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Enriched-air fluidized bed gasification using bench and pilot scale reactors of dairy manure with sand bedding based on response surface methods

机译:基于响应面法的使用带有砂层的乳牛粪的台式和中试规模反应器进行的富集流化床气化

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Enriched-air gasification was performed in fluidized bed reactors using the processed dairy manure which was mixed with sand bedding. The effects of temperature, modified equivalence ratio (ERm), and oxygen concentration on the gas products were investigated based on the statistical models using a bench-scale reactor in order to obtain empirical correlations. Then, the empirical equations were applied to compare the produced gases from a pilot-scale fluidized bed gasifier. The empirical and actual H-2 and CH4 compositions were within a 10% error, while the sum of produced CO and CO2 gases showed similar composition within 3% error. The most influential factors for the syngas heating value were temperature followed by the oxygen concentration and ER (equivalence ratio). The composition of H-2 (2.1-11.5%) and CO (5.9-20.3%) rose with an increase in temperature and oxygen concentration. The variation of CO2 (16.8-31.6%) was mainly affected by the degree of oxygen concentration in the gasifying agent. The ranges of the LHV (lower heating value), carbon conversion efficiency and cold gas efficiency were discussed. An economic review showed favorable indications for on-site dairy manure gasification process for electric power based on the depreciable payback period and the power production costs. (C) 2015 Elsevier Ltd. All rights reserved.
机译:在流化床反应器中进行浓缩空气气化,方法是将经过处理的乳牛粪与砂层混合。基于统计模型,使用台式规模的反应器,研究了温度,修正的当量比(ERm)和氧气浓度对气体产物的影响,以获得经验相关性。然后,应用经验方程式比较中试流化床气化炉产生的气体。经验和实际的H-2和CH4组成误差在10%以内,而产生的CO和CO2气体的总和显示出相似的组成在3%误差以内。对合成气热值影响最大的因素是温度,其次是氧气浓度和ER(当量比)。 H-2(2.1-11.5%)和CO(5.9-20.3%)的组成随温度和氧气浓度的增加而增加。 CO 2的变化(16.8-31.6%)主要受气化剂中氧气浓度的影响。讨论了LHV(较低的热值),碳转化效率和冷气效率的范围。经济评估显示,基于可折旧的投资回收期和发电成本,现场乳化气发电的有利迹象。 (C)2015 Elsevier Ltd.保留所有权利。

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