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循环流化床锅炉高效炉内脱硫理论和关键技术 被引量:6
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作者 谭波 王传志 +2 位作者 司硕 刘忠攀 蓝天 《洁净煤技术》 CAS 2020年第4期168-174,共7页
低成本、无废水、系统简单的炉内脱硫技术是循环流化床锅炉实现洁净燃烧有效和优选途径之一。由于影响因素众多及试验数据分散,目前仍缺少具有普遍适用的脱硫效率预测手段,对于实际应用过程中脱硫效率随Ca/S比增加出现下降现象的原因还... 低成本、无废水、系统简单的炉内脱硫技术是循环流化床锅炉实现洁净燃烧有效和优选途径之一。由于影响因素众多及试验数据分散,目前仍缺少具有普遍适用的脱硫效率预测手段,对于实际应用过程中脱硫效率随Ca/S比增加出现下降现象的原因还未给出合理解释,单纯Ca/S比也无法反映实际参与脱硫的石灰石量,因而难以描述炉内石灰石的脱硫规律。为了探索决定炉内石灰石脱硫效率的本质,以锅炉炉内物料运动、分布规律为基础,通过探讨入炉石灰石随炉内物料运动及反应变化情况,对循环流化床炉内脱硫进行深入分析,提出“石灰石有效存有量”的概念,并根据灰平衡原理建立数学模型。通过与不同规模的燃烧颗粒煤和煤泥的工业循环流化床锅炉试验数据进行比较,验证了该模型的有效性。研究结果表明,实际决定炉内脱硫效率的最重要因素是“石灰石有效存有量”,该理论的建立为有效提高炉内脱硫效率提供了依据,由此得出实现炉内高效脱硫的关键在于:①优化石灰石粒度分布以有效提高外循环石灰石量和石灰石炉内的停留时间;②合理排渣以减少石灰石有效存有量的损失;③提高气-固接触效率以充分利用有效石灰石的活性。 展开更多
关键词 循环流化床锅炉 高效炉内脱硫 石灰石有效存有量 气-固接触效率
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Developments in the understanding of gas–solid contact efficiency in the circulating fluidized bed riser reactor:A review 被引量:6
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作者 Chengxiu Wang Jesse Zhu 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2016年第1期53-62,共10页
In the last several decades, circulating fluidized bed reactors have been studied in many aspects including hydrodynamics, heat and mass transfer and gas–solid two phase contacting. However, despite the abundance of ... In the last several decades, circulating fluidized bed reactors have been studied in many aspects including hydrodynamics, heat and mass transfer and gas–solid two phase contacting. However, despite the abundance of review papers on hydrodynamics, there is no summary paper on gas–solid contact efficiency to date, especially on high density circulating fluidized beds(CFBs). This paper gives an introduction to, and a review of the measurement of contact efficiency in circulating fluidized bed riser. Firstly, the popular testing method of contact efficiency including the method of heating transfer experiment and hot model reaction are discussed, then previous published papers are reviewed based on the discussed methods. Some key results of the experimental work are described and discussed. Gas–solid contact efficiency is affected by the operating conditions as well as the particle size distribution. The result of the contact efficiency shows that the CFB riser is far away from an ideal plug flow reactor due to the characteristics of hydrodynamics in the riser. Lacunae in the available literature have been delineated and recommendations have been made for further work. 展开更多
关键词 Circulating fluidized bed Riser High density Gas–solid contacting Heat transfer Ozone decomposition
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