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SI 수소생산 공정 Section 3 열교환기 설계

Design of Heat Exchanger for Section 3 of SI Hydrogen Production Process

  • 김기섭 (한국교통대학교 화공신소재고분자공학부) ;
  • 박병흥 (한국교통대학교 화공신소재고분자공학부)
  • 투고 : 2017.04.20
  • 심사 : 2017.05.19
  • 발행 : 2017.05.31

초록

SI process is one of the most advanced thermochemical water splitting cycles enabling mass production of hydrogen without emitting carbon dioxide when coupled to nuclear heat energy. The highest temperature (close to $1000^{\circ}C$) required in SI process is well matched with the outlet temperature of a coolant circulating a high-temperature gas-cooled reactor at around $950^{\circ}C$. In Section 3, some heat exchangers are included to recover heats from process flows at high temperature. In this work, we designed a heat exchanger based on the $1Nm^3/hr$ $H_2$ production capacity using commercial tools for chemical process design.

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참고문헌

  1. J. L. Russel, Jr., K. H. McCorkle, J. H. Norman, J. T. Porter II, T. S. Roemer, J. R. Schuster, and R. S. Sharp, Proc. 1st World Hydrogen Energy Conf., Miami Beach, March (1976)
  2. W. L. McCabe, J. C. Smith, and P. Harriott, Unit Operation of Chemical Engineering, 7th Ed., McGraw-Hill (2005).