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epsilon-NTU relationships in parallel-series arrangements: Application to plate and tubular heat exchangers

机译:并联系统中的ε-NTU关系:在板式和管式热交换器中的应用

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The epsilon-NTU method has advantages over other methods because it does not require assumption of an outlet temperature to determine the duty of a heat exchanger. In this work, the epsilon-NTU method was used to obtain a general algebraic expression of the effectiveness of PHEs in the N-Pa pass-1 pass configuration as a function of the heat capacity ratio (C*) and the number of transfer units (NTU). This expression is valid for PHEs with a high number of plates (N-p > 40). In addition, 1 pass-1 pass and 2 pass-1 pass PHEs were numerically analyzed to obtain an algebraic expression of the effectiveness of PHEs with a low number of thermal plates (N-P < 40) as a function of C*, NTU and the number of plates. Finally, the expression obtained for N-pa pass-1 pass PHEs with a high number of plates was generalized for use in any heat exchanger with series-parallel configurations, such as series-parallel arrangements of double-pipe or shell-and-tube heat exchangers. (C) 2016 Elsevier Ltd. All rights reserved.
机译:ε-NTU方法具有优于其他方法的优点,因为它不需要假设出口温度即可确定热交换器的负荷。在这项工作中,使用ε-NTU方法获得了N-Pa通过1次通过配置中PHE的有效性与热容量比(C *)和传递单位数量的函数的一般代数表达式。 (NTU)。该表达式对于具有大量塔板(N-p> 40)的PHE有效。此外,对1次通过1次和2次通过1次的PHE进行了数值分析,以代数式表达了具有少量热板(NP <40)的PHE作为C *,NTU和温度的函数的有效性。板数。最后,针对具有大量塔板的N-pa pass-1次PHE获得的表达式可推广用于任何具有串并联配置的换热器,例如双管或壳管式串并联布置热交换器。 (C)2016 Elsevier Ltd.保留所有权利。

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