| 带循环的二阶变压吸附碳捕集工艺模拟、实验及分析 |
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| 引用本文： | 刘冰,孙伟娜,安亚雄,江南,汪亚燕,邢瑞,张东辉.带循环的二阶变压吸附碳捕集工艺模拟、实验及分析[J].化工学报,2018,69(11):4788-4797. |
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| 作者姓名： | 刘冰 孙伟娜 安亚雄 江南 汪亚燕 邢瑞 张东辉 |
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| 作者单位： | 1. 化学工程联合国家重点实验室, 天津大学化工学院化学工程研究所, 天津 300350;
2. 乐凯医疗科技有限公司, 河北 保定 071054 |
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| 摘 要： | 针对日益严重的温室效应及传统CO2捕集和储存技术的不足，设计带循环的二阶四塔变压吸附装置捕集电厂烟道气中的二氧化碳，采用炭分子筛作为第一阶二塔处理装置吸附剂，采用13X作为第二阶二塔处理装置的吸附剂。建立上述工艺的数学模型，通过实验验证数学模型和模拟结果的准确性。模拟结果表明，本工艺可以将烟道气中的CO2（15%）富集为纯度95%的产品气，收率为93.92%，工艺处理量为4.576 mol CO2·h-1·kg-1，能耗为0.847 MJ·（kg CO2）-1，通过对比，本工艺具有处理量大、回收率高、纯度高的优点。在此基础上，根据数学模型分析二阶床层在一个周期内的压力变化、温度分布、固相和气相组成分布、能耗组成、生产能力。
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| 关 键 词： | 吸附 数值模拟 实验验证 二氧化碳捕集 炭分子筛 13X |
| 收稿时间： | 2018-04-11 |
| 修稿时间： | 2018-09-19 |
Simulation,experimentation and analyzation of two stage pressure swing adsorption process for CO2 capture |
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| LIU Bing,SUN Weina,AN Yaxiong,JIANG Nan,WANG Yayan,XING Rui,ZHANG Donghui.Simulation,experimentation and analyzation of two stage pressure swing adsorption process for CO2 capture[J].Journal of Chemical Industry and Engineering(China),2018,69(11):4788-4797. |
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| Authors: | LIU Bing SUN Weina AN Yaxiong JIANG Nan WANG Yayan XING Rui ZHANG Donghui |
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| Affiliation: | 1. State Key Laboratory of Chemical Engineering, Chemical Engineering Research Center, School of Chemical Engineering and Technology, Tianjin University, Tianjin 300350, China;
2. Lekai Medical Technology Co., Ltd., Baoding 071054, Hebei, China |
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| Abstract: | Aiming at the increasingly serious greenhouse effect and shortcomings of traditional CO2-capture and storage technology (CCS), the two-stage and four-bed pressure swing adsorption (PSA) device was investigated to capture carbon dioxide from flue gas of power plant, which used carbon molecular sieve as the adsorbent of the first stage process and 13X zeolite as the adsorbent of the second stage process. In order to improve the recovery of CO2, a cycle was added into the process. The mathematical model of the above process was established. Then experiment was carried out, and the accuracy of the model was verified by comparison between the results of experiment and simulation. Results of simulation displayed that the trace CO2 (15%) in the flue gas could be enriched to 95% with a recovery of 93.92%. The productivity was 4.576 mol CO2·h-1·kg-1 while the energy consumption was only 0.847 MJ·(kg CO2)-1. By comparing with other processes, this process has the characteristics of high recovery, high purity and large amount of productivity. On this basis, the analysis of energy consumption, the temperature distribution, composition distribution in solid phase and gas phase were carried out within a cycle. |
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| Keywords: | adsorption numerical simulation experimental validation carbon dioxide capture carbon molecular sieve 13X |
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