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作 者:贾兆华 毛伟[1,2] 白彦波 李晨[1,2] 吕剑 JIA Zhao-hua;MAO Wei;BAI Yan-bo;LI Chen;LV Jian(Xi'an Modem Chemistry Research Institute, Xi'an 710065, China;State Key Laboratory for Efficient Development and Utilization of Fluorine & Nitrogen Chemicals, Xi'an 710065, China)
机构地区:[1]西安近代化学研究所,陕西西安710065 [2]氟氮化工资源高效开发与利用国家重点实验室,陕西西安710065
出 处:《现代化工》2018年第4期87-90,共4页Modern Chemical Industry
基 金:国家自然科学基金项目(21327011;21503610)
摘 要:利用多元醇氟化法制备了氟化铝、氟化镁及镁铝复合型氟化物等催化剂,并对所制催化剂在1,1,1,3,3-五氟丙烷(HFC-245fa)气相脱氟化氢制备1,3,3,3-四氟丙烯(HFO-1234ze)反应中的催化性能进行了研究。结果表明,单一氟化镁催化剂活性较低,HFC-245fa转化率仅为7.8%;以摩尔分数为9%Al/MgF_2作为催化HFC-245fa脱氟化氢反应催化剂,在反应温度为280℃,接触时间为25 s,催化剂用量为5 m L时,HFC-245fa的转化率、HFO-1234ze的选择性分别达到53%和100%,与单一组分氟化铝催化性能相当,且运行200 h后保持96%的初始活性。Gas-phase catalytic dehydrofluorination of 1,1,1,3,3-pentafluoropropane( HFC-245 fa) to prepare 1,3,3,3-tetrafluoropropylene( HFO-1234 ze) is investigated over a series of magnesium fluoride,aluminum fluoride and magnesium-aluminum fluoride catalysts that are prepared by polyols mediated fluorination method. The results show that the conversion of HFC-245 fa is only 7. 9% over single magnesium fluoride catalyst. Higher conversion of HFC-245 fa( 53%) and higher selectivity of HFO-1234 ze( 100%) are achieved over 9 mol. % Al/MgF2 catalyst when the dosage of catalyst is 5 m L,the reaction temperature is 280℃ and the contact time is 25 s. The catalytic performance is same as single aluminum fluoride catalyst.The catalyst can still retain 96% of initial activity after it has been used for 200 hours.
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