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Estimating Number of Shells in Shell and Tube Heat Exchangers: A New Approach Based on Temperature Cross

机译:估算管壳式换热器中的壳数:基于温度跨度的新方法

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Multipass heat exchangers are often designed by using the rule of thumb F_T≥0.75, which is rather arbitrary. F_T falls sharply with the increase in temperature cross. Hence, only a limited temperature cross can be allowed. The ability to accommodate temperature cross increases rapidly as the number of shell passes is increased. Throuhg many investigators have emphasized the importance of temperature cross in exchanger design, it has as yet not been explicitly accounted for in the design. This paper introduces a new approach for estimating the number shells in a shell and tube exchanger which directly accounts for temperature cross, rather than routing this effect through F_T or O_p (Ahmad et al.'s parameter, which is again a correction factor not directly related to temperature cross). The approach is compatible with the established design procedures and bypasses the F_T. It generates better designs by defining maximum permissible temperature cross, than the Traditional designs based on specifying minimum permissible F_T. Expressions have also Been provided with correlate the present formulation with that of Ahmad et al.
机译:通常通过经验法则F_T≥0.75来设计多通道热交换器,这是相当随意的。 F_T随着温度跨度的增加而急剧下降。因此,仅允许有限的温度交叉。随着壳通过次数的增加,适应温度交叉的能力迅速提高。通过许多研究人员已经强调了温度交叉在交换器设计中的重要性,但尚未在设计中对其进行明确说明。本文介绍了一种估算壳管交换器中的壳数的新方法,该方法直接考虑了温度交叉,而不是通过F_T或O_p来传递这种影响(Ahmad等人的参数,这也是一个校正因子,而不是直接与温度交叉相关)。该方法与已建立的设计程序兼容,并且绕过了F_T。与基于指定最小允许F_T的传统设计相比,它通过定义最大允许温度跨度来生成更好的设计。还提供了与本发明的制剂与Ahmad等人的相关的表达。

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