Method for preparing benzene toluene xylene (BTX) by aromatizing glycerinum
A technology for light aromatic hydrocarbons and aromatization, which is applied in the production of hydrocarbons from oxygen-containing organic compounds and the production of bulk chemicals. The effect of smooth development, changing the dependence of petrochemical raw materials, and simple process flow
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Embodiment 1
[0019] 1) Glycerin is mixed with water, methanol, ethanol, isopropanol and isobutanol at a ratio of 20% of the glycerin mass concentration, heated and vaporized at 290°C, and then pumped into a fixed tank filled with hydrogen-type ZSM-5 molecular sieve catalyst. Bed reactor, operated under normal pressure, at a reaction temperature of 400°C and a mass space velocity of 0.96h -1 The reaction is carried out under certain conditions, and it is converted into aromatic hydrocarbon-based products through catalytic conversion;
[0020] 2) The reaction product is condensed and separated to obtain a liquid phase product and a gas phase product, and the liquid phase product is separated by rectification to obtain light aromatics (BTX) and non-aromatics, and the gas phase product is returned to the reactor to continue the reaction.
[0021] The reaction results are compared in Table 1.
Embodiment 2
[0023] 1) Mix glycerin and isopropanol at a ratio of 25% glycerin mass concentration, heat and vaporize at 290°C, and pump them into the In a fixed bed reactor with 22 molecular sieve catalysts, operate under normal pressure, at a reaction temperature of 400°C and a mass space velocity of 0.96h -1 The reaction is carried out under certain conditions, and it is converted into aromatic hydrocarbon-based products through catalytic conversion;
[0024] 2) The reaction product is condensed and separated to obtain a liquid phase product and a gas phase product, and the liquid phase product is separated by rectification to obtain light aromatics (BTX) and non-aromatics, and the gas phase product is returned to the reactor to continue the reaction.
[0025] The reaction results are compared in Table 2.
Embodiment 3
[0027] 1) Glycerin and isobutanol are mixed according to the ratio of glycerol mass concentration of 25%, heated and vaporized at 290°C, and then pumped into fixed-bed reactors filled with MCM-41 molecular sieve catalysts, operated under normal pressure, at The reaction temperatures are 350°C, 400°C, and 450°C respectively, and the mass space velocity is 0.96h -1 The reaction is carried out under certain conditions, and it is converted into aromatic hydrocarbon-based products through catalytic conversion;
[0028] 2) The reaction product is condensed and separated to obtain a liquid phase product and a gas phase product, and the liquid phase product is separated by rectification to obtain light aromatics (BTX) and non-aromatics, and the gas phase product is returned to the reactor to continue the reaction.
[0029] The reaction results are compared in Table 3.
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