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机构地区:[1]陕西榆林能源集团有限公司,陕西榆林719000 [2]西北大学化工学院,陕西西安710069
出 处:《工业催化》2016年第8期72-77,共6页Industrial Catalysis
基 金:国家自然科学基金青年基金(21206136);陕西省科技统筹创新工程计划项目(2014KTCL01-09);教育部博士点新教师基金(20126101120013);陕西省教育厅产业化培育项目(14JF026;15JF031);陕西省青年科技新星项目(2016KJXX-32);西北大学"优秀青年学术骨干支持计划"
摘 要:使用工业催化剂Ni-Mo/Al2O3,在固定床反应器上对360℃前馏分煤焦油进行加氢处理实验,研究反应温度(320~400)℃对煤焦油加氢产物分布及化学组成的影响。实验过程中,反应条件设定为:压力10 MPa,空速0.5 h^(-1),氢油体积比1 600∶1。使用GC-MS分析煤焦油加氢前后的化学组成变化,结果表明,升高反应温度对煤焦油中芳烃类物质的加氢饱和反应不利,但有利于杂原子的脱除以及油品的轻质化。煤焦油中最主要的两类化合物是烷基萘与酚类物质,加氢过程中主要转化为二环癸烷与烷基环己烷。The hydrotreatment of low temperature coal tar was carried out in a fixed bed reactor by using Ni-Mo/A1203 catalyst. The effects of reaction temperature (320 -400) ℃ on distribution and chemical composition of hydrogenated products of coal tar were investigated. The reaction condition during the ex- perimental process was determined as follows: pressure 10 MPa, space velocity 0.5 h- 1, volume ratio of hydrogen to oil 1 600: 1. The feedstock and the product were analyzed by GC-MS. The results showed that increasing reaction temperature was beneficial to the hetero atom removal and oil upgrading but had a negative impact on hydrogenation of aromatics in coal tar. Two kinds of the main compounds in coal tar were naphthalene and phenol, which were transformed into decahydronaphthalene and eyclohexane respec- tively during hydrogenation.
关 键 词:精细化学工程 煤焦油 GC-MS Ni-Mo/Al2O3催化剂 汽油 柴油
分 类 号:TQ522.64[化学工程—煤化学工程]
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