• Title/Summary/Keyword: 간접 냉동법 담수화

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Performance Analysis of Freezing Desalination System using Seawater Heat Pump (해수 히트펌프를 이용한 냉동법 담수화시스템 개념설계)

  • Lee, Ho-Saeng;Lee, Seung-Won;Yoon, Jung-In;Kim, Hyeon-Ju
    • Journal of Advanced Marine Engineering and Technology
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    • v.35 no.4
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    • pp.373-378
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    • 2011
  • The freeze desalination cycle with seawater heat pump system is simulated and designed for the basic data for the design of freeze desalination system. The basic model of seawater heat pump system is refrigeration cycle and indirect freeze desalination method is used for seawater desalination. The cycle performance of seawater heat pump such as COP, compressor work, condensing capacity was analyzed and the desalination performance such as fresh water productivity and energy per unit fresh water productivity was compared with respect to the seawater temperature of condenser inlet and ice ratio in the evaporator. The compressor work and condensing capacity decreased with respect to the decrease of seawater inlet temperature. The energy per unit fresh water productivity in case of $8^{\circ}C$ seawater inlet temperature showed 28.9% lower than that of $20^{\circ}C$.

Analysis of Heating and Desalination Cycle Using Low Temperature Seawater (저온 해수를 이용한 난방 및 담수화사이클 성능 해석)

  • Lee, H.S.;Lee, S.W.;Jung, D.H.;Moon, D.S.;Kim, H.J.
    • Journal of the Korean Society for Marine Environment & Energy
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    • v.14 no.4
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    • pp.301-306
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    • 2011
  • The paper presents an analysis of the heating cycle and discusses a desalination cycle that uses lowtemperature seawater. The basic heating cycle model is the heat pump cycle, and seawater desalination is usually performed by the indirect freezing desalination method. The low temperature of the seawater (below $5^{\circ}C$) acts as the heat source of the evaporator. R-134a, R-1234yf, R-600a are used as working fluids. In the 2-stage compression cycle, the compressor's work decreased by about 15.6% from that in the 1-stage compression cycle. Further, the COP in the 2-stage cycle was 17.6% higher than that in the 1-stage cycle. In the indirect desalination cycle, the energy per unit fresh water productivity in the 2-stage cycle was 19.8% lower than that in the 1-stage cycle.