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Investigation of Propene Oligomerization Catalyzed by Phosphotungstic Acid Catalysts

Investigation of Propene Oligomerization Catalyzed by Phosphotungstic Acid Catalysts
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摘要 In this paper,the propene oligomerization reaction catalyzed by phosphotungstic acid supported on two kinds of silica gel was studied,it had been found out that the conversion of propene catalyzed by the type A silica gel-phosphotungstic acid catalyst was 3.38m%,while the conversion of propene catalyzed by the type B silica gel-phosphotungstic acid catalyst was 90.1m% with a nonene selectivity of 42.33m%,and a dodecene selectivity of 31.79m%.The influence of reaction temperature,pressure and liquid hourly space velocity(LHSV) on the reaction catalyzed by the type B silica gelphosphotungstic acid catalyst was investigated.It had been verified that when the reaction temperature increased from 170℃ to 190℃,the conversion of propene increased while the selectivity of nonene and dodecene decreased;when the reaction pressure increased from 3.5 MPa to 4.5 MPa,the conversion of propene increased also,and the selectivity of nonene and dodecene changed very little.The conversion of propene at a space velocity of between 0.5h-1 and 1.0h-1 was higher than that achieved at 2.0h-1,but the selectivity of nonene and dodecene did not show regular fluctuations.An optimum conversion of propene(91.05m%) and an optimum selectivity of nonene and dodecene(89.51m%) could be achieved at a reaction temperature of 170℃,a reaction pressure of 4.5MPa,and a LHSV of 1.0h-1.The experiments on catalyst life showed that the activity of the type B silica gel-phosphotungstic acid catalyst could be only maintained in 25 hours,and the reason was explained also. In this paper, the propene oligomerization reaction catalyzed by phosphotungstic acid supported on two kinds of silica gel was studied, it had been found out that the conversion of propene catalyzed by the type A silica gel-phosphotung- stic acid catalyst was 3.38 m%, while the conversion of propene catalyzed by the type B silica gel-phosphotungstic acid catalyst was 90.1 m% with a nonene selectivity of 42.33 m%, and a dodecene selectivity of 31.79 m%. The influence of reaction temperature, pressure and liquid hourly space velocity (LHSV) on the reaction catalyzed by the type B silica gel- phosphotungstic acid catalyst was investigated. It had been verified that when the reaction temperature increased from 170 ~C to 190 ~C, the conversion of propene increased while the selectivity of nonene and dodecene decreased; when the re- action pressure increased from 3.5 MPa to 4.5 MPa, the conversion of propene increased also, and the selectivity of nonene and dodecene changed very little. The conversion of propene at a space velocity of between 0.5 h-1 and 1.0 h-~ was higher than that achieved at 2.0 h-~, but the selectivity of nonene and dodecene did not show regular fluctuations. An optimum conversion of propene (91.05 m%) and an optimum selectivity of nonene and dodecene (89.51 m%) could be achieved at a reaction temperature of 170 ~C, a reaction pressure of 4.5MPa, and a LHSV of 1.0 fit. The experiments on catalyst life showed that the activity of the type B silica gel-phosphotungstic acid catalyst could be only maintained in 25 hours, and the reason was explained also.
出处 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2012年第3期10-16,共7页 中国炼油与石油化工(英文版)
关键词 磷钨酸催化剂 丙烯齐聚 十二碳烯 硅胶负载 反应温度 反应压力 转化率 催化剂寿命 phosphotungstic acid, support, propene oligomerization, conversion, selectivity, nonene, dodecene
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