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Producing supported cobalt catalysts for the fischer-tropsch synthesis

机译:生产费-托合成的负载型钴催化剂

摘要

A process for producing a supported Fischer-Tropsch catalyst includes treating, in an activation stage (12), a particulate pre-reduction cobalt nitrate-based supported Fischer- Tropsch synthesis catalyst precursor containing reducible cobalt oxides, with hydrogen as a reducing gas in order to reduce the cobalt oxides over a period of time to Co, with ammonia and water being formed, the reduction including a time period when predominantly CoO is reduced to Co. Unreacted hydrogen is withdrawn (20), which thus includes water and treated to lower its dewpoint (14). At least a portion of the withdrawn unreacted hydrogen is returned to the activation stage (12) as recycle hydrogen (26). An ammonia concentration is maintained in the activation stage (12), at least during the time when predominantly CoO is reduced to Co, of less than 250 volume parts per million ("vppm").
机译:制备负载型费-托催化剂的方法包括在活化阶段(12)中,以氢作为还原气体依次处理包含可还原的钴氧化物的颗粒状的预还原的硝酸钴基的负载型费-托合成催化剂前体。为了在一段时间内将钴氧化物还原为Co并形成氨和水,该还原过程包括将CoO主要还原为Co的时间段。未反应的氢被抽出(20),因此其中包括水并进行了处理以降低其露点(14)。至少一部分取出的未反应氢作为再循环氢(26)返回活化阶段(12)。至少在主要将CoO还原成Co的时间内,在活化阶段(12)中保持小于百万分之250体积份(“ vppm”)的氨浓度。

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