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CO2 capture from flue gas by two successive VPSA units using 13XAPG

机译:两个连续的VPSA装置使用13XAPG从烟气中捕获二氧化碳

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With the development of novel adsorbent material and adsorption process, adsorption technology has become a potential tool for the CO2 removal from flue gases. The reduction of carbon dioxide emissions from flue gases with two successive vacuum pressure swing adsorption (VPSA) units, using 13XAPG as the adsorbent, was investigated both theoretically and experimentally. A 3-bed 5-step VPSA process was designed to capture CO2 from flue gases, which included feed pressurization, adsorption, rinse, blowdown and counter-current purge. It was found that was difficult to achieve both high CO2 purity and high CO2 recovery by one VPSA unit when capturing CO2 from flue gases at atmospheric pressure. After the verification of one-column VPSA experiment for further concentrating CO2 stream from one VPSA unit to above 95 % purity, two successive VPSA units were designed, composed of 3-bed 5-step cycle for the first unit and 2-bed 6-step cycle for the second unit, and the effects of operating parameters on the separation behaviors were investigated by simulation. With the proposed VPSA process, a CO2 purity of 96.54 % was obtained with recovery of 93.35 %. The total specific power consumption of the two successive VPSA units was 528.39 kJ/kg_(CO2), while the unit productivity was 0.031 kg_(CO2)/kg h.
机译:随着新型吸附材料和吸附工艺的发展,吸附技术已成为从烟气中去除CO2的潜在工具。在理论上和实验上都研究了使用13XAPG作为吸附剂,采用两个连续的真空变压吸附(VPSA)装置减少烟道气中二氧化碳排放的方法。设计了一个三床五步VPSA工艺,用于从烟道气中捕集CO2,包括进料加压,吸附,冲洗,排污和逆流吹扫。发现在大气压下从烟道气中捕集二氧化碳时,很难通过一个VPSA装置同时实现高二氧化碳纯度和高二氧化碳回收率。在验证了将一台VPSA装置中的CO2物流进一步浓缩至纯度高于95%的单柱VPSA实验的验证之后,设计了两个连续的VPSA装置,其中第一台装置的3床5步循环和2床6式通过模拟研究了第二单元的第二步循环,以及操作参数对分离行为的影响。通过提出的VPSA工艺,CO2纯度达到96.54%,回收率达到93.35%。两个连续的VPSA单元的总单位能耗为528.39 kJ / kg_(CO2),而单位生产率为0.031 kg_(CO2)/ kg h。

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