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作 者:孙锋 申成 罗聪[2] 罗童 SUN Feng;SHEN Cheng;LUO Cong;LUO Tong(China Ship Development and Design Center,Wuhan 430064,China;State Key Laboratory of Coal Combustion,Huazhong University of Science and Technology,Wuhan 430074,China)
机构地区:[1]中国舰船研究设计中心,湖北武汉430064 [2]华中科技大学煤燃烧国家重点实验室,湖北武汉430074
出 处:《洁净煤技术》2021年第2期180-186,共7页Clean Coal Technology
基 金:国家自然科学基金资助项目(51606076)。
摘 要:钙基吸附剂进行多次CO_(2)捕集后,碳酸化效率会大幅衰减,此时的吸附剂能否高效脱硫利用是值得重点关注的问题。鉴于此,筛选了高性能合成钙基吸附剂和天然石灰石吸附剂,通过热重分析仪分析对比其在多循环CO_(2)捕集后的碳酸化和硫酸化反应性能,采用微粒模型研究其硫酸化反应动力学特征。结果发现,高性能合成钙基吸附剂的碳酸化反应速率和CO_(2)吸附能力明显高于石灰石吸附剂。在长达500循环的CO_(2)捕集试验后,高性能合成钙基吸附剂的CO_(2)吸附能力比石灰石高10倍以上,其SO_(2)吸附能力相较于石灰石提升约40%。经历多次CO_(2)捕集反应循环后,2种吸附剂的硫酸化能力均有提升:其中,石灰石吸附剂的提升幅度更大,硫酸化转化率从26%提升到35%,而高性能合成钙基吸附剂的硫酸化转化率则从38%提升到43%。通过微粒模型计算发现,2种吸附剂的硫酸化反应均是与SO_(2)浓度相关的一级反应,多循环捕集CO_(2)反应后,石灰石吸附剂的硫酸化反应活化能下降接近30%,而高性能合成钙基吸附剂的硫酸化反应活化能只下降了5%。研究结果说明2种不同钙基吸附剂在进行循环CO_(2)捕集后,脱硫能力得到了不同程度的提高,且均可以较好地应用于SO_(2)的脱除。The carbonation conversion of the calcium-based sorbent decreases significantly after multiple CO_(2) capture cycles,whether the sorbent can be further used efficiently in desulfurization reaction is important issue which deserves concerns.In order to delve into this is⁃sue,the high performance calcium-based sorbent and natural limestone sorbent were selected,the carbonation and sulfation reaction per⁃formance after multiple CO_(2) capture cycles were analyzed and compared by thermal gravimetric analyzer,and the sulfation kinetics charac⁃teristics were studied by particle model.The results showed that the rate of carbonation reaction and CO_(2) adsorption capacity of the high performance calcium-based sorbents are much higher than those of limestone adsorbent.After multiple cycles of CO_(2) capture test,the CO_(2) adsorption capacity of high performance calcium-based sorbents is over 10 times higher than that of limestone,and its SO_(2) adsorption ca⁃pacities was improved by 40%than that of limestone.After multiple CO_(2) capture reactions,their sulfation abilities are both improved.The improvement of limestone is greater,the sulfation conversion is increased from 26%to 35%,while the sulfation conversion of high perform⁃ance calcium-based sorbent is increased from 38%to 43%.It is found through particle model calculation that the sulfation process of both sorbents is a first-order reaction related to the concentration of SO_(2).After the multiple CO_(2) capture cycles,the activation energy of sulfa⁃tion reaction of limestone decreases by nearly 30%,while that of high performance calcium-based sorbent only decreases by 5%.The re⁃sults indicate that the desulphurization capacity of two different calcium-based sorbents can be improved to different degrees after multiple CO_(2) capture cycles,and both of them can be better used for SO_(2) removal.
关 键 词:钙基吸附剂 硫酸化 CO_(2)捕集 微粒模型 反应动力学
分 类 号:TK09[动力工程及工程热物理]
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