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Using pressure swing adsorption (PSA) technology to purify carbon monoxide (CO) discharged from industrial gases is a high-efficiency and economical method. In this article, a four-bed PSA experiment for CO purification was improved and optimized, in which a set of 120 m^3·h^-1 pilot-scale PSA device was developed to purify CO from industrial tail gases, a set of control systems suitable for industry production was developed, and the influences of the operating parameters on CO purification were investigated. The experimental results indicated that the pilot-scale PSA device could produce qualified product gas and get high CO recovery ratio under optimized conditions. The research may provide reliable fundamental data, for industrial scale utilization of CO, from industrial tail gases, and have strong market competitive power and a broad promoted application prospect. 相似文献
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《分离科学与技术》2012,47(9):845-864
Abstract Binary mixtures can be separated into two high-purity products by a new pressure swing adsorption (PSA) cycle. The product purity depends on the purge/feed ratio of the respective gases in the PSA cycle. The process characteristics of the new PSA cycle, using activated carbon as the sorbent, can be adequately predicted by an equilibrium model. 相似文献
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《分离科学与技术》2012,47(14-15):2379-2396
Abstract Pressure swing adsorption (PSA) processes for air separation differ by the modes and conditions of operation of the adsorption, the desorption, and the complementary steps, as well as by the types of adsorbents used. Three commercial PSA processes for air separation are reviewed and compared. The first process uses a zeolitic adsorbent and produces only an oxygen-enriched product gas. The second process uses a carbon molecular sieve and produces only a nitrogen-enriched product gas. The third process uses a zeolite and simultaneously produces both oxygen-and nitrogen-enriched product gases. The performance and separation efficiency of the last process, called the ‘vacuum swing adsorption (VSA) process’, are reported to be superior to the others. 相似文献
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简单介绍了变压吸附气体分离技术的工艺特点,技术进展和在我国的应用情况,对变压吸附各种不同的工艺在粉末冶金生产过程中的应用进行了展望,预计该技术在粉末冶金行业将会得到迅速推广,为生产厂家带来良好的经济效益,促进粉末冶金技术的进步。 相似文献
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变压吸附分离CO技术及其在羰基合成工业中的应用 总被引:2,自引:0,他引:2
简述了不同吸附分离CO技术的特点,介绍了变压吸附分离CO技术的原理和工艺现状以及羰基合成工业中分离CO技术的选择. 相似文献
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变压吸附分离提纯CO_2技术的应用 总被引:3,自引:0,他引:3
本文叙述了变压吸附提纯CO2技术的基本原理和工艺过程,介绍了我国PSA-CO2的开发过程及发展前景,对已开发的PSA-CO2工业装置的生产成本和经济性进行了分析 相似文献
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我国煤层气蕴藏丰富,在面临能源危机时代煤层气可作为天然气能源的有效补充。本文介绍了低浓煤层气回收即CH4/N2分离几种常见技术:低温技术、水合物技术、溶解技术、膜分离和变压吸附技术(PSA)的分离原理、技术开发和研究的现状,并分析了各项技术目前存在的问题。讨论了多孔材料,如活性炭、碳分子筛、沸石分子筛和新型金属有机骨架材料(MOFs)等对CH4/N2吸附分离效果的研究进展,由于MOFs材料的吸附性能随温度或压力的改变出现飞跃,预示了其在PSA领域广阔的应用前景。 相似文献
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介绍了变压吸附(PSA)技术在回收电石法聚氯乙烯生产过程的精馏尾气中氢气的原理及应用,阐述了变压吸附技术的工艺流程及其分离原理,分析了采用此技术后的环境和经济效益。 相似文献
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《Gas Separation & Purification》1993,7(4):247-251
The development and commercialization of carbon molecular sieves (CMS) are closely connected with the development of pressure swing adsorption (PSA) processes for the separation of gases. It was already known in the 1960s that certain carbonaceous materials have a molecular sieving effect similar to that of the well known zeolitic molecular sieves. The effect was observed during basic research on anthracite and bituminous coal which are both known to be porous. However, the separation effect, e.g. for oxygen/nitrogen, was very small. It was not until the 1970s that large-scale production of uniform quality CMS suitable for commercial application in PSA processes was established. Nowadays, different types of CMS are successfully used in PSA plants, e.g. for the generation of nitrogen from air, for the production of methane from biogases, and for the recovery of hydrogen from coke oven and steam reforming gases1–4. 相似文献
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Huiru Li Zuwei Liao Jingyuan Sun Binbo Jiang Jingdai Wang Yongrong Yang 《中国化学工程学报》2019,27(8):1870-1878
Methane steam reforming is the main hydrogen production method in the industry. The product of methane steam reforming contains H_2, CH_4, CO and CO_2 and is then purified by pressure swing adsorption(PSA) technology. In this study, a layered two-bed PSA process was designed theoretically to purify H_2 from methane steam reforming off gas. The effects of adsorption pressure, adsorption time and purgeto-feed ratio(P/F ratio) on process performance were investigated to design a PSA process with more than99.95% purity and 80% recovery. Since the feed composition of the PSA process changes with the upstream process, the effect of the feed composition on the process performance was discussed as well.The result showed that the increase of CH_4 concentration, which was the weakest adsorbate, would have a negative impact on product purity. 相似文献
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《Gas Separation & Purification》1993,7(2):69-73
Recent pressure swing adsorption (PSA) processes are designed to produce multiple product gases of high purity and recovery from binary or multicomponent feed gases. Processes are also designed to alter the composition of a feed gas mixture. One example of these new processes is described and its performance reported. The commercial adsorbents used in these processes come from a large family of generic adsorbents like zeolites, activated carbons, silica and alumina gels, etc. Most of these adsorbents are energetically very heterogeneous. This makes a priori design of these processes extremely difficult and experimental process performance data are needed. Several fundamental problems on this subject are discussed. 相似文献