“Development and commercial application of the packaged technology for toluene disproportionation and transalkylation” jointly undertaken by SINOPEC Shanghai Petrochemical Research Institute and Zhenhai Refining and...“Development and commercial application of the packaged technology for toluene disproportionation and transalkylation” jointly undertaken by SINOPEC Shanghai Petrochemical Research Institute and Zhenhai Refining and Chemical Company had recently passed the technical appraisal organized by SINOPEC Science and Technology Development Division.展开更多
This paper refers to the results of study and development of benzene and polyethylbenzene transalkylation catalyst (type AEB-1) for synthesis of ethylbenzene. The effect of reaction conditions on the reaction performa...This paper refers to the results of study and development of benzene and polyethylbenzene transalkylation catalyst (type AEB-1) for synthesis of ethylbenzene. The effect of reaction conditions on the reaction performance of the catalyst was investigated in the pressurized microreactor CDS-900. A transalkylation catalyst with high activity, good selectivity and stability was developed following a 2000-hour test on the activity and stability of the catalyst. The preparation of this catalyst was implemented in pilot scale and this catalyst was tested for activity and stability in a 150 t/a pilot unit for production of ethylbenzene. The test results have shown that this transalkylation catalyst has excellent activity, selectivity and stability. The operation of pilot test unit ran smoothly and the process scheme is viable.展开更多
Isopropylation of naphthalene with propene resulted in a variety of isomers having different alkylation levels.The most important isomer is 2,6-DIPN,which is the precursor of important monomer 2,6-naphthalene di- carb...Isopropylation of naphthalene with propene resulted in a variety of isomers having different alkylation levels.The most important isomer is 2,6-DIPN,which is the precursor of important monomer 2,6-naphthalene di- carboxylic acid used for making liquid crystal polymers.In order to increase the yield of 2,6-DIPN,the intermo- lecular transalkylation with naphthalene was applied to the mixture of other DIPNs and PIPN to obtain MIPN en- riched product,which underwent isopropylation with propene to produce 2,6-DIPN in a higher yield.The experi- mental study showed that the preferable conditions for transalkylation were reaction temperature of 325℃,the mo- lar ratio of isopropyl group to naphthyl group(IP/N)of 0.8︰1—0.9︰1,reaction time of 4h and 5%of amorphous silica-alumina by mass.The conversions of DIPN and PIPN in its mixture were 62%—69%and 87%—88%respec- tively and the yield of MIPN was greater than 40%.The mixture of MIPN enriched product and recovered MIPN from rectification was subject to isopropylation with propene at 275℃over a shape-selective catalyst to produce 2,6-DIPN in a yield up to 38%.A recycled process of recovered components was established,through one cycle the yield of 2,6-DIPN based on naphthalene may be 2.8 times higher than before,and the utilization ratio of raw naph- thalene was increased by 46%.展开更多
文摘“Development and commercial application of the packaged technology for toluene disproportionation and transalkylation” jointly undertaken by SINOPEC Shanghai Petrochemical Research Institute and Zhenhai Refining and Chemical Company had recently passed the technical appraisal organized by SINOPEC Science and Technology Development Division.
文摘This paper refers to the results of study and development of benzene and polyethylbenzene transalkylation catalyst (type AEB-1) for synthesis of ethylbenzene. The effect of reaction conditions on the reaction performance of the catalyst was investigated in the pressurized microreactor CDS-900. A transalkylation catalyst with high activity, good selectivity and stability was developed following a 2000-hour test on the activity and stability of the catalyst. The preparation of this catalyst was implemented in pilot scale and this catalyst was tested for activity and stability in a 150 t/a pilot unit for production of ethylbenzene. The test results have shown that this transalkylation catalyst has excellent activity, selectivity and stability. The operation of pilot test unit ran smoothly and the process scheme is viable.
基金Supported by the Northeast Rejuvenation Strategy Foundation of Anshan City,China(032042).
文摘Isopropylation of naphthalene with propene resulted in a variety of isomers having different alkylation levels.The most important isomer is 2,6-DIPN,which is the precursor of important monomer 2,6-naphthalene di- carboxylic acid used for making liquid crystal polymers.In order to increase the yield of 2,6-DIPN,the intermo- lecular transalkylation with naphthalene was applied to the mixture of other DIPNs and PIPN to obtain MIPN en- riched product,which underwent isopropylation with propene to produce 2,6-DIPN in a higher yield.The experi- mental study showed that the preferable conditions for transalkylation were reaction temperature of 325℃,the mo- lar ratio of isopropyl group to naphthyl group(IP/N)of 0.8︰1—0.9︰1,reaction time of 4h and 5%of amorphous silica-alumina by mass.The conversions of DIPN and PIPN in its mixture were 62%—69%and 87%—88%respec- tively and the yield of MIPN was greater than 40%.The mixture of MIPN enriched product and recovered MIPN from rectification was subject to isopropylation with propene at 275℃over a shape-selective catalyst to produce 2,6-DIPN in a yield up to 38%.A recycled process of recovered components was established,through one cycle the yield of 2,6-DIPN based on naphthalene may be 2.8 times higher than before,and the utilization ratio of raw naph- thalene was increased by 46%.
