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improvement in the process of regenerating lizzatori minds, conversion of hydrocarbons

机译:改善lizzatori思想的过程,碳氢化合物的转化

摘要

1439532 Catalyst regeneration U O P INC 29 May 1973 [30 May 1972 (2) 18 Dec 1972] 25366/73 Heading B1F In a process for regenerating spent catalyst containing coke in a dense phase fluidised bed with fresh regeneration gas containing free oxygen in a regeneration zone from which spent regeneration gas is removed, controlled afterburning of the carbon monoxide to carbon dioxide is substantially completed in the bed, the afterburning being initiated by setting up afterburning conditions in the dense bed and being controlled by monitoring a parometer selected from a temperature in the regeneration zone, an average temperature in the regeneration zone, a temperature differential in the regeneration zone and the quantity of free oxygen in the spent regeneration gas, and the inflow of the fresh regeneration gas is regulated to maintain the monitored parometer substantially constant. The dense bed temperature may be maintained within the range of 650-800‹C, the inflow of fresh regeneration gas may be regulated to maintain the free oxygen content of the spent regeneration gas constant within the range between 0.1 and 20 mole %, and the temperature difference between the dense bed and the dilute phase above the bed may be maintained at a temperature difference less than 30‹C.
机译:1439532催化剂再生UOP INC 1973年5月29日[1972年5月30日(2)1972年12月18日] 25366/73标题B1F在再生区中用含有游离氧的新鲜再生气体在密相流化床中再生含有焦炭的废催化剂的方法从中除去废的再生气,基本上在床中完成一氧化碳至二氧化碳的受控后燃烧,通过在致密床中设置后燃烧条件来启动后燃烧,并通过监测选自温度传感器的温度来控制该后燃烧。调节再生区,再生区中的平均温度,再生区中的温度差和用过的再生气体中的游离氧气的量,以及新鲜再生气体的流入量,以保持所监测的比重计基本恒定。致密床温度可以保持在650-800℃的范围内,新鲜再生气体的流入可以被调节以将废再生气体的游离氧含量保持恒定在0.1至20摩尔%之间,并且致密床和床上方稀相之间的温差可保持在小于30℃的温度差。

著录项

  • 公开/公告号IT985236B

    专利类型

  • 公开/公告日1974-11-30

    原文格式PDF

  • 申请/专利权人 UNIVERSAL OIL PROD CO;

    申请/专利号IT19730050298

  • 发明设计人

    申请日1973-05-29

  • 分类号B01J;

  • 国家 IT

  • 入库时间 2022-08-23 04:28:51

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