Design of multiple shell and tube heat exchangers in series: E shell and F shell |
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| Authors: | U. Vengateson |
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| Affiliation: | 1. State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing, 102249, China;2. School of Chemical Engineering, Xi''an Jiaotong University, Xi''an, 710049, China;1. Chemical Engineering Department, Av. Colombo 5790, State University of Maringá, 87020900 Maringá, PR, Brazil;2. Chemical Engineering Department, Carretera de San Vicente del Raspeig S/N, University of Alicante, 03690 San Vicente del Raspeig, Alicante, Spain |
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| Abstract: | Multiple shell and tube heat exchangers in the series are employed to handle the temperature cross in the chemical process industries. Depending on the degree of temperature cross, certain number of heat exchangers (either E or F shell type) need to be connected in series such that the temperature cross in each exchanger is within allowable limit. Determination of the number of exchangers for the given terminal temperatures is essential during heat exchanger design phase. In this paper, using finite difference calculus, modeling has been done to calculate the number of shells required for both E and F shell cases. In addition, equations are developed to determine hot and cold fluid temperature profiles across all heat exchangers. Design procedure is illustrated with the help of a case study and the capital cost of both cases is compared. Issues related to E shell and F shells are also discussed. |
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