首页> 外国专利> METHOD FOR SEPARATING AND DETERMINING RELATIVELY STRONG ON ADSORPTION AGENTS, ADSORBABLE GASES FROM GAS MIXTURES OTHERWHERE THEREOUGH ONLY LESS ADSORBABLE GASES, AND SYSTEM FOR CARRYING OUT THIS

METHOD FOR SEPARATING AND DETERMINING RELATIVELY STRONG ON ADSORPTION AGENTS, ADSORBABLE GASES FROM GAS MIXTURES OTHERWHERE THEREOUGH ONLY LESS ADSORBABLE GASES, AND SYSTEM FOR CARRYING OUT THIS

机译:相对较弱的吸附剂,气体混合物中的吸附气体进行分离和测定的方法以及实施该方法的系统

摘要

In the separation and recovery of gases which are relatively strongly adsorbable on adsorbents (product gas components), especially methane or carbon dioxide, from gas mixtures which otherwise contain essentially only more lightly adsorbable gases (waste gas components), and especially carbon-containing adsorbents by means of the pressure- swing technique in adsorbers, wherein the starting gas mixture which is to be separated is passed in the adsorption phase through an adsorbent layer with adsorption of the product gas component(s) and outflow of the waste gas component(s), until just before the product gas component(s) break(s) through, the product gas component(s) is or are then desorbed by lowering the pressure and flushing and, after conclusion of the desorption, the gas pressure in the adsorber is restored by a gas mixture from the pressure-swing process for a new adsorption phase, a product gas of high purity and yield is obtained by flushing with product gas components of approximately product gas quality, at least towards the end of flushing, up to adsorption pressure, the gas initially flowing out being passed into the waste gas and the gas flowing out later, which is enriched in the product gas component(s), optionally being recycled to the pressure-swing process, whereupon the desorption phase follows in which, with expansion, especially evacuation, of the adsorber to a lower pressure, a highly enriched product gas is obtained, of which a part is returned to the pressure-swing process for flushing and the rest is recovered.
机译:在从气体混合物中分离和回收相对较强地吸附在吸附剂(产物气体成分)上的气体,特别是甲烷或二氧化碳时,该气体混合物基本上只含有较轻的可吸附气体(废气成分),尤其是含碳吸附剂借助于吸附器中的变压技术,其中将要分离的起始气体混合物在吸附相中通过吸附剂层,同时吸附产物气成分并排出废气成分。 ),直到产品气成分突破之前,通过降低压力和冲洗来清除产品气成分,然后在解吸结束后再通过吸附器中的气体压力进行解吸通过变压过程中的气体混合物将其回收到新的吸附阶段,通过用适当的产品气组分冲洗获得高纯度和高产率的产品气至少在冲洗结束时达到吸附气体压力的产物气体质量接近,吸附气体最初流出的气体进入废气,随后流出的气体富含产物气成分,视情况而定循环到变压过程中,随后进入解吸阶段,在该阶段中,吸附器膨胀(尤其是抽空)至较低压力,获得了高度浓缩的产品气,其中一部分气体返回变压过程冲洗,其余的恢复。

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