填料床塔式反应器去除二氧化碳的建模与优化

K. Thirugnanasambandham
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引用次数: 1

摘要

温室气体导致的全球变暖已经成为一个严重的全球性问题。由于二氧化碳(CO2)是造成这一现象的主要原因,人们正在通过碳捕获来对抗这一现象。在不同的工艺参数(如温度、进料流量和吸附剂质量)下,研究了聚-(D)氨基葡萄糖在填充床塔式反应器中的CO2捕集。为分析工艺参数对填料床塔中CO2捕集能力的影响,进行了实验统计设计。所得结果表明,进料流量对其影响较大。在以下操作条件下,最多可捕获956毫克二氧化碳;温度40℃,进料流速30 ml/min,加入0.25 g聚-(D)氨基葡萄糖。证实了聚-(D)氨基葡萄糖在填料床塔中捕获CO2的能力。
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Modeling and Optimization of Carbon Dioxide Removal in Packed Bed Column Reactor
Global warming due to greenhouse gases has become a serious global issue. Extensive efforts are being made to fighting this phenomenon through carbon capture as carbon dioxide (CO2) is its major contributor. This study focused on CO2 capture in packed bed column reactor using Poly-(D) glucosamine under the various process parameters such as temperature, feed flow rate and mass of the adsorbent. Statistical design of experiments was carried out in order to analysis the effect process parameters on the capacity of CO2 capture in packed bed column. The obtained results show that feed flow rate has the significant affect compared to others. The maximum of 956 mg of CO2 is captured under the following operating conditions; temperature of 40oC, feed flow rate of 30 ml/min and 0.25 g of the Poly-(D) glucosamine. The ability of Poly-(D) glucosamine to capture the CO2 in packed bed column is confirmed.
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