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作 者:田朕 韩洋 代正华 周峰[3] 王辅臣 TIAN Zhen;HAN Yang;DAI Zhenghua;ZHOU Feng;WANG Fuchen(School of Resources and Environmental Engineering,East China University of Science and Technology,Shanghai Coal Gasification Engineering Technology Research Center,200237 Shanghai,China;School of Chemical Engineering,Xinjiang University,830046 Urumqi,China;Hydrogen Energy Manufacturing Department of Sinopec Zhenhai Refining and Chemical Company,315207 Ningbo,China)
机构地区:[1]华东理工大学资源与环境工程学院,上海煤气化工程技术研究中心,上海200237 [2]新疆大学化工学院,乌鲁木齐830046 [3]中国石化镇海炼化分公司氢能制造部,浙江宁波315207
出 处:《煤炭转化》2024年第3期103-112,共10页Coal Conversion
基 金:国家重点研发计划项目(2022YFB4101504);新疆维吾尔自治区自然科学基金重点项目(2023D01D02);上海市2021年科技创新行动计划项目(21DZ1209003).
摘 要:应用气化技术将脱油沥青(DOA)转化为合成气是一种环保、高效提升脱油沥青附加值的方法。但脱油沥青气化反应活性较低且气化炭黑生成量大,而生物质中的碱金属元素可以有效催化化石燃料的气化反应,故选用稻草秸秆(RS)与脱油沥青共气化以提升脱油沥青的气化反应速率。采用常压热重分析仪(TGA)考察了DOA和RS在不同掺混比(m_(DOA):m_(RS)分别为9:1,8:2,7:3,1:1,3:7)下共气化的反应特性,并与DOA单独气化的反应特性进行了对比。采用SEM-EDS对共气化产物进行微观形貌和元素分布表征,选择Coats-Redfern法配合Malek最概然机理函数计算共气化动力学相关参数及动力学方程。结果表明:RS主要通过灰分中含有的钾元素催化气化反应,共气化过程中钾由RS转移到DOA表面,在DOA表面通过扩张孔隙形成了新的孔隙,增加了气化反应活性位点;当DOA与RS的掺混比为3:7时,共气化的协同作用最明显,与DOA单独气化相比,活化能降低约94.7 kJ/mol。Using gasification technology to convert the deoiled asphalt into synthesis gas is an environmentally friendly and efficient method to enhance its added value.However,the gasification reaction activity of deoiled asphalt is low,and the amount of carbon black generated during gasification is large.The alkali metal elements in biomass can effectively catalyze the gasification reaction of fossil fuels.Therefore,co-gasification of straw(RS)and deoiled asphalt was selected to improve its gasification reaction rate.An atmospheric thermogravimetric analyzer(TGA)was employed to investigate the co-gasification reaction characteristics of DOA and RS at different mixing ratios(m_(DOA):m_(RS)is 9:1,8:2,7:3,1:1,3:7 respectively).The results were then compared with those obtained when only DOA was used.Scanning electron microscopy with energy-dispersive X-ray spectroscopy(SEM-EDS)was used to characterize the microstructure and elemental distribution of co-gasification products,and the Coats-Redfern method was selected in conjunction with Malek’s most probable mechanism function to calculate the co-gasification kinetic parameters and kinetic equations.The results show that RS mainly catalyzes gasification reactions through potassium elements in the ash.During co-gasification,potassium is transferred from_(RS)to the surface of DOA,and the gasification reaction active sites are increased on the surface of DOA by expanding pores and forming new pores;The synergistic effect of co-gasification is most significant when the mixing ratio of DOA and RS is 3:7,and the activation energy is reduced by approximately 94.7 kJ/mol compared to DOA gasification alone.
分 类 号:TQ534[化学工程—煤化学工程]
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