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首页> 外文期刊>Applied thermal engineering: Design, processes, equipment, economics >Modelling and simulation analysis of an ORC-FPC waste heat recovery system for the stationary CNG-fuelled compressor
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Modelling and simulation analysis of an ORC-FPC waste heat recovery system for the stationary CNG-fuelled compressor

机译:固定式CNG燃料压缩机ORC-FPC余热回收系统的建模与仿真分析

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In this paper, an organic Rankine cycle-free piston compressor (ORC-FPC) system was employed to recover waste heat of exhaust gas produced by a stationary compressed natural gas (CNG) fuelled internal combustion compressor. FPC was used as the expander in ORC to assist in compressing natural gas, of which the working principle was investigated in detail. To verify the feasibility of the system, an ORC-FPC model was built up with GT-suite software and parameters of the key parts were selected based on the analytical data. Effects of ratio of the power piston area to the compression piston area (S-p/S-c) and output pressure of natural gas on the system were studied through GT-suite simulations. Results indicated that the feasibility of the system could be validated based on the present model. When S-p/S-c varied from 2.5 to 5.0, the effective efficiency of FPC (eta(e,t)) in five cycles decreased gradually, while the indicated efficiency of FPC (eta(i,t)) in five cycles firstly decreased and then increased. When S-p/S-c was 2.5, the model achieved the best performance (eta(i,t) of 50.7% and eta(e,t) of 23.7%). eta(i,t) and eta(e,t) decreased with the increase of output pressure of CNGwithin the range of 11-14 bar, and the best performance of the system was obtained at 11 bar (eta(i,t) of 53.2% and eta(e,t) of 26.5%). (C) 2015 Elsevier Ltd. All rights reserved.
机译:本文采用有机朗肯无循环活塞式压缩机(ORC-FPC)系统回收由固定压缩天然气(CNG)燃料的内燃压缩机产生的废气废热。 FPC被用作ORC中的膨胀剂以辅助压缩天然气,详细研究了其工作原理。为了验证该系统的可行性,使用GT-suite软件建立了ORC-FPC模型,并根据分析数据选择了关键部件的参数。通过GT套件仿真研究了动力活塞面积与压缩活塞面积之比(S-p / S-c)和天然气输出压力对系统的影响。结果表明,基于该模型可以验证该系统的可行性。当Sp / Sc从2.5变为5.0时,五个周期内FPC的有效效率(eta(e,t))逐渐降低,而五个周期内FPC的指示效率(eta(i,t))则先下降,然后下降。增加。当S-p / S-c为2.5时,模型获得最佳性能(eta(i,t)为50.7%,eta(e,t)为23.7%)。在11-14 bar范围内,随着CNG输出压力的增加,eta(i,t)和eta(e,t)减小,并且在11 bar(eta(i,t) 53.2%和eta(e,t)为26.5%)。 (C)2015 Elsevier Ltd.保留所有权利。

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