A kind of preparation method of bio-based aromatic hydrocarbon
A bio-based, aromatic technology, applied in chemical instruments and methods, production of hydrocarbons and hydrocarbons from oxygen-containing organic compounds, etc., can solve the problems of limited raw materials, only 18% conversion rate of aromatics, and not much biomass, etc. To achieve the effect of reducing dependence, improving methanol conversion rate, and simple reaction operation
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Embodiment 1
[0028] Put 10g of catalyst into a fixed-bed reactor, and pretreat the catalyst by steam method for 12h at normal pressure of 480°C, and the mass space velocity of deionized water is 2h -1 . After processing finishes, pass into nitrogen, control reactor internal pressure to be 0.16MPa, temperature is 480 ℃, remove nitrogen, methanol aqueous solution (methanol mass concentration is 90%) and fatty acid methyl ester are pumped into reactor and fatty acid methyl ester respectively by feed pump. Catalyst contact reaction, feed mass space velocity is 1h -1 , wherein the weight ratio of methanol and fatty acid methyl ester is 1:1. The reaction products were analyzed using the PONA software developed by the Academy of Stone Sciences, and the results are shown in Table 1.
Embodiment 2
[0030] Put 10g of catalyst into a fixed-bed reactor, and pretreat the catalyst by steam method for 12h at normal pressure of 480°C, and the mass space velocity of deionized water is 2h -1 . After the treatment, feed nitrogen, control the pressure in the reactor to be 0.16MPa, and the temperature is 480°C, remove the nitrogen, and respectively pump methanol aqueous solution (methanol mass concentration is 90%) and soybean oil into the reactor to contact with the catalyst through the feed pump Reaction, methanol and soybean oil feed space velocity is 0.5h -1 , wherein the weight ratio of methanol and soybean oil is 1:1. The reaction products were analyzed by PONA software developed by the Academy of Stone Sciences. The results are shown in Table 1.
Embodiment 3
[0032] Put 10g of catalyst into a fixed-bed reactor, and pretreat the catalyst by steam method for 12h at normal pressure of 480°C, and the mass space velocity of deionized water is 2h -1 . After the treatment finishes, feed nitrogen, control the pressure in the reactor to be 0.2MPa, and the temperature is 350°C, remove the nitrogen, and methanol aqueous solution (methanol mass concentration is 90%) and fatty acid methyl ester are pumped into the reactor and Catalyst contact reaction, feed mass space velocity is 1h -1 , wherein the weight ratio of methanol and fatty acid methyl ester is 2:1. The reaction products were analyzed using the PONA software developed by the Academy of Stone Sciences, and the results are shown in Table 1.
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