首页> 外国专利> Removal of nickel tetra:carbonyl and iron penta:carbonyl from hydrogen sulphide gases - by washing with methanol and removing condensate

Removal of nickel tetra:carbonyl and iron penta:carbonyl from hydrogen sulphide gases - by washing with methanol and removing condensate

机译:通过用甲醇洗涤并除去冷凝液,从硫化氢气体中除去四羰基镍和五羰基铁

摘要

Removal of Ni(CO)4 and Fe(CO)5 from H2S-rich gases. esp. Claus gas produced during methanol washing of crude synthesis gas and regeneration of the loaded methanol, comprises subjecting the Claus gas, cooled in many stages, to postwashing with metal carbonyl-free methanol, adding the washing soln. to the methanol washings and completely or partially removing the condensate from the last cooling stage from the process. PREFERRED PROCESS - Pref. the Claus gas stream, cooled to at least 40 deg.C is cooled to -15 to -55 deg.C in the last stage. Postwashing takes place at -15 to -55 (pref. -25 to -45) deg.C at 100-400 kPa superpressure. Metal carbonyl-free cold methanol from washing of crude synethesis gas is used as the postwash methanol. Postwashing of the Claus gas occurs by fine distribution of the washing liq. in the gas stream. Postwashing is a one- or multistage process. The loaded postwashing methanol is fed into the liq. phase of the condensate from the cooling stages of the Claus gas. ADVANTAGE - The removal of metal carbonyl prevents disturbances in the Claus Proces
机译:从富含H2S的气体中去除Ni(CO)4和Fe(CO)5。尤其是在甲醇洗涤粗合成气和负载的甲醇再生过程中产生的克劳斯气体,包括将经过多步冷却的克劳斯气体用无羰基金属的甲醇进行后洗涤,然后添加洗涤液。进行甲醇洗涤,并从过程的最后冷却阶段完全或部分除去冷凝物。优选过程-优选冷却至至少40℃的克劳斯气流在最后阶段被冷却至-15至-55℃。后洗是在-15至-55(优选-25至-45)℃,100-400 kPa超压下进行的。来自粗合成气洗涤的不含金属羰基的冷甲醇用作后洗涤甲醇。克劳斯气体的后洗涤是通过洗涤液的精细分布进行的。在气流中。后洗是一个单阶段或多阶段的过程。将装载的后洗甲醇加入液体中。克劳斯气体的冷却阶段产生的冷凝水相。优势-羰基金属的去除可防止Claus程序受到干扰

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