Method for preparing diesel hydrocarbons from vegetable fat through catalytic hydrogenation and deoxygenation
A vegetable oil, catalytic hydrogenation technology, applied in the preparation of liquid hydrocarbon mixtures, petroleum industry, biological raw materials, etc., can solve the problems of restrictions, high prices, limited reserves, etc., achieve reduced production costs, low boiling point, and avoid production costs the increased effect of
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Embodiment 1
[0035] Add 0.2g of Mo2C / AC catalyst, 1.0g of sunflower oil and 20mL of n-hexane into a 100mL reactor, fill it with hydrogen, start stirring and heating at an initial hydrogen pressure of 2.5MPa, stop the reaction after 10 hours at 270°C, and wait to cool to After room temperature, the catalyst was separated by filtration to obtain clear and transparent diesel hydrocarbons. Quantitative detection of the product by high-performance liquid chromatography and gas chromatography shows that the conversion rate of the raw material sunflower oil can reach 97%, and the total output of diesel hydrocarbons is 0.61g.
[0036] The product composition is shown in the table below:
[0037]
Embodiment 2
[0039] Add 0.4g of Mo2C / AC catalyst, 2.0g of olive oil and 30mL of n-octane into a 100mL reactor, fill it with hydrogen, start stirring and heating at an initial hydrogen pressure of 4.0MPa, and stop the reaction at 320°C for 6 hours, and wait to cool to After room temperature, the catalyst was separated by filtration to obtain clear and transparent diesel hydrocarbons. Quantitatively detect the product by high performance liquid chromatography and gas chromatography respectively, it can be seen that the conversion rate of the raw material olive oil can reach 100%, and the total output of diesel oil hydrocarbons is 1.44g.
[0040] The product composition is shown in the table below:
[0041]
Embodiment 3
[0043] Add 0.25g of Mo2C / AC catalyst, 1.5g of corn oil and 25mL of n-heptane into a 100mL reactor, fill it with hydrogen, start stirring and heating at an initial hydrogen pressure of 2.5MPa, stop the reaction after 8 hours at 290°C, and wait to cool to After room temperature, the catalyst was separated by filtration to obtain clear and transparent diesel hydrocarbons. Quantitative detection of the product by high-performance liquid chromatography and gas chromatography respectively shows that the conversion rate of raw material corn oil can reach 100%, and the total output of diesel hydrocarbons is 1.00g.
[0044] The product composition is shown in the table below:
[0045]
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