首页> 外国专利> GASIFICATION PROCESS COMBINED WITH STEAM METHANE REFORMING TO PRODUCE SYNGAS SUITABLE FOR METHANOL PRODUCTION

GASIFICATION PROCESS COMBINED WITH STEAM METHANE REFORMING TO PRODUCE SYNGAS SUITABLE FOR METHANOL PRODUCTION

机译:气化工艺与蒸汽甲烷重整相结合以生产适用于甲醇生产的合成气

摘要

An improved method for the production of stoichiometric ratioed syngas comprises partially oxidizing a gaseous feedstock containing substantial amounts of methane in a gasifier to produce a hot synthesis gas stream that is passed in indirect heat exchange through a steam reforming catalytic reactor. A portion of the steam reforming reaction products are mixed with the cooled gasifier synthesis gas stream exiting the steam reforming catalytic reactor to form a combined synthesis gas stream, called a "stoichiometric ratioed synthesis gas." The stoichiometric ratioed synthesis gas stream can then be passed into a methanol synthesis unit at substantially the specifications for optimal methanol production with little or no external compression. In a second embodiment the gasifier unit is arranged and operated in parallel with a primary steam reformer unit. The respective synthesis gas streams exiting each unit are combined to form a combined synthesis gas stream that undergoes oxidation in a secondary catalytic reformer unit to form a stoichiometric ratioed synthesis gas that requires minimal external compression before being converted to methanol.
机译:用于生产化学计量比的合成气的改进方法包括在气化器中部分氧化包含大量甲烷的气态原料,以产生热合成气流,该热合成气流通过蒸汽重整催化反应器进行间接热交换。将一部分蒸汽重整反应产物与离开蒸汽重整催化反应器的冷却的气化器合成气流混合以形成合并的合成气流,称为“化学计量比合成气”。然后可以将化学计量比的合成气流以基本达到最佳甲醇生产规格的方式通入甲醇合成装置,而很少或没有外部压缩。在第二实施例中,气化器单元与主蒸汽重整器单元平行布置和操作。离开每个单元的各个合成气流被合并以形成组合的合成气流,该组合的合成气流在次级催化重整器单元中进行氧化以形成化学计量比的合成气,该合成气在转化为甲醇之前需要最小的外部压缩。

著录项

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号