Biodiesel hydrogenation and deoxygenation process
A hydrodeoxygenation and biodiesel technology, applied in the petroleum industry, processing hydrocarbon oil, refining hydrocarbon oil, etc., can solve the problems of biodiesel molecular structure unchanged, engine damage, pipeline blockage, etc.
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Embodiment 1
[0039] 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.
[0040] 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 bat...
Embodiment 2
[0045] 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.
[0046] All the other conditions are the same as in Example 1.
[0047] After testing the final product, its deoxidation rate reached 99.85%. After 500 hours of continuous operation of the device, the deoxidation rate still reached 99.5%.
Embodiment 3
[0072] 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.
[0073] The final product was tested, and after 3 months of use, the pressure drop of the catalyst bed did not change, which was 17% lower than the pressure drop of the catalyst bed in Example 1 for the same use time.
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