パイロリティックガス化炉の開発

  • 村上 高広
    石川島播磨重工業株式会社基盤技術研究所
  • 許 光文
    石川島播磨重工業株式会社基盤技術研究所
  • 須田 俊之
    石川島播磨重工業株式会社基盤技術研究所
  • 松澤 克明
    石川島播磨重工業株式会社基盤技術研究所
  • 谷 秀久
    石川島播磨重工業株式会社電力事業部

書誌事項

タイトル別名
  • Development of Pyrolytic Gasifier
  • パイロリティックガスカロ ノ カイハツ

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抄録

The purpose of this study is to investigate experimentally the characteristics of a pyrolytic gasifier. Two facilities were used. One is a 1⁄5 scale plastic model of the 6t⁄d pilot plant. With this model the relative solid circulation rate was measured. The second facility was used the lab-scale bubbling fluidized bed gasifier coupled with a pneumatically transported char bed combustor. Here, the gasification characteristics were investigated for a two-stage bubbling fluidized bed gasifier.The results revealed that a relative solid circulation rate above 20 could be achieved by control of fluidized bed height and pressure in the gasifier, therefore allowing self-sustaining operation. The combustor inlet showed severe wear; hence, for this part abrasion-resistant material must be used. Concerning gasification characteristics, the two-stage bubbling fluidized bed gasifier showed a remarkable increase in gasification efficiency and tar suppression. When gasifying Ca-impregnated fuel, however, no remarkable change in tar contents was observed. This result is interpreted such that tar can easily be reformed/destructed by a Ca-catalyst. A cold gas efficiency about 83.5 %, which is feasible for self-sustained operation, was still achieved at somewhat lower temperatures in the gasifier for Ca-impregnated fuel. Consequently, the operation of the pyrolytic gasifier is easy. However, for the lower temperature tar increased. Therefore, gas reforming at a subsequent stage of the gasifier is important.

収録刊行物

  • 高温学会誌

    高温学会誌 33 (1), 21-26, 2007

    一般社団法人 スマートプロセス学会 (旧高温学会)

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