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METHOD FOR PURIFYING HYDROGEN OR HELIUM, AND DEVICE FOR PURIFYING HYDROGEN OR HELIUM

机译:提纯氢或氦的方法以及提纯氢或氦的装置

摘要

This method that purifies hydrogen or helium from a source gas mainly composed of hydrogen or helium and including volatile aromatic compounds as impurities by using a PSA technique performed using adsorption towers (10A to 10C) filled with absorbents repeats a cycle that includes an adsorption step, a depressurization step, a desorption step, and a cleaning step in the adsorption towers (10A to 10C). The adsorption towers (10A to 10C) are divided into a first region, a second region, and a third region in order from the upstream side to the downstream side in a flow direction of the source gas in the adsorption towers. The first region is filled with a silica gel-based first adsorbent 131 having a fill ratio of 15 to 75 vol% relative to the total fill capacity of adsorbents. The second region is filled with a zeolite-based second adsorbent 132 having a fill ratio of 15 to 75 vol%. The third region is filled with an activated carbon-based third adsorbent 133 having a fill ratio of 5 to 30 vol%.
机译:该方法通过使用填充有吸收剂的吸附塔(10A至10C)通过PSA技术从主要由氢或氦组成,并包含挥发性芳香族化合物作为杂质的原料气中纯化氢或氦的方法重复了一个包括吸附步骤的循环,吸附塔(10A至10C)中的减压步骤,解吸步骤和清洁步骤。沿吸附塔中的原料气体的流动方向从上游侧到下游侧按顺序将吸附塔(10A至10C)划分为第一区域,第二区域和第三区域。第一区域填充有基于硅胶的第一吸附剂131,其相对于吸附剂的总填充容量具有15至75vol%的填充率。第二区域填充有填充率为15〜75体积%的沸石类第二吸附剂132。在第三区域中填充有填充率为5〜30体积%的活性炭类第三吸附剂133。

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