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- W2388649849 abstract "The utilization status of cracking C9 was summarized.With Ni-Cu as catalyst,cracking C9 was catalytically hydrogenated in the fixed bed reactor by using two-order deep hydrogenation process.The effects of pressure,temperature and space velocity on the hydrogenation of cracking C9 were investigated,and the process conditions were optimized,which provides a basis for further scale-up study.The experimental result shows that the conversion of unsaturated components is over 90% in the conditions of reaction pressure 5.0 MPa,reaction temperature 150 ℃,and space velocity 0.75 h-1,and the final conversion reaches 98% around when taking the first hydrogenation product as raw material,carrying on the secondary hydrogenation in the optimal conditions." @default.
- W2388649849 created "2016-06-24" @default.
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- W2388649849 date "2011-01-01" @default.
- W2388649849 modified "2023-09-24" @default.
- W2388649849 title "Optimization of catalytic hydrogenation process of cracking C_9" @default.
- W2388649849 hasPublicationYear "2011" @default.
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