催化作用
松节油
化学
产量(工程)
异构化
活化能
反应速率
反应级数
化学反应工程
化学工程
反应速率常数
化学动力学
动力学
有机化学
材料科学
复合材料
物理
量子力学
工程类
作者
Gaodong Yang,Haibo Liu,Zheng Zhou,Zhibing Zhang
标识
DOI:10.1016/j.cej.2011.01.037
摘要
A study of turpentine direct hydration was carried out, using macropore and strong acidic cation exchange resin Amberlyst 15 wet as catalyst. During the hydration process, the isomerization of α-pinene also took place under the catalytic condition. The effects of different parameters such as agitation speed, catalyst type, catalyst loading, mass ratio of the reactants, temperature and the reusability of catalyst on the conversion of turpentine and the yield of α-terpineol were investigated to obtain the optimal reaction conditions in a stirred-tank reactor. Based on these optimized conditions, the experiment was conducted in a new pilot-scale jet reactor to achieve an excellent performance. Kinetics of the direct hydration reaction was also performed in the temperature range 328.15–348.15 K. A pseudohomogeneous (PH) model was used to explain the reaction rate equation and to determine the reaction rate constants and reaction activation energy.
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