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가압 유동층 반응기에서 SEWGS 공정을 위한 WGS 촉매의 반응특성

Reaction Characteristics of WGS Catalyst for SEWGS Process in a Pressurized Fluidized Bed Reactor

  • 투고 : 2012.07.31
  • 심사 : 2012.08.24
  • 발행 : 2012.08.31

초록

To check effects of operating variables on reaction characteristics of WGS catalyst for SEWGS process, water gas shift reaction tests were carried out in a pressurized fluidized bed reactor using commercial WGS catalyst and sand(as a substitute for $CO_2$ absorbent) as bed materials. Simulated syngas(mixed with $N_2$) was used as a reactant gas. Operating temperature was $210^{\circ}C$ and operating pressure was 20 bar. WGS catalyst content, steam/CO ratio, gas velocity, and syngas concentration were considered as experimental variables. CO conversion increased as the catalyst content and steam/CO ratio increased. CO conversion at fluidized bed condition was higher than that of fixed bed condition. However, CO conversion were maintained almost same value within the fluidized bed condition. CO conversion decreased as the syngas concentration increased. The optimum operation condition was confirmed and long time water gas shift reaction test up to 24 hours at the optimum operating conditions was carried out.

키워드

참고문헌

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피인용 문헌

  1. Capture vol.24, pp.5, 2013, https://doi.org/10.7316/KHNES.2013.24.5.428
  2. Attrition Characteristics of WGS Catalysts for SEWGS System vol.25, pp.2, 2014, https://doi.org/10.7316/KHNES.2014.25.2.122
  3. Effect of Pre-treatment Method on Reactivity of WGS Catalyst for SEWGS System vol.25, pp.4, 2014, https://doi.org/10.7316/KHNES.2014.25.4.355
  4. Comparison of Solid Circulation Characteristics with Change of Lower Loop Seal Geometry in a Circulating Fluidized Bed vol.52, pp.4, 2014, https://doi.org/10.9713/kcer.2014.52.4.522
  5. CO Conversion Characteristics of WGS Catalysts for SEWGS System vol.26, pp.2, 2015, https://doi.org/10.7316/KHNES.2015.26.2.096