Hydrogenation regeneration process for waste lubricating oil
A technology for hydrogenation regeneration and waste lubricating oil, which is applied in the fields of hydrotreating process, petroleum industry, lubricating composition, etc. It can solve the problems of limited depth of catalyst desulfurization and denitrification, and the inability to reduce the total sulfur content to below 10ppm or even 5ppm.
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Embodiment 1
[0041] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ MCM-41, Co. 2+ The doping amount in MCM-41 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.
[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 is set to 3 layers, the temperature of the catalyst bed is measured by a UGU808 temperature control meter, and the raw material is used for lubrication. The oil is continuously transported by a double-plunger micropump manufactured by Beijing Satellite Manufacturing Plant, 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 ...
Embodiment 2
[0049] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ MCM-41, Co. 2+ The doping amount in MCM-41 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.
[0050] All the other conditions are the same as in Example 1.
[0051] The final product was tested and the total sulfur content was reduced to 3 ppm and the total basic nitrogen content was reduced to 9 ppm.
Embodiment 3
[0076] 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.
[0077] The final product was tested, and after 3 months of use, the pressure drop of the catalyst bed did not change, which was 16% lower than the pressure drop of the catalyst bed in Example 1 for the same use time.
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