摘要
The kinetics of simultaneous transesterification and esterification with a carbon-based solid acid catalyst was studied.Two solid acid catalysts were prepared by the sulfonation of carbonized vegetable oil asphalt and petroleum asphalt.These catalysts were characterized on the basis of elemental analysis,acidity site concentration,the Brunauer-Emmett-Teller（BET）surface area and pore size.The kinetic parameters with the two catalysts were determined,and the reaction system can be described as a pseudo homogeneous catalyzed reaction.All the forward and reverse reactions follow second order kinetics.The calculated concentration values from the kinetic equations are in good agreement with experimental values.
有基于碳的稳固的酸催化剂的同时的 transesterification 和酯化作用的动力学被学习。二稳固的酸催化剂被使碳化的蔬菜油沥青和石油沥青的 sulfonation 准备。这些催化剂根据元素的分析，酸味地点集中， Brunauer-Emmett-Teller (赌注) 表面区域和毛孔尺寸被描绘。有二催化剂的运动参数被决定，并且反应系统能被描述为假同类的催化反应。所有前面、反向的反应跟随第二顺序动力学。从运动方程的计算集中价值在对试验性的价值的好同意。
