Fluid catalytic cracking (FCC) gasoline hydrogen desulfurization process
A hydrodesulfurization and desulfurization process technology, which is applied in the petroleum industry, processing hydrocarbon oil, refining hydrocarbon oil, etc., can solve the problems of high operating cost, lower gasoline octane number, and easy saturation of olefins.
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Embodiment 1
[0035] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ KIT-1, Co. 2+ The doping amount in KIT-1 is controlled at 0.65% of the carrier mass. The active component molybdenum nitride MO 2 N, tungsten nitride W 2 N, molybdenum carbide Mo 2 The total content of C and tungsten carbide WC is 10% of the mass of the carrier, and their molar ratio is 1:0.4:0.3:0.8.
[0036] The catalyst is loaded into a fixed bed reactor, the reaction tube of the reactor is made of stainless steel with an inner diameter of 50 mm, the catalyst bed temperature is measured with a UGU808 temperature control meter, and the raw material light oil is manufactured by Beijing Satellite Manufacturing Plant The double-plunger micropump continuously transports the hydrogen gas from a high-pressure cylinder and controls the flow rate with a Beijing Qixing Huachuang D07-11A / ZM gas mass flow meter. The catalyst loading is 2kg. The reacted product is cooled in a water bath for gas...
Embodiment 2
[0041] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ KIT-1, Co. 2+ The doping amount in KIT-1 is controlled at 0.7% of the carrier mass. The active component molybdenum nitride MO 2 N, tungsten nitride W 2 N, molybdenum carbide Mo 2 The total content of C and tungsten carbide WC is 10% of the mass of the carrier, and the molar ratio is 1:0.6:0.45):1.2.
[0042] All the other conditions are the same as in Example 1.
[0043] The final product was tested and its research octane number was still 94.1, while the total sulfur content was reduced to 4ppm.
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