Exploratory Study for the Upgrading of Transport Properties of Heavy Oil by Slurry-Phase Hydrocracking
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文摘
The partial hydrocracking of a crude oil of 13掳 American Petroleum Institute (API) gravity and viscosity of 6100 cSt at 37.8 掳C was carried out in a batch reactor using a dispersed catalyst. The operating conditions were varied in the following ranges: hydrogen pressure of 40鈥?00 kg/cm2, temperature of 360鈥?00 掳C, and reaction time of 3鈥? h. Molybdenum trioxide of analytical grade was employed as a dispersed catalyst, and its concentration was modified from 0 to 2 wt %. The obtained results showed that the most favorable reaction conditions to obtain an upgraded crude oil with the required specifications for transportation by pipeline are 40 kg/cm2, 380 掳C, 4 h of reaction, and a catalyst concentration of 0.75 wt %. At these operation conditions, no coke formation was observed.

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