Hydrofining catalyst
A hydrofining and catalyst technology, applied in molecular sieve catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of easy saturation of olefins, high operating costs, and large equipment investment
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Embodiment 1
[0040] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ For KIT-1, the doping amount of Co2+ in KIT-1 is controlled at 0.65% of the mass of the carrier. 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.
[0041] 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 b...
Embodiment 2
[0046] The catalyst is prepared by impregnation method, the carrier is KIT-1 doped with Co2+, and the doping amount of Co2+ 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.
[0047] All the other conditions are the same as in Example 1.
[0048] The final product was tested and its research octane number was still 94.0, while the total sulfur content was reduced to 2 ppm.
Embodiment 3
[0073] The catalyst contains catalytic promoter Cr 2 o 3 , ZrO 2 , CeO 2 , V 2 o 5 and NbOPO 4 , its content is respectively 1%, 1.5%, 2%, 1% and 3%, all the other are identical with embodiment 1.
[0074] The final product was tested, and after it was used for 3 months, the pressure drop of the catalyst bed did not change, which was 15.3% lower than the pressure drop of the catalyst bed in Example 1 for the same use time.
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