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作 者:黄力[1] 纵宇浩 李庆宁[2] 田晓明[2] 孙勇[3]
机构地区:[1]中国大唐集团公司大唐南京环保科技有限责任公司,江苏南京211111 [2]中国石化金陵石化公司质检中心,江苏南京210033 [3]中国石化金陵石化公司烷基苯厂,江苏南京210046
出 处:《石化技术与应用》2016年第3期207-211,共5页Petrochemical Technology & Application
摘 要:分别采用烧炭法和烧炭-氯氧化法对积炭后的Pt-Sn-Na/ZSM-5丙烷脱氢催化剂进行再生(以下分别简称试样1和试样2)。借用X射线衍射法、透射电子显微镜、H2-程序升温还原法、NH3-程序升温脱附法等分析了催化剂物理化学性质,并在固定床反应装置上,考察了催化剂的丙烷脱氢性能。结果表明:试样1的Pt分散度明显下降;氯氧化处理可有效促进烧炭后催化剂Pt的再分散,并且增加了催化剂表面酸性,因此,试样2的丙烷转化率较高,但丙烯选择性较低;此外,由于氯氧化处理中水蒸气的存在,导致催化剂的机械强度下降,以及Pt-Sn合金的生成,因此,试样2经二次再生后,丙烯收率明显降低。Pt- Sn- Na / ZSM- 5 catalyst of carbon deposit for propane dehydrogenation were regenerated by oxilization and oxilization- oxychlorination methods( referred to sample 1 and sample 2,respectively). The physicochemical properties of the catalysts were characterized by X- ray diffraction,transmission electron microscope,H2- temperature programmed reduction method,NH3- temperature programmed stripping method,and so on. The propane dehydrogenation performance of catalyst was investigated in a fixed bed reactor. The results showed that the Pt dispersion of sample 1 declined obviously,while the oxychlorination treatment could effectively improve the redispersion of Pt after the coke burning,and increased the amount of acid of sample2. Therefore,the propane conversion of sample 2 increased and the propene selectivity decreased. Besides,the existence of stream during the oxychlorination treatment led to the decrease of mechanical strength and formation of Pt- Sn alloy. Consequently,the propene yield of sample 2dropped obviously after the second regeneration.
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