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首页> 外文期刊>Organic process research & development >Production of p-Cymene from Crude Sulphate Turpentine with Commercial Zeolite Catalyst Using a Continuous Fixed Bed Reactor
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Production of p-Cymene from Crude Sulphate Turpentine with Commercial Zeolite Catalyst Using a Continuous Fixed Bed Reactor

机译:使用连续固定床反应器用商业沸石催化剂从硫酸盐松节油中生产对伞花烃

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摘要

Crude sulphate turpentine (CST), containing alpha-pinene, 3-carene, other terpene isomers, and organic sulphur compounds, was used as feedstock in the production of cymenes with commercial zeolite catalysts. The catalysts used were not sensitive to sulphur, and the desulphurisation step was not needed prior to cymene synthesis. The experiments were performed in a continuous fixed bed reactor. Promising results were obtained after initial optimization at temperatures close to 300 degrees C with faujasite Y zeolite under 5 bar N-2 pressure. Cymenes were produced with 54% yields from model compound alpha-pinene and with 28% yields from CST. The mechanistic route of the reaction can be divided into three steps: (1) ring opening, (2) rearrangement, and (3) dehydrogenation. The final step in the formation of p-cymene can occur via dehydrogenation or disproportion; here the effect of reaction conditions and catalyst plays a crucial role.
机译:含有α-pine烯,3-烯,其他萜烯异构体和有机硫化合物的粗硫酸盐松节油(CST)用作工业沸石催化剂生产苏木精的原料。所用的催化剂对硫不敏感,并且在合成ym茂烯之前不需要脱硫步骤。实验在连续固定床反应器中进行。在八巴石Y沸石,5 bar N-2压力下,在接近300摄氏度的温度下进行初步优化后,获得了可喜的结果。从模型化合物α-pine烯中提取的精氨酸产量为54%,从CST中提取的产量为28%。反应的机理路线可分为三个步骤:(1)开环,(2)重排和(3)脱氢。对伞花烃形成的最后步骤可以通过脱氢或歧化反应进行。在这里,反应条件和催化剂的作用起着至关重要的作用。

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