Hydrodesulfurization catalyst
A hydrodesulfurization and catalyst technology is applied in the field of hydrodesulfurization catalysts, FCC gasoline hydrodesulfurization catalysts and the reduction of octane number reduction, which can solve the problems of high consumption of hydrogen, easy saturation of olefins, and large equipment investment.
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Embodiment 1
[0041] The catalyst was prepared by impregnation method, and the carrier was doped Cu 2+ SAPO-5, Cu 2+ The doping amount in SAPO-5 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.
[0042] 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 ga...
Embodiment 2
[0047] The catalyst was prepared by impregnation method, and the carrier was doped Cu 2+ SAPO-5, Cu 2+ The doping amount in SAPO-5 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.
[0048] All the other conditions are the same as in Example 1.
[0049] The final product was tested and its research octane number was still 93.9, while the total sulfur content was reduced to 4ppm.
Embodiment 3
[0074] 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%, 2%, 1.5%, 1% and 3%, all the other are identical with embodiment 1.
[0075] 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 14.9% lower than the pressure drop of the catalyst bed in Example 1 for the same use time.
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