A method for co-refining oil by using FCC oil slurry and coal
A technology for co-refining and oil slurry, which is applied in the petroleum industry, processing hydrocarbon oil, preparation of liquid hydrocarbon mixtures, etc., can solve the problems of difficult industrial production, harsh raw material requirements, increased energy consumption of equipment, etc., and achieve the limit of raw material properties. The effect of low requirements, good product quality and lower cost investment
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Embodiment 1
[0072] Using pure FCC oil slurry as raw material, first mix the oil slurry with catalyst, additives, and co-catalysts, and enter the suspension bed reactor for reaction. Additives are 0-0.75wt%, catalysts are 0-1.6wt%, co-catalysts are 0-1.0wt%, The reaction temperature is 427°C to 462°C. The scale of the device is 150 kg / day, and the process flow is the method of co-refining oil with FCC oil slurry and coal of the present invention.
Embodiment 2
[0074] The raw material is Yulin Daliuta coal + FCC oil slurry. First, the Yulin Daliuta coal is pulverized to obtain coal powder with a particle size of less than 100 μm. After drying, it is mixed with heated oil slurry, catalysts, and additives to prepare oil-coal slurry. The additive for the suspended bed hydrocracking reaction is activated carbon, the catalyst is an iron-based catalyst, the additive is 0-0.75wt%, the catalyst is 0-1.6wt%, the co-catalyst is 0-1.0wt%, the reaction temperature is 445 ° C ~ 470 ° C, the co-catalyst The addition amount is 0.5-1.0wt%, the oil-coal slurry concentration is 35-55wt%, the device scale is 150 kg / day, and the process flow is the method of co-refining oil with FCC oil slurry and coal of the present invention.
Embodiment 3
[0076] Using FCC oil slurry + atmospheric residual oil as the base oil, and the raw coal is cold water well coal. Firstly, the cold water well coal is pulverized to obtain coal powder with a particle size of less than 100 μm. After drying, it is mixed with heated oil slurry, catalyst, and auxiliary The catalyst and additives are evenly mixed to form oil-coal slurry. The additive for the suspension bed hydrocracking reaction is activated carbon, the catalyst is an iron-based catalyst, the additive is 0-0.75wt%, the catalyst is 0-1.6wt%, and the co-catalyst is 0-1.0wt%. The reaction temperature is 445°C-470°C, the concentration of oil-coal slurry is 35-55%wt, the scale of the device is 150 kg / day, and the process flow is the method of co-refining oil with FCC oil slurry and coal of the present invention.
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