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用于天然气发动机的废热回收有机朗肯循环系统中板式换热器的多目标优化

Multiobjective Optimization of a Plate Heat Exchanger in a Waste Heat Recovery Organic Rankine Cycle System for Natural Gas Engines.

作者信息

Valencia Guillermo, Núñez José, Duarte Jorge

机构信息

Programa de Ingeniería Mecánica, Grupo de Investigación en Gestión Eficiente de la Energía KAI, Universidad del Atlántico, Carrera 30 Número 8-49, Puerto Colombia, Área Metropolitana de Barranquilla 080007, Colombia.

Departamento de Energia, Grupo de Investigación en Optimización Energética GIOPEN, Universidad de la Costa CUC, Cl. 58 # 55-66, Barranquilla, Atlántico 080002, Colombia.

出版信息

Entropy (Basel). 2019 Jul 3;21(7):655. doi: 10.3390/e21070655.

Abstract

A multiobjective optimization of an organic Rankine cycle (ORC) evaporator, operating with toluene as the working fluid, is presented in this paper for waste heat recovery (WHR) from the exhaust gases of a 2 MW Jenbacher JMS 612 GS-N.L. gas internal combustion engine. Indirect evaporation between the exhaust gas and the organic fluid in the parallel plate heat exchanger (ITC2) implied irreversible heat transfer and high investment costs, which were considered as objective functions to be minimized. Energy and exergy balances were applied to the system components, in addition to the phenomenological equations in the ITC2, to calculate global energy indicators, such as the thermal efficiency of the configuration, the heat recovery efficiency, the overall energy conversion efficiency, the absolute increase of engine thermal efficiency, and the reduction of the break-specific fuel consumption of the system, of the system integrated with the gas engine. The results allowed calculation of the plate spacing, plate height, plate width, and chevron angle that minimized the investment cost and entropy generation of the equipment, reaching 22.04 m in the heat transfer area, 693.87 kW in the energy transfer by heat recovery from the exhaust gas, and 41.6% in the overall thermal efficiency of the ORC as a bottoming cycle for the engine. This type of result contributes to the inclusion of this technology in the industrial sector as a consequence of the improvement in thermal efficiency and economic viability.

摘要

本文针对以甲苯为工质运行的有机朗肯循环(ORC)蒸发器进行了多目标优化,用于从一台2兆瓦的 Jenbacher JMS 612 GS-N.L. 气体内燃机的废气中回收余热(WHR)。平行板式换热器(ITC2)中废气与有机流体之间的间接蒸发意味着不可逆传热和高投资成本,这些被视为要最小化的目标函数。除了ITC2中的现象学方程外,还将能量和㶲平衡应用于系统组件,以计算全局能量指标,如配置的热效率、热回收效率、整体能量转换效率、发动机热效率的绝对增加以及系统与燃气发动机集成时系统制动器特定燃料消耗的降低。结果允许计算使设备投资成本和熵产生最小化的板间距、板高度、板宽度和人字形角度,传热面积达到22.04平方米,从废气中回收热量进行能量传递达到693.87千瓦,作为发动机底部循环的ORC整体热效率达到41.6%。由于热效率和经济可行性的提高,这种类型的结果有助于将该技术纳入工业领域。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/778d/7515151/e558a3502db4/entropy-21-00655-g001.jpg

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