Biodiesel hydrodeoxygenation process
A technology of hydrodeoxygenation and biodiesel, which is applied in the fields of biofuel, petroleum industry, biological raw materials, etc., can solve the problems of pipeline blockage, deterioration, and the molecular structure of biodiesel has not changed.
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Embodiment 1
[0039] The catalyst was prepared by impregnation method, and the carrier was doped Cu 2+ MCM-41, Cu 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 50mm, the temperature of the catalyst bed 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 gas 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 ...
Embodiment 2
[0045] The catalyst was prepared by impregnation method, and the carrier was doped Cu 2+ MCM-41, Cu 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 99.1%.
Embodiment 3
[0072] The catalyst contains catalytic promoter Cr 2 o 3 , ZrO 2 , CeO 2 , V 2 o 5 and NbOPO 4 , its content is respectively 2.2%, 1.5%, 2.7%, 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 13% lower than the pressure drop of the catalyst bed in Example 1 for the same use time.
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