. Independent variables for a plate and shell heat exchanger are flow rate and inlet temperature. Compared with experimental data, the accuracy of the developed are at the type A and type B in the heat transfer rate, respectively. In the pressure drop, the accuracy of the proposed program for a plate and shell heat exchanger is within and 5% error bounds for the type A and type B, respectively.
Key concepts: Plate heat exchanger, Shell and tube heat exchanger, Plate fin heat exchanger, Heat exchanger, Concentric tube heat exchanger, Pressure drop, NTU method, Shell (structure)