Aviation kerosene hydrorefining technology
A technology for hydrorefining and aviation kerosene, which is applied in the petroleum industry, refining hydrocarbon oil, processing hydrocarbon oil, etc., and can solve the problems that catalysts and hydrogenation conditions are difficult to apply or cannot be applied.
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Embodiment 1
[0037] The catalyst was prepared by impregnation method, and the carrier was a mixture of MSU-G, SBA-15 and HMS, and the mixing ratio was 1:1.1:0.5. 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.
[0038] 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 with a UGU808 temperature control meter, and the raw material aviation kerosene The double-plunger micropump manufactured by Beijing Satellite Manufacturing Plant is continuously transported. The hydrogen is supplied by a high-pressure cylinder and the flow rate is controlled by a Beijing Qixing Huachuang D07-11A / ZM gas mass flow meter. The catalyst loading is 2kg. The reacted produc...
Embodiment 2
[0043] The catalyst is prepared by the impregnation method, and the carrier is a mixture of MSU-G / SBA-15 complex, MSU-G / HMS and SBA-15 / HMS complex, wherein the ratio of MSU-G, SBA-15 and HMS is the same as in the example 1 is the same. 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.
[0044] All the other conditions are the same as in Example 1.
[0045] The final product was tested and the total sulfur content was reduced to 4 ppm and the total basic nitrogen content was reduced to 5 ppm.
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