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Working Fluid Selection of Organic Rankine Cycle Using Low-grade Waste Heat with Variable Inlet and Constant Outlet Temperatures

机译:使用低级废热与可变入口和恒定出口温度的低级废热工作流体选择有机朗克循环

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This paper presents selection of working fluids for non-regenerative subcritical organic Rankine cycle(ORC)with alkanes,fluorinated alkanes,ethers,fluorinated ethers,aromatics,linear siloxanes and alcohols as working fluids using PR equation of state.The ORC system is driven by the waste heat source with temperature between 120 oC and 300 0C,whose specified outlet temperature is 80 0C.The first law efficiency,overall heat transfer capacity,turbine size factor and environment are used for comparison of different cases.The suitable working fluids for ORC system at different cases are shown:(a)case I(120 0C-80 0C): R161,R152a,RC270,RE170,CF31,RE134,R600a,isobutene,1-butene,R600,trans-2-butene,cis-2-butene,R245ca and R60la;(b)case 2(160 0C-80 0C): RC270,RE170,isobutene,l-butene,R600a,R600,R245fa,trans-2-butene,cis-2-butene;(c)case 3(200 0C-80 oC): cis-2-butene,trans-2-butene,R60la,R601,1-butene,isohexane,n-hexane and isobutene;(d)case 4(250 0C-80 0C): cyclopentane,n-hexane,acetone,cyclohexane;(e)case 5(300 0C-80 0C): acetone,cyclopentane,cyclohexane,benzene.
机译:本文提出了烷烃,氟化烷烃,醚,氟化醚,芳烃,线性硅氧烷和醇作为工作流体使用state.The ORC系统的PR方程的工作流体用于非再生亚临界有机朗肯循环(ORC)的选择由驱动用120摄氏度和300 0℃,指定其出口温度为80 0C.The第一定律效率,总传热容量,涡轮尺寸因子和环境被用于不同的例。合适的工作流体为ORC的比较之间的温度废热源系统在不同的情况下被示出:(A)情况下,I(120 0C-80℃):R161,R152a的,RC270,RE170,CF31,RE134,R600a的,异丁烯,1-丁烯,R600,反式-2-丁烯,顺式2-丁烯,R245ca和R60la;(b)情况下,2(160 0C-80℃):RC270,RE170,异丁烯,1-丁烯,R600a的,R600,的R245fa,反式-2-丁烯,顺式-2-丁烯;( c)中壳体3(200 0C-80℃):顺式-2-丁烯,反式-2-丁烯,R60la,R601,1丁烯,异己烷,正 - 己烷和异丁烯;(d)情况下,图4(250 0C-80 ℃):环戊烷,正己烷,丙酮,环己ANE;(e)中壳体5(300 0C-80℃):丙酮,环戊烷,环己烷,苯等。

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