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Optimization of Reaction Conditions for the High Purity Hydrogen Production Process Using By-Product Gases in Steel Works

철강산업 부생가스를 이용한 고순도 수소 제조 공정의 반응 조건 최적화

  • CHOI, HANSEUL (Clean Coal Research Group, Research Institute of industrial Science and Technology) ;
  • KIM, JOONWOO (Clean Coal Research Group, Research Institute of industrial Science and Technology) ;
  • KIM, WOOHYOUNG (Clean Coal Research Group, Research Institute of industrial Science and Technology) ;
  • KIM, SUNGJOONG (Clean Coal Research Group, Research Institute of industrial Science and Technology) ;
  • KOH, DONGJUN (Clean Coal Research Group, Research Institute of industrial Science and Technology)
  • Received : 2016.11.01
  • Accepted : 2016.12.30
  • Published : 2016.12.30

Abstract

Low-priced hydrogen is required in petrochemical industry for producing low-sulfur oil, and upgrading low-grade crude oil since environmental regulations have been reinforced. Steel industry can produce hydrogen from by-product gases such as Blast Furnace Gas (BFG), Coke Oven Gas (COG), and Linze Donawitz Gas (LDG) with water gas shift (WGS) reaction by catalysis. In this study, we optimized conditions for WGS reaction with commercial catalysts by BFG and LDG. In particular, the influence on activity of gas-hourly-space-velocity, and $H_2O/CO$ ratios at different temperatures were investigated. As a result, 99.9%, and 97% CO conversion were showed with BFG, and LDG respectively under $350^{\circ}C$ High Temperature Shift (HTS), $200^{\circ}C$ Low Temperature Shift (LTS), 3.0 of $H_2O/CO$, and $1500h^{-1}$ of GHSV. Furthermore, 99.9% CO conversion lasted for 250 hours with BFG as feed gas.

Keywords

References

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