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F-T合成铁催化剂羰基硫中毒行为的研究 被引量:3

Study of poisoning behavior of Fe-Cu-K catalyst by COS in Fischer-Topsch synthesis
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摘要 在获得F-T合成本征动力学模型的基础上,对F-T合成Fe-Cu-K业催化剂COS中毒本征失活动力学进行了研究。所考察条件为:合成气中COS浓度分别为51、129和245ppm,空速为1800~2000hˉ1,温度为504~556K,压力为2.3lMPa,催化剂粒度为0.154~0.180mm。中毒过程催化活性模型值与实验值符合较好,且催化剂在合成气中低硫浓度时其失活速率快。并用XRD和TEM考察了催化剂表面硫的形貌。 ased on the intrinsic kinetics model for F-T synthesis,kinetics for the deactivation of Fe-Cu-K commercial catalyst in Fischer-Topsch synthesis was studied.The investigation was carried out tinder the following conditions: COS concentrations in syngds, 51,129,and 245 ppm respectively; space velocity, 1800-2000 h-1; temperature, 504-556K; pressure, 2.31 MPa; particle size of catalyst, 0.154-0.180mm. The catalytic activity model data in the posisoning course were in better keeping with the experimental data. The deactivation rate of te catalyst was more rapid at lower concentrations of sulphur in syngas. The appearances and shapes of sulphur on the catalyst surface were determined by XRD and TEM methods.
出处 《天然气化工—C1化学与化工》 CAS CSCD 北大核心 1994年第5期15-20,共6页 Natural Gas Chemical Industry
关键词 F-T合成 铁催化剂 中毒 F-T synthesis, poisoning of COS, intrinsic kinetics
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参考文献1

  • 1张碧江主编..煤基合成液体燃料[M].太原:山西科学技术出版社,1993:583.

同被引文献44

  • 1李新学,刘迎新,魏雄辉.羰基硫脱除技术[J].现代化工,2004,24(8):19-22. 被引量:36
  • 2张青林.-[J].催化学报,1988,9(2):131-131. 被引量:4
  • 3张青林 郭汉贤.羰基硫水解催化剂的中毒特征及其机理.催化学报,1998,9(2):131-136. 被引量:1
  • 4郭汉贤.羰基硫脱除及水解技术应用展望.化肥工业,1988,15(1):52-61. 被引量:1
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  • 7Fiedorow R, Leaute R, Dalla Lana I G. A study of kinetics and mechanism of COS hydrolysis over Alumina[J]. J Catal,1984,85:339. 被引量:1
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