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作 者:袁秉宇[1] 曾逸凡[1] 袁英[1] 徐梦舟[1] 崔玉宝[1] 吴倩[1]
机构地区:[1]同济大学化学系,上海200092
出 处:《广东化工》2012年第15期206-207,共2页Guangdong Chemical Industry
基 金:同济大学大学生创新实践训练计划
摘 要:采用酸性较强的HY分子筛进行废塑料垃圾油催化裂化反应,通过正交实验设计,考察了原料液浓度、反应温度、反应空时等反应条件对废塑料垃圾油轻质化产物分布的影响。实验结果表明,较优的操条件为反应温度450℃,原料液配比浓度为30 wt%,反应空时为0.38g(cat).g(oil)-1.h。Cracking reactions of the waste plastic oil is catalyzed with the strong acid HY zeolite catalyze, design by orthogonal experimental, we have studied the influence of operating conditions on the distribution of products with different pyrolytic oil concentration, reaction temperature and time factor. The experimental results showed that the optimum operating conditions were as follow: the reaction temperature was 450 ℃, the pyrolytic oil concentration was 30 wt%, and the time facotr was 0.38g(cat)·g(oil)^-1·h.
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