Hydrodesulfurization-heavy oil catalytic cracking combination process of residue oil of high-sulfur crude oil
A technology of hydrodesulfurization and heavy oil catalysis, which is applied in hydroprocessing process, petroleum industry, molecular sieve catalyst, etc. It can solve the problems of poor desulfurization effect and rapid catalyst deactivation
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Embodiment 1
[0044] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ SAPO-5, Co 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.
[0045] 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 50mm, the catalyst bed is set to 3 layers, the temperature of the catalyst bed is measured by a UGU808 temperature control meter, and the raw material is from Beijing The double-plunger micropump manufactured by the satellite manufacturing plant is continuously transported. The hydrogen is supplied by a high-pressure gas cylinder and the flow rate is controlled by a Beijing Qixing Huachuang D07-11A / ZM gas mass flow meter. The hydrogenation cataly...
Embodiment 2
[0050] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ SAPO-5, Co 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.
[0051] All the other conditions are the same as in Example 1.
[0052] The final product was tested and the total sulfur content was reduced to 3ppm with no change in catalyst bed pressure drop.
Embodiment 3
[0077] The catalyst contains catalyst promoter TiO 2 , CeO 2 , V 2 o 5 and NbOPO 4 , its content is respectively 1%, 1.5%, 1% and 3%, all the other are identical with embodiment 1.
[0078] The final product was tested, and after 3 months of use, the pressure drop of the catalyst bed did not change, which was 14% lower than the pressure drop of the catalyst bed in Example 1 for the same use time.
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