• Title/Summary/Keyword: 칼리나사이클

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Basic performance analysis of ocean thermal energy conversion using the refrigerant mixture R32/R152a (R32/R152a 혼합냉매를 적용한 해양온도차발전의 기초성능해석)

  • Cha, Sang Won;Lee, Ho Saeng;Moon, Deok Soo;Kim, Hyeon Ju
    • Journal of Advanced Marine Engineering and Technology
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    • v.38 no.4
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    • pp.502-507
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    • 2014
  • In this paper, performance characteristics of cycles were studied when mixed working fluid was used for ocean thermal energy conversion (OTEC). Among the various mixed refrigerants for industrial heat-pump, R32/R152a used in ocean thermal energy conversion system. For simulations, R32/R152a were used in existing closed cycle and Kalina cycle which is used only ammonia and water as mixed refrigerant. Temperature of the warm heat source was 26 and 29 celsius degree, temperature of the cold heat source was 5 celsius degree. In results of simulation, Gross power of the closed cycle on R32 was 22kW, and efficiency of the cycle was 2.02%. When the mixed refrigerant of R32/R152a, in the ratio of 90 to 10, gross power of the closed cycle was 29.93kW, and efficiency of the cycle was 2.78%. Gross power and cycle efficiency of R32/R152a increased by 36% and 37% than those of existing single refrigerant. Additionally, the same simulations were conducted in Kalina cycle with the same various composition ratio of mixed refrigerant.

Simulation of a geothermal power generation system using the Kalina cycle (칼리나 사이클을 이용한 지열발전 시스템의 시뮬레이션)

  • Chang, Ki-Chang;Baik, Young-Jin;Kim, Min-Sung;Lee, Young-Soo;Park, Seong-Ryong;Ra, Ho-Sang
    • 한국신재생에너지학회:학술대회논문집
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    • 2008.05a
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    • pp.626-629
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    • 2008
  • In this study, a geothermal power generation system using the Kalina cycle was investigated by the simulation method. The Kalina cycle system can be used for the utilization of a low-temperature heat sources such as geothermal and industrial waste heat that are not hot enough to produce steam. The sea/river water can be considered as a cooling media. A steady-state simulation model was developed to analyze and optimize its performance. The model contains a turbine, a pump, an expansion valve and heat exchangers. The turbine and pump were modelled by an isentropic efficiency, while a condenser, an evaporator and a regenerative heat exchanger were modeled by UA-LMTD method with a counter-flow assumption. The effect of the ammonia fraction at the separator inlet on the cycle performance is investigated in detail.

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