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Experimental validation of the calcium looping CO2 capture process with two circulating fluidized bed carbonator reactors

机译:使用两个循环流化床碳酸化器反应器进行钙循环CO2捕集过程的实验验证

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摘要

[EN] Postcombustion CO2 capture using CaO as a regenerable solid sorbent in a circulating fluidized bed\ud(CFB) carbonator is emerging as a promising CO2 capture technology. Experimental validation of this\udconcept is provided through a comparative analysis of the results obtained in two laboratory-scale dual\udfluidized bed (DFB) installations located at INCAR-CSIC (Spain) and IFK (Germany). The analysis is focused on the performance of the CFB carbonator reactors operated with continuous solid circulation of\udCaO. A reasonable closure of the carbon balances (i) between the CO2 that has disappeared from the gas\udphase, (ii) the CaCO3 circulating between the reactors and (iii) the CaCO3 that is formed within the\udcarbonator bed has been established. A necessary condition for the capture of a given molar flow of CO2\udis experimentally demonstrated and requires that a slightly over-stoichiometric molar flow of active CaO\udis supplied to the carbonator. The deactivation behavior of the sorbents during continuous looping\udconditions has been measured. The key parameter to interpret the carbonator reactor results has been the\udactive space time, that is indicative of the CaO inventory per molar flow of CO2 participating in the\udcarbonation reaction and of the reaction rate of the solid inventory in the reactor. Two different\udapproaches have been utilized in order to find a suitable expression for this parameter, thus achieving its\udcorrelation with the CO2 capture efficiency. A simple model assuming instant mixing of solids and plugflow\udof the gas has been tested. Based mainly on carbonator active space time variation, the CO2 capture\udefficiency are shown to lie between 30 % and above 90 %. These results confirm the technical viability\udof the calcium looping postcombustion CO2 capture process. They have been used for designing the\udcurrent pilot-plant facilities which are scaled up 20-50 times in regard to the lab-scale units. Moreover,\udthe lab-scale results obtained allow for simulation work to be initiated in regard to the full scale Ca looping application.
机译:[EN]使用CaO作为循环流化床\ ud(CFB)碳酸化器中的可再生固体吸附剂进行燃烧后CO2捕集正在成为一种有前途的CO2捕集技术。通过对位于INCAR-CSIC(西班牙)和IFK(德国)的两个实验室规模的双流化床(DFB)装置获得的结果进行比较分析,提供了对这一概念的实验验证。该分析集中于连续的\ udCaO固体循环运行的CFB碳酸化​​器反应器的性能。已经建立了合理的碳平衡平衡:(i)从气相中消失的二氧化碳之间;(ii)在反应器之间循环的CaCO3;以及(iii)在碳化器床中形成的CaCO3。实验证明了捕获给定摩尔流量的二氧化碳的必要条件,并要求向碳酸化器供应的活性碳酸钙的摩尔流量略高于化学计量。已经测量了在连续成环条件下吸附剂的失活行为。解释碳酸化器反应器结果的关键参数是“空余时间”,它表示参与碳酸化反应的每摩尔CO2的CaO存量和反应器中固体存量的反应速率。为了找到适合该参数的表达式,使用了两种不同的方法,从而实现了与二氧化碳捕获效率的相关。测试了一个简单模型,该模型假设固体和气体的活塞流\ ud立即混合。主要基于碳酸化器的活跃时空变化,表明CO2捕集/效率不足介于30%和90%以上。这些结果证实了钙循环燃烧后CO 2捕集过程的技术可行性。它们已用于设计\ udcurrent中试工厂设施,相对于实验室规模的单位,该工厂的规模扩大了20至50倍。此外,获得的实验室规模的结果允许就全比例Ca循环应用启动仿真工作。

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