Method for preparing aromatic hydrocarbons by aromatization of alcohol compounds
An aromatization and compound technology, applied in the field of aromatization of alcohol compounds to produce aromatics
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Embodiment 1
[0020] Weigh 5 grams of WO that has been dried at 120°C to remove water for 12 hours 3 / ZrO 2 Catalyst, the share ratio of metal oxide is 3 / 97, charged into the fixed bed reactor. The reaction substrate is 1-butanol, and the weight space velocity is 0.5 hours -1 , hydrogen pressure 1.0MPa, flow rate 20ml min -1 , temperature 450°C. After the reaction, the qualitative analysis of the reaction results was carried out by mass spectrometry, and the quantitative analysis of the reaction results was carried out by chromatography. The conversion rate of the reaction substrate was 97%, and the selectivity of BTX was 88%.
Embodiment 2
[0022] Weigh 5 grams of WO that has been dried at 120°C to remove water for 12 hours 3 / ZrO 2 Catalyst, the share ratio of metal oxide is 5 / 95, charged into the fixed bed reactor. The reaction substrate is 2-butanol, and the weight space velocity is 1.0 hours -1 , hydrogen pressure 1.0MPa, flow 50ml min -1 , temperature 400°C. After the reaction, the qualitative analysis of the reaction results was carried out by mass spectrometry, and the quantitative analysis of the reaction results was carried out by chromatography. The reaction substrate conversion rate is 90%, and the selectivity of BTX is 93%.
Embodiment 3
[0024] Liquid-phase reforming of glucose to prepare amyl alcohol: 5 grams of PtRe / C catalyst prepared by impregnation method was loaded in a fixed-bed reactor, the metal content in the catalyst was 5%, and the ratio of Pt and Re was 50:50. Raise the temperature of the reactor, keep it at 350°C for 2 hours in a hydrogen atmosphere, then cool down to 210°C, and keep the weight space velocity in a nitrogen atmosphere for 1h -1 Add 40% concentration of glucose aqueous solution under the conditions of the liquid phase reforming reaction. After the raw material passes through the catalyst bed, the product flow is cooled and collected, and the oil phase in the upper layer is analyzed and characterized to identify the main product as 2-pentanol. The reaction conversion rate was 99%, and the selectivity of pentanol was 85%.
[0025] Weigh 5 grams of WO that has been dried at 120°C to remove water for 12 hours 3 / ZrO 2 The catalyst, the share ratio of metal oxide is 20 / 80, is loaded ...
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