期刊文献+

工质对低温蒸汽闪蒸–双工质联合循环性能的影响 被引量:5

Thermodynamic Performance Analysis for Flashing-binary Cycle Using Different Working Fluids to Low Temperature Steam
下载PDF
导出
摘要 为获得不同工质对新型双工质-闪蒸-双工质联合循环系统热力性能的影响规律及确定系统最佳工质,以流量27.8 kg/s,383.15 K的饱和蒸汽为热源,针对5种低沸点有机工质,以热力学第一、二定律为基础,编制计算程序,将不同工质对该联合循环系统热力性能的影响进行了对比分析。研究结果表明:在具有潜热的高压级双工质阶段,采用不同工质系统净输出功和热效率随蒸发压力增加均呈现出逐渐增加,增幅减小的趋势,热力性能表现为R600>R236fa>R114>R245fa>R123;对于不同温度热水热源,净输出功则表现出随蒸发压力的提高先增加后减小的特点,在汽轮机背压一定时,工质的沸点越低,其热力性能越好,热力性能表现为R236fa>R600>R114>R245fa>R123;在高压级、低压级双工质阶段分别采用R600,R236fa作为工质时,该联合循环系统取得最大净输出功6 466.1 kW、最大热效率9.46%和最小火用损失9 511.5 kW。 In order to obtain the thermodynamic performance of different organic working fluids on binaryflash-binary system and determine the best fluids, the saturated steam at 27.8 kg/s and 383.15 K was regarded as heat source. Based on the first and the second law of thermodynamic, the calculation program was written. The results show that in the high level binary stage which has latent heat, the net output work increases gradually with the evaporation pressure. And so does the thermal efficiency. But it increases more and more slowly, while the thermal performance shows R600〉R236fa〉 R114〉R245fa〉R123. As for the hot water heat source, the net output power increases at first and then decreases. When the back pressure is certain, the boiling point is lower, the thermodynamic performance is better. And the performance reveals to R236fa〉R600〉R114〉R245fa〉R123. The combined cycle system can reach the largest net output work of 6 466.1 kW, the maximum thermal efficiency of 9.46% and the minimum energy loss of 9 511.5 kW when R600, R236 fa are used respectively in high level and low level binary phase.
出处 《中国电机工程学报》 EI CSCD 北大核心 2014年第20期3257-3265,共9页 Proceedings of the CSEE
基金 国家自然科学基金项目(51104083 51374123)~~
关键词 联合循环系统 有机工质 低温余热蒸汽 热力性能 标态沸点 combined cycle system organic working fluid low temperature waste heat steam thermodynamic performance standard boiling point
  • 相关文献

参考文献24

  • 1Athanasios I.P,Mirko S,Patrick L.On the systematic design and selection of optimal working fluids for organic rankine cycles[J].Applied Thermal Engineering,2010,30(7):760-769.
  • 2周颖艳,杜小泽,杨立军,杨勇平.吸收烟气余热的非共沸混合工质蒸发换热特性[J].中国电机工程学报,2013,33(8):9-15. 被引量:22
  • 3Aleksandra B G,Wladyslaw N.Maximising the working fluid flow as a way of increasing power output of geothermal power plant[J].Applied Thermal Engineering,2007,27(11-12):2074-2078.
  • 4刘超,徐进良,陈奇成,苗政.低温跨临界有机朗肯循环工质筛选[J].中国电机工程学报,2013,33(23):37-43. 被引量:21
  • 5Hettiarachchi H D,Golubovic M,Worek W,et al.Optimum design criteria for an organic Rankine cycle using low-temperature geothermal heat sources[J].Journal of Energy Resources Technology 2007,129(3):24-37.
  • 6Badr O,Callaghan P W,Probert S D.Thermodynamic and thermophysical properties of organic working fluids for Rankine cycle engines[J].Applied Energy,1985,19(l):1-40.
  • 7Badr O,Probert S D.Selecting a working fluid for rankine cycle engine[J].Applied Energy,1985,21(1):1-42.
  • 8Saleh B,Koglbauer G,Wendland M,et al.Working fluids for low temperature organic Rankine cycles[J].Energy,2007,32(7):1210-1221.
  • 9Hung T C.Waste heat recovery of organic Rankine cycle using dry fluids[J].Energy Conversion and Management,2001,42(5):539-553.
  • 10Steven B J.Predicting performance of refrigerants using the peng robinson equation of state[J].International Journal of Refrigeration,2007,30(8):1319-1328.

二级参考文献133

共引文献239

同被引文献60

  • 1王智,于一达,韩中合,杜燕.低温再热式有机朗肯循环的参数优化[J].热力发电,2013,42(5):22-29. 被引量:10
  • 2肖立川,陈宏,黄冬良,陈辉.应用多工质朗肯循环提高火电厂效率[J].动力工程,2006,26(2):273-277. 被引量:5
  • 3严家騄.低温热能发电方案中选择工质和确定参数的热力学原则和计算式.工程热物理学报,1982,3(1):1-7.
  • 4Hettiarachchi H D,Golubovic M,Worek W,et al.Optimum design criteria for an organic Rankine cycle using low-temperature geothermal heat sources[J].Journal of Energy Resources Technology,2007,129(3):24-37.
  • 5Wei D H,Lu X S,Lu Z,et al.Performance analysis and optimization of organic Rankine cycle(ORC) for waste heat recovery[J].Energy Conversion and Management,2007,48(4):1113-1119.
  • 6Dai Y P,Wang J F,Gao L.Parametric optimization and comparative study of organic Rankine cycle (ORC) for low grade waste heat recovery[J].Energy Conversion and Management,2009,50(4):576-582.
  • 7Mago P J,Chamra L M,Srinivasan.An examination of regenerative organic Rankine cycles using drying fluids [J].Applied Thermal Engineering,2008,28(8-9):998-1007.
  • 8Desai N B,Bandyopadhyay S.Process integration of organic Rankine cycle[J].Energy,2009,34(10):1674 - 1686.
  • 9Liu B T,Chien K H,Wang C C.Effect of working fluids on organic Rankine cycle for waste heat recovery [J].Energy,2004,29(8):1207 -1217.
  • 10Saleh B,Koglbauer G,Wendland M,et al.Working fluids for low temperature organic Rankine cycles[J].Energy,2007,32(7):1210-1221.

引证文献5

二级引证文献22

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部