Effect of off-design heat source temperature on heat transfer characteristics and system performance of a 250-kW organic Rankine cycle system

被引:52
作者
Fu, Ben-Ran [1 ]
Hsu, Sung-Wei [1 ]
Lee, Yuh-Ren [1 ]
Hsieh, Jui-Ching [1 ]
Chang, Chia-Ming [1 ]
Liu, Chih-His [1 ]
机构
[1] Ind Technol Res Inst, Green Energy & Environm Res Labs, Hsinchu, Taiwan
关键词
Organic Rankine cycle; Off-design condition; Heat transfer characteristic; LOW-GRADE HEAT; WASTE HEAT; POWER-GENERATION; FLUID SELECTION; WORKING FLUIDS; ORC; OPTIMIZATION; MODEL;
D O I
10.1016/j.applthermaleng.2014.04.065
中图分类号
O414.1 [热力学];
学科分类号
摘要
This work investigated the effect of off-design heat source temperature on the heat transfer characteristics and system performance of a 250-kW organic Rankine cycle system. R245fa was used as a working fluid. The net power output was 243 kW and the system thermal efficiency was 9.5% under design conditions. For an off-design heat source temperature (T-W,T-in), the operating pressure was controlled to meet that R245fa reached the saturation liquid and vapor states at the outlet of the preheater and evaporator, respectively. The results demonstrated that the increase rate in evaporation temperature was almost the same as that in T-W,T-in; higher T-W,T-in yields better heat transfer performance of the preheater and required a smaller evaporator heat capacity; and the net power output and system thermal efficiency increased linearly with increasing T-W,T-in. The net power output increased by 41.9%, whereas the total heat transfer rate increased by only 7.0% for the studied range of T-W,T-in. In conclusion, an off-design operation was studied by the pressure control approach within a heat source temperature variation of -10.3 degrees C to +19.8 degrees C from design, resulting in variations of -13.6% to +22.6% and -11.5% to +17.4% in the net power output and system thermal efficiency, respectively. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:7 / 12
页数:6
相关论文
共 25 条
[1]   Comparative performance analysis of low-temperature Organic Rankine Cycle (ORC) using pure and zeotropic working fluids [J].
Aghahosseini, S. ;
Dincer, I. .
APPLIED THERMAL ENGINEERING, 2013, 54 (01) :35-42
[2]   Quasi-dynamic model for an organic Rankine cycle [J].
Bamgbopa, Musbaudeen O. ;
Uzgoren, Eray .
ENERGY CONVERSION AND MANAGEMENT, 2013, 72 :117-124
[3]   A review of working fluid and expander selections for organic Rankine cycle [J].
Bao, Junjiang ;
Zhao, Li .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2013, 24 :325-342
[4]  
Bejan A., 1993, HEAT TRANSFER
[5]  
Bell K.J., 1963, BULLETIN, V5
[6]   Evaluation of carbon dioxide blends with isopentane and propane as working fluids for organic Rankine cycles [J].
Garg, Pardeep ;
Kumar, Pramod ;
Srinivasan, Kandadai ;
Dutta, Pradip .
APPLIED THERMAL ENGINEERING, 2013, 52 (02) :439-448
[7]  
GNIELINSKI V, 1976, INT CHEM ENG, V16, P359
[8]   Optimization of low temperature solar thermal electric generation with Organic Rankine Cycle in different areas [J].
Jing, Li ;
Gang, Pei ;
Jie, Ji .
APPLIED ENERGY, 2010, 87 (11) :3355-3365
[9]  
Leading Electric & Machinery Co, 2013, US MAN
[10]   Dynamic Response of a 50 kW Organic Rankine Cycle System in Association with Evaporators [J].
Lee, Yuh-Ren ;
Kuo, Chi-Ron ;
Liu, Chih-Hsi ;
Fu, Ben-Ran ;
Hsieh, Jui-Ching ;
Wang, Chi-Chuan .
ENERGIES, 2014, 7 (04) :2436-2448