Biodiesel hydrodeoxygenation process
A hydrodeoxygenation and biodiesel technology, applied in the petroleum industry, processing hydrocarbon oil, refining hydrocarbon oil, etc., can solve problems such as deterioration, biodiesel molecular structure unchanged, and pipeline blockage
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Embodiment 1
[0040] The catalyst is prepared by impregnation method, and the carrier is doped Cu 2+ KIT-1, Cu 2+ The doping amount in KIT-1 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 carrier mass, and the molar ratio is 1:0.4:0.3:0.8.
[0041] The catalyst was filled into a fixed-bed reactor. The reaction tube of the reactor was made of stainless steel with an inner diameter of 50mm. The temperature of the catalyst bed was measured with a UGU808 temperature control meter. The raw material light oil was manufactured by Beijing Satellite Manufacturing Factory. The double plunger micro-pump continuously delivers hydrogen. The hydrogen is supplied from a high-pressure cylinder and the flow rate is controlled by the Beijing Qixing Huachuang D07-11A / ZM gas mass flow meter. The catalyst loading is 2kg. The product after the reaction is cooled i...
Embodiment 2
[0046] The catalyst is prepared by impregnation method, and the carrier is doped Cu 2+ KIT-1, Cu 2+ The amount of doping in KIT-1 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 carrier mass, and the molar ratio is 1:0.6:0.45):1.2.
[0047] The remaining conditions are the same as in Example 1.
[0048] After testing the final product, its deoxygenation rate reached 99.85%, and after 500 hours of continuous operation of the device, the deoxygenation rate still reached 99.0%.
Embodiment 3
[0073] The catalyst contains catalytic promoter TiO 2 , CeO 2 , V 2 O 5 And NbOPO 4 , The contents are 1%, 1.5%, 1% and 3% respectively, and the rest are the same as in Example 1.
[0074] After testing the final product, after 3 months of use, there was no change in the pressure drop of the catalyst bed, which was reduced by 17% compared to the catalyst bed pressure drop of Example 1 for the same use time.
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