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用于电厂燃烧后二氧化碳捕集的“连续膜柱”的膜级联类型 第1部分:二元气体混合物分离的模拟

Membrane Cascade Type of «Continuous Membrane Column» for Power Plant Post-Combustion Carbon Dioxide Capture Part 1: Simulation of the Binary Gas Mixture Separation.

作者信息

Atlaskin Artem A, Petukhov Anton N, Stepakova Anna N, Tsivkovsky Nikita S, Kryuchkov Sergey S, Smorodin Kirill A, Moiseenko Irina S, Atlaskina Maria E, Suvorov Sergey S, Stepanova Ekaterina A, Vorotyntsev Ilya V

机构信息

Laboratory of Electronic Grade Substances Technologies, Mendeleev University of Chemical Technology of Russia, 125047 Moscow, Russia.

Chemical Engineering Laboratory, National Research Lobachevsky State University of Nizhny Novgorod, 603022 Nizhny Novgorod, Russia.

出版信息

Membranes (Basel). 2023 Feb 24;13(3):270. doi: 10.3390/membranes13030270.

DOI:10.3390/membranes13030270
PMID:36984657
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC10057425/
Abstract

The present paper deals with the complex study of CO capture from combined heat power plant flue gases using the efficient technological design of a membrane cascade type of «Continuous Membrane Column» for binary gas mixture separation. In contrast to well-known multi-step or multi-stage process designs, the cascade type of separation unit provides several advantages. Here, the separation process is implemented in it by creating two counter current flows. In one of them is depleted by the high-permeable component in a continuous mode, meanwhile the other one is enriched. Taking into account that the circulating flows rate overcomes the withdrawn one, there is a multiplicative increase in separation efficiency. A comprehensive study of CO capture using the membrane cascade type of «Continuous Membrane Column» includes the determination of the optimal membrane material characteristics, the sensitivity study of the process, and a feasibility evaluation. It was clearly demonstrated that the proposed process achieves efficient CO capture, which meets the modern requirements in terms of the CO content (≥95 mol.%), recovery rate (≥90%), and residual CO concentration (≤2 mol.%). Moreover, it was observed that it is possible to process CO with a purity of up to 99.8 mol.% at the same recovery rate. This enables the use of this specific process design in CO pretreatment operations for the production of high-purity carbon dioxide.

摘要

本文论述了利用“连续膜柱”型膜级联的高效工艺设计,对联合热电厂烟气中的CO捕集进行综合研究,以分离二元气体混合物。与众所周知的多步或多级工艺设计相比,级联型分离单元具有若干优点。在此,分离过程通过形成两个逆流来实现。在其中一个流中,高渗透组分以连续模式被消耗,而另一个流则被富集。考虑到循环流速超过抽出流速,分离效率呈倍增增加。使用“连续膜柱”型膜级联对CO捕集进行的综合研究包括确定最佳膜材料特性、过程敏感性研究和可行性评估。结果清楚地表明,所提出的工艺实现了高效的CO捕集,在CO含量(≥95摩尔%)、回收率(≥90%)和残余CO浓度(≤2摩尔%)方面符合现代要求。此外,观察到在相同回收率下,可以处理纯度高达99.8摩尔%的CO。这使得这种特定的工艺设计能够用于生产高纯度二氧化碳的CO预处理操作中。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/8df99c6e36e3/membranes-13-00270-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/ffa2ff40f693/membranes-13-00270-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/4c42dc098f03/membranes-13-00270-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/fcf616a51395/membranes-13-00270-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/bd7b3e7f304e/membranes-13-00270-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/f4138e571620/membranes-13-00270-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/90adb3a62958/membranes-13-00270-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/da6d446d632e/membranes-13-00270-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/8df99c6e36e3/membranes-13-00270-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/ffa2ff40f693/membranes-13-00270-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/4c42dc098f03/membranes-13-00270-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/fcf616a51395/membranes-13-00270-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/bd7b3e7f304e/membranes-13-00270-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/f4138e571620/membranes-13-00270-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/90adb3a62958/membranes-13-00270-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/da6d446d632e/membranes-13-00270-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cbf1/10057425/8df99c6e36e3/membranes-13-00270-g008.jpg

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