Performance analysis of a zeotropic mixture ( R290/CO2) for trans-critical power cycle

被引:25
作者
Pan, Lisheng [1 ]
Wei, Xiaolin [1 ]
Shi, Weixiu [2 ]
机构
[1] Chinese Acad Sci, Inst Mech, State Key Lab High Temp Gas Dynam, Beijing 100190, Peoples R China
[2] Beijing Univ Civil Engn & Architecture, Sch Environm & Energy Engn, Beijing 100044, Peoples R China
基金
中国国家自然科学基金;
关键词
CO2; R290; Zeotropic mixture; Low-grade heat energy; Trans-critical power cycle; WORKING FLUIDS; CO2; CAPTURE; RANKINE; SELECTION;
D O I
10.1016/j.cjche.2014.04.003
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Low critical temperature limits the application of CO2 trans-critical power cycle. The binary mixture of R290/CO2 has higher critical temperature. Using mixture fluid may solve the problem that subcritical CO2 is hardly condensed by conventional cooling water. In this article, theoretical analysis is executed to study the performance of the zeotropic mixture for trans-critical power cycle using low-grade liquid heat source with temperature of 200 degrees C. The results indicated that the problem that CO2 can't be condensed in power cycle by conventional cooling water can be solved by mixing R290 to CO2. Variation trend of outlet temperature of thermal oil in supercritical heater with heating pressure is determined by the composition of the mixture fluid. Gliding temperature causes the maximum outlet temperature of cooling water with the increase of mass fraction of R290. There are the maximum values for cycle thermal efficiency and net power output with the increase of supercritical heating pressure. (C) 2015 The Chemical Industry and Engineering Society of China, and Chemical Industry Press. All rights reserved.
引用
收藏
页码:572 / 577
页数:6
相关论文
共 21 条
[1]  
Calm J.M., 2007, HPAC Eng (Heat Pip Air Cond), P50
[2]   Energetic and exergetic analysis of CO2- and R32-based transcritical Rankine cycles for low-grade heat conversion [J].
Chen, Huijuan ;
Goswami, D. Yogi ;
Rahman, Muhammad M. ;
Stefanakos, Elias K. .
APPLIED ENERGY, 2011, 88 (08) :2802-2808
[3]   Potential of zeotropic mixtures as working fluids in organic Rankine cycles [J].
Chys, M. ;
van den Broek, M. ;
Vanslambrouck, B. ;
De Paepe, M. .
ENERGY, 2012, 44 (01) :623-632
[4]   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
[5]  
Guo T., 2010, SCI CHINA SER E, V53, P1869
[6]   Optimum design criteria for an Organic Rankine cycle using low-temperature geothermal heat sources [J].
Hettiarachchia, H. D. Madhawa ;
Golubovica, Mihajlo ;
Worek, William M. ;
Ikegami, Yasuyuki .
ENERGY, 2007, 32 (09) :1698-1706
[7]   Transcritical or supercritical CO2 cycles using both low- and high-temperature heat sources [J].
Kim, Y. M. ;
Kim, C. G. ;
Favrat, D. .
ENERGY, 2012, 43 (01) :402-415
[8]   Working fluids for low-temperature heat source [J].
Lakew, Amlaku Able ;
Bolland, Olav .
APPLIED THERMAL ENGINEERING, 2010, 30 (10) :1262-1268
[9]  
Lemmon E., 2018, NIST Standard Reference Database 23, DOI [DOI 10.18434/T4D303, 10.18434/T4/1502528, DOI 10.18434/T4/1502528, 10.18434/T4D303]
[10]   A thermodynamic criterion for selection of working fluid for subcritical and supercritical domestic micro CHP [J].
Mikielewicz, Dariusz ;
Mikielewicz, Jarostaw .
APPLIED THERMAL ENGINEERING, 2010, 30 (16) :2357-2362