• Title/Summary/Keyword: 석탄.바이오매스 주입비

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Numerical Study on 300 MW Shell-Type One-Stage Entrained Flow Bed Gasifier : Effect of Coal·Biomass Blending Ratio on CO2 Gasification (300MW급 Shell형 1단 분류층 가스화기 성능에 대한 전산수치해석 : 석탄·바이오매스 혼합비에 따른 CO2 가스화 반응)

  • Hong, Jung-Woo;Park, Sang-Shin;Song, Ji-Hoon;Hwang, Jung-Ho
    • Transactions of the Korean hydrogen and new energy society
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    • v.23 no.3
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    • pp.274-284
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    • 2012
  • Recently, gasification technology for coal blended with biomass has been an issue. Especially, An advantages of coal blended with biomass are 1) obtaining high cold gas efficiency, 2) obtaining syn-gas of high-high heating value (HHV), and 3) controlling occurrence of $CO_2$. In this study, the efficiency and characteristic of 300 MW Shell type gasifier were predicted using CFD simulation. The CFD simulation was performed for biomass coal blending ratios of 0~0.2, 0.5, 1 and $O_2$/fuel ratios of 0.5~0.84. Kinetic parameters (A, $E_a$) obtained by $CO_2$ gasification experiment were used as inputs for the simulation. In results of CFD simulation, residence times of particle in 300MW Shell type gasifer presented as 7.39 sec ~ 13.65 sec. Temperature of exit increased with $O_2$/fuel ratio as 1400 K ~ 2800 K, while there is not an effects of biomass coal blending ratios. Considering both aspects of temperature for causing wall slagging and high cold gas efficiency, the optimal $O_2$/fuel ratio and blending ratio were found to be 0.585 and 0.05, respectively.