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Fischer-Tropsch synthesis has stage(s) separating water and hydrocarbons and water purification stage(s) with adsorbent chosen from activated carbon, hydrophobic clay or hydrophobic zeolite

机译:费-托合成具有将水和碳氢化合物分离的阶段和具有选自活性炭,疏水性粘土或疏水性沸石的吸附剂的净水阶段

摘要

The production of hydrocarbons and pure water by Fischer-Tropsch synthesis includes stage(s) to separate the water and hydrocarbons and water purification stage(s) involving contact with an adsorbent. The adsorbent is chosen from activated carbon, hydrophobic clay or its derivatives and hydrophobic zeolite or its derivatives. Preferred Features: Between separation and purification there is a stripping stage using steam or inert gas. This stage operates at 0.02-10 MPa and 60-210 deg C. The adsorbent operates at = 50 deg C. The amount of water treated per hour is about 5 times the mass of the adsorbent. Two adsorbent beds are arranged in parallel. One is used while the other is regenerated. The zeolite may have a silicon/aluminum molecular ratio - 20. After the purification stage(s) the water percolates through a bed of bacteria and/or activated sludge. Finally the water is exposed to air, mineralized and gasified with carbon dioxide at = 0.5 MPa also produced by the synthesis.
机译:通过费-托合成法生产烃和纯水包括将水和烃分离的阶段和涉及与吸附剂接触的水纯化阶段。吸附剂选自活性炭,疏水性粘土或其衍生物和疏水性沸石或其衍生物。优选的特征:在分离和纯化之间,存在使用蒸汽或惰性气体的汽提阶段。该阶段在0.02-10 MPa和60-210摄氏度下运行。吸附剂在<= 50摄氏度下运行。每小时处理的水量约为吸附剂质量的5倍。两个吸附床平行布置。一个被使用,而另一个则被再生。沸石的硅/铝分子比可以为20。在纯化阶段之后,水会通过细菌和/或活性污泥床渗透。最后,将水暴露于空气中,矿化并用合成法产生的<= 0.5 MPa的二氧化碳进行气化。

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