Ullmann's Encyclopedia of Industrial Chemistry 2015
DOI: 10.1002/14356007.t12_t01
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Heat Exchangers, 2. Heat Transfer for Heat Exchanger Design

Abstract: The article contains sections titled: 1. Basic Heat‐Transfer and Pressure‐Drop Analysis 1.1. Basic Equations and Definitions of Heat‐Transfer Analysis 1.1.1. Fundamental Concepts … Show more

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Cited by 12 publications
(17 citation statements)
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“…This is due to temperature differences and film heat transfer coefficients between process streams. Furthermore, in the industry, there is a large versatility of heat exchangers that range in size from small (0.1 m 2 ) to supergiant (over 10 5 m 2 ) …”
Section: Resultsmentioning
confidence: 99%
“…This is due to temperature differences and film heat transfer coefficients between process streams. Furthermore, in the industry, there is a large versatility of heat exchangers that range in size from small (0.1 m 2 ) to supergiant (over 10 5 m 2 ) …”
Section: Resultsmentioning
confidence: 99%
“…The heat exchanger equations are written according to the P-NTU method, which is similar to the ϵ-NTU method, but it does not depend on the effectiveness factor. In this paper, the equations are described in relation to the hot stream.…”
Section: Heat Exchanger Network Modelmentioning
confidence: 99%
“…The total pressure drop for the tube side of a heat exchanger (ΔPf) consisting of three parts can be calculated by eq . where ΔPs ex, n , ΔPl ex, n , and ΔPn ex, n represent straight pipe resistance, local resistance, and nozzle resistance. The three resistances can be calculated by eqs – where ξ is the friction coefficient, which can be calculated by eq , proposed by Gu . The subscript ex means heat exchanger, L is the length of tubes, N is the number of tube passes, and ζ in eq is the local resistance coefficient; it has a value of 3–4 for multiple tube passes, while it equals 2 for a single tube pass.…”
Section: Model Formulationsmentioning
confidence: 99%