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A Calculation Method for the Optimized Thermal-Fluid Dynamic Sizing of Heat Exchangers

机译:换热器热流动态优化尺寸的计算方法

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摘要

A thermal-fluid dynamic calculation model has been developed for sizing some compact heat exchangers. In particular, the exhaust heat recovery systems are considered, as the internal regeneration considerably improves the turbogas power cycles efficiency. The calculation model is designed for selecting the best heat transfer surfaces and optimizing some objective-functions. For almost 60 plate-fin heat transfer surfaces, analytical correlations are derived in a database-like form, to calculate the Colburn j factor and Fanning f factor as functions of Reynolds number. A model is developed also for innovative PCHEs, using a simplified approach. The sizing procedure, based on the core mass velocity equation, is implemented on an electronic worksheet. If the minimum heat exchanger effectiveness and the maximum pressure drops are input, the model gives the heat exchanger core sizing for the possible combinations of the heat transfer surfaces. For each combination, the calculation method minimizes (or maximizes) the selected objective-function by means of an optimization procedure, performed by a solver through the Newton or the conjugate gradients algorithm. The thermal-fluid dynamic calculation method is applied to a high-temperature recuperator with a high-streams pressure ratio. The results show the difficulty of arranging streams with highly different volumetric flows (i.e., same massive flow rates but very different pressures) on the two sides of the heat exchanger, so that very unbalanced aspect ratios arise for the cores, due to the limits imposed to the maximum allowable pressure drops.
机译:已经开发出一种热流体动态计算模型来确定一些紧凑型热交换器的尺寸。特别是考虑了废热回收系统,因为内部再生可显着提高涡轮动力循环的效率。该计算模型旨在选择最佳的传热表面并优化一些目标函数。对于近60个板翅式传热表面,以数据库形式导出分析相关性,以计算作为雷诺数函数的Colburn j因子和Fanning f因子。还使用简化方法为创新的PCHE开发了一个模型。基于核心质量速度方程的上浆程序在电子工作表上执行。如果输入了最小换热器效率和最大压降,则模型会为换热面的可能组合提供换热器芯的尺寸。对于每种组合,计算方法都通过优化程序将所选目标函数最小化(或最大化),该优化过程由求解器通过牛顿或共轭梯度算法执行。该热流体动态计算方法应用于具有高流压比的高温换热器。结果表明,很难在热交换器的两侧布置体积流量非常不同(即相同的大流量但压力非常不同)的流,因此,由于施加的限制,芯的长径比非常不平衡到最大允许压降。

著录项

  • 来源
    《Heat Transfer Engineering》 |2008年第6期|556-564|共9页
  • 作者

    MAURIZIO PIEVE;

  • 作者单位
  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

  • 入库时间 2022-08-18 00:19:45

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