Hydrogenation and deoxygenation process of biodiesel
A hydrodeoxygenation and biodiesel technology, applied in the fields of biofuels, petroleum industry, biological raw materials, etc., can solve the problems of deterioration, the molecular structure of biodiesel has not changed, and the pipeline is blocked.
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Embodiment 1
[0045] 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.
[0046] 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 bath for gas-liquid separation.
[004...
Embodiment 2
[0051] 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.
[0052] All the other conditions are the same as in Example 1.
[0053] 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 99.3%.
Embodiment 3
[0081] The catalyst contains catalytic promoter Cr 2 o 3 , ZrO 2 , CeO 2 , V 2 o 5 and NbOPO 4 , its content is respectively 1%, 1.5%, 2%, 1% and 3%, all the other are identical with embodiment 1.
[0082] The final product was tested, and after 3 months of use, the pressure drop of the catalyst bed did not change, which was 16.9% lower than the pressure drop of the catalyst bed in Example 1 for the same use time.
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