Journal of Liaoning Petrochemical University
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Preparation and Evaluation of Catalyst for Non -Hydrogen Dewaxing
SONG Yi,LIU Jie, ZAI Yu -chun
Abstract418)      PDF (182KB)(288)      
    A new catalyst for non -hydrogen - dewaxing was prepared by hydrothermal method , using ZSM -5 as the principal component and then adding self -made BCM zeolites.Its catalytic performance was evaluated using catalytic cracked diesel fuel and AGO NO .3 as feed stock .The results show that catalyst has obviousde -waxing effect.The pour point can be reduced by 62 ℃, and higher liquor yield(>95%)were obtained at the temperature of 340 ℃ and space velocity of 1 h -1 .The diesel oil produced using the catalyst shows higher cetane number index , lower content of sulfur and nitrogen, and lower pour point , can meet the quality requirements of product blending .
2007, 27 (4): 17-20.
Non-Hydrogen-Dewaxing Catalyst for Hydrocracked Tail Oil
ZHANG Ai-min, LIU jie, SONG Yi, LI Dong-sheng, ZHAI Yu-chun
Abstract379)      PDF (141KB)(215)      
The catalytic performance of self- developed non-hydrogen-dewaxing catalyst (FC-DB) was evaluated, and the hydrocracking tail oil was used as feed stock. The influence of reaction temperature and space velocity on the yield and pouring point of base oil was investigated. The relationships between yield, pouring point and operation conditions were determined by polynary quadratic regression, and the optimum operation conditions were determined by non-linear programming. The reaction temperature is 400 ℃ and space velocity is 1.2 h-1. At this time, the yield and pouring point of base oil respectively are 92.53% and -20 ℃, approximately dropping 53 ℃. The qualify of base oil obtained under above optimum operation conditions was analyzed, and the base oil can be used as premium lubricant base oil because of its high viscosity index, low pouring point, acidity and residue carbon.
2007, 27 (3): 21-24.