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Steam regeneration of PEI impregnated silica sorbents for post-combustion CO_2 capture: preliminary results

机译:PEI浸渍二氧化硅凝乳剂的蒸汽再生用于燃烧后CO_2捕获:初步结果

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Extensive research work is under progress in the field of post-combustion CO_2 capture from flue gas, focusing on design of new, cost-effective and selective adsorbents and adsorption technologies. Recently, a lot has been mentioned in literature on using steam stripping for capturing CO_2 from flue gas and the ease of recovery of CO_2 by condensing the moisture. But very little data is available on suitability of steam for multi-cyclic CO_2 adsorption study. Previous work on suitability of amine based solid adsorbents for CO_2 capture using an inert gas for the regeneration step has been carried out in our research group. The primary focus of the current work is to study CO_2 regeneration using steam stripping. Commercial silica support (Fuji Silysia Cariact Grade Q-10, particle size 75-150 μm) was impregnated with low molecular weight Polyethyleneimine (PEI) (Sigma Aldrich, Mn-600), using wet impregnation technique. CO_2 adsorption-desorption cyclic study was conducted in a lab-scale packed bed reactor. The reactor was a 1/2 inch stainless steel tube with a frit to hold the sample. All the connecting lines were heated to prevent condensation of steam. 1g of sorbent was fed at a time. The effluent gas composition from reactor was analyzed with a Pfieffer Mass spectrometer (Omnistar GSD 320). Firstly, the sample was heated to 110°C and purged with 100 cc/min N_2 to remove any CO_2 and moisture adsorbed in the sample. The sorbent was then cooled down to 75°C (adsorption temperature). After the temperature stabilized, 100 cc/min. of gas (10% CO_2 balanced with N_2 (henceforth mentioned as flue gas)) was passed through the reactor. Adsorption was carried out for 10 min. After this the temperature of reactor was ramped up to 110°C. At this point, the sorbent was stripped of CO_2 using a mixture of 90% H_2O and 10% N_2 (henceforth mentioned as steam). N_2 was added as a reference gas in the MS. Steam stripping was carried out for 10 min, followed by drying of sample at 110°C using N_2 and then cooling to 75°C for the next cycle. A set of 20 cycles was performed in this way. A K-type thermocouple was used to record the temperature profile in the sample during adsorption and desorption.
机译:广泛的研究工作正在燃油燃气后CO_2捕获领域正在进行,重点是设计新,经济效益和选择性吸附剂和吸附技术。最近,使用蒸汽汽提来捕获来自烟道气的CO_2的蒸汽汽提以及通过冷凝水分缩小CO_2的易于恢复的文献中提到了很多。但是,对于多循环CO_2吸附研究的蒸汽适用性非常少。在我们的研究组中,在我们的研究组中进行了使用惰性气体的Co_2捕获的胺基固体吸附剂的适用性。目前工作的主要重点是使用蒸汽汽提研究CO_2再生。使用湿浸渍技术,用低分子量聚乙烯亚胺(PEI)(Sigma Aldrich,MN-600)浸渍商业二氧化硅载体(富士甲岛CARIACE Q-10,粒径75-150μm)。 CO_2吸附 - 解吸循环研究是在实验室规模的填充床反应器中进行的。反应器是1/2英寸不锈钢管,玻璃料以保持样品。加热所有连接线以防止蒸汽冷凝。 1克吸附剂一次喂食。用PFieffer质谱仪(Omnistar GSD 320)分析来自反应器的废气组合物。首先,将样品加热至110℃并用100cc / min n_2吹扫,以除去吸附在样品中的任何CO_2和水分。然后将吸附剂冷却至75℃(吸附温度)。温度稳定后,100cc / min。通过反应器通过气体(用N_2(以后称为烟气)平衡的10%CO_2)通过反应器。吸附10分钟。在此之后,反应器的温度升高至110℃。此时,使用90%H_2O和10%N_2的混合物(作为蒸汽提及的10%N_2的混合物,将吸附剂剥离CO_2。将N_2加入MS中的参考气体。进行蒸汽汽提10分钟,然后使用N_2在110℃下干燥样品,然后冷却至下一个循环的75℃。以这种方式进行一组20个循环。 K型热电偶用于在吸附和解吸期间记录样品中的温度曲线。

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