首页> 外国专利> A PROCESS FOR REMOVING HYDROGEN SULPHIDE AND CARBON DIOXIDE FROM FUEL GAS OR SYNTHESIS GAS CONTAINING THE SAME

A PROCESS FOR REMOVING HYDROGEN SULPHIDE AND CARBON DIOXIDE FROM FUEL GAS OR SYNTHESIS GAS CONTAINING THE SAME

机译:从燃料气体或含有该气体的合成气中脱除硫化氢和二氧化碳的方法

摘要

1,203,103. Purifying combustible gas. METALLGESELLSCHAFT A.G. 3 Oct., 1967 [14 Oct., 1966], No. 44926/67. Heading C5E. H 2 S and CO 2 are removed from fuel gas or synthesis gas by a process similar to that described in Specification 1,196,658. Scrubbing liquid containing CO 2 is divided into two main portions. The first traverses line 16, H 2 S absorber 4, flash tower 7, regenerating column 8, and heat exchangers 85, 94 for returning to the CO 2 absorber 5 cooled and completely regenerated; the second is cooled at 6 and partially regenerated in flash tower 9, optionally with CO 2 stripping at 93, for returning via 13 to a coarse scrubbing zone 51 of the absorber 5. Flashed-off gases containing H 2 and CO are returned via line 18 and compressor 42 to the gas input, and other flashed-off gases leave at 28 and 29. Ammonia evaporators 6, 54 are provided. Xylene may be used as scrubbing liquid.
机译:1,203,103。净化可燃气体。 METALLGESELLSCHAFT A.G.,1967年10月3日[1966年10月14日],第44926/67号。标题C5E。 H 2 S和CO 2通过类似于规范1196658中所述的方法从燃料气体或合成气中除去。含有CO 2的洗涤液分为两个主要部分。第一横穿管线16,H 2 S吸收器4,闪蒸塔7,再生塔8和热交换器85、94,用于使冷却并完全再生的CO 2吸收器5返回;第二个冷却至6,然后在闪蒸塔9中进行部分再生,必要时在93处进行CO 2汽提,以通过13返回吸收塔5的粗洗涤区51。闪蒸出的H 2和CO气体通过管线返回18和压缩机42进入气体输入,其他闪蒸气体在28和29处离开。设有氨气蒸发器6、54。二甲苯可用作洗涤液。

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