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The combined effect of H2O and SO2 on CO2 uptake and sorbent attrition during fluidised bed calcium looping
Proceedings of the Combustion Institute ( IF 5.3 ) Pub Date : 2018-08-25 , DOI: 10.1016/j.proci.2018.08.013
Antonio Coppola , Alessandro Esposito , Fabio Montagnaro , Mauro Iuliano , Fabrizio Scala , Piero Salatino

The effect of steam and sulphur dioxide on CO2 capture by limestone during calcium looping was studied in a novel lab-scale twin fluidised bed device (Twin Beds – TB). The apparatus consists of two interconnected batch fluidised bed reactors which are connected to each other by a duct permitting a rapid and complete pneumatic transport of the sorbent (limestone) between the reactors. Tests were carried out under typical calcium looping operating conditions with or without the presence of H2O and/or SO2 during the carbonation stage. Carbonation was carried out at 650°C in presence of 15% CO2, 10% steam (when present) and by investigating two SO2 levels, representative of either raw (1500 ppm) or pre-desulphurised (75 ppm) typical flue gas derived from coal combustion. The sorbent used was a reactive German limestone. Its performance was evaluated in terms of CO2 capture capacity, sulphur uptake, attrition and fragmentation. Results demonstrated the beneficial effect of H2O and the detrimental effect of SO2 on the CO2 capture capacity. When both species were simultaneously present in the gas, steam was still able to enhance the CO2 capture capacity even outweighing the negative effect of SO2 at low SO2 concentrations. A clear relationship between degrees of Ca carbonation and sulphation was observed. As regards the mechanical properties of the sorbent, both H2O and SO2 hardened the particle surface inducing a decrease of the measured attrition rate, that was indeed always very low. Conversely, the fragmentation tendency increased in presence of H2O and SO2 most likely due to the augmented internal stresses within the particles. Clear bimodal particle size distributions for in-bed sorbent fragments were observed. Microstructural scanning electron microscope and porosimetric characterisations aided in explaining the observed trends.



中文翻译:

H 2 O和SO 2对流化床钙循环过程中CO 2吸收和吸附剂损耗的联合作用

在新型实验室规模的双流化床设备(Twin Beds – TB)中研究了蒸汽和二氧化硫对钙环化过程中石灰石捕集CO 2的影响。该设备由两个相互连接的间歇流化床反应器组成,它们通过导管相互连接,从而允许在反应器之间快速,完全地气动吸附剂(石灰石)输送。在碳酸化阶段中在有或没有H 2 O和/或SO 2的情况下,在典型的钙循环操作条件下进行测试。碳酸化反应是在650°C,15%CO 2和10%蒸汽(如果存在)存在下,通过研究两种SO 2进行的。浓度,代表来自煤炭燃烧的原始(1500 ppm)或预脱硫(75 ppm)典型烟气。所用的吸附剂是反应性德国石灰石。根据CO 2捕集能力,硫吸收,磨损和碎裂来评估其性能。结果证明了H 2 O的有益作用和SO 2对CO 2捕集能力的有害作用。当两种物质同时存在于气体中时,蒸汽仍然能够提高CO 2的捕集能力,甚至抵消了低SO 2下SO 2的负面影响。浓度。观察到Ca碳酸化程度与硫酸化程度之间存在明显的关系。关于吸附剂的机械性能,H 2 O和SO 2均使颗粒表面变硬,从而导致测得的磨损率降低,这实际上总是非常低的。相反,在H 2 O和SO 2的存在下,碎裂趋势增加的原因很可能是由于颗粒内部的内应力增加。观察到床内吸附剂碎片的清晰的双峰粒度分布。显微结构扫描电子显微镜和孔隙率表征有助于解释观察到的趋势。

更新日期:2018-08-25
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