Thermoeconomic analysis of recuperative sub- and transcritical organic Rankine cycle systems

被引:13
|
作者
Oyewunmi, Oyeniyi A. [1 ]
Lecompte, Steven [2 ]
De Paepe, Michel [2 ]
Markides, Christos N. [1 ]
机构
[1] Imperial Coll London, Clean Energy Proc CEP Lab, Dept Chem Engn, London SW7 2AZ, England
[2] Univ Ghent, Dept Flow Heat & Combust Mech, Ghent, Belgium
基金
英国工程与自然科学研究理事会;
关键词
Waste Heat Recovery; Organic Rankine Cycle; Recuperator; Regenerator; Power Generation; Optimization; SAFT-VR MIE; FLUID SELECTION; HEAT-RECOVERY; MIXTURES; DESIGN; ORC;
D O I
10.1016/j.egypro.2017.09.187
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
There is significant interest in the deployment of organic Rankine cycle (ORC) technology for waste-heat recovery and power generation in industrial settings. This study considers ORC systems optimized for maximum power generation using a case study of an exhaust flue-gas stream at a temperature of 380 degrees C as the heat source, covering over 35 working fluids and also considering the option of featuring a recuperator. Systems based on transcritical cycles are found to deliver higher power outputs than subcritical ones, with optimal evaporation pressures that are 4-5 times the critical pressures of refrigerants and light hydrocarbons, and 1-2 times those of siloxanes and heavy hydrocarbons. For maximum power production, a recuperator is necessary for ORC systems with constraints imposed on their evaporation and condensation pressures. This includes, for example, limiting the minimum condensation pressure to atmospheric pressure to prevent sub-atmospheric operation of this component, as is the case when employing heavy hydrocarbon and siloxane working fluids. For scenarios where such operating constraints are relaxed, the optimal cycles do not feature a recuperator, with some systems showing more than three times the generated power than with this component, albeit at higher investment costs. (C) 2017 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:58 / 65
页数:8
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