Stolle Achim, Schmidt Robert, Jacob Katharina
Institute for Technical Chemistry and Environmental Chemistry (ITUC), Friedrich-Schiller University Jena, Lessingstr. 12, D-07743 Jena, Germany.
Faraday Discuss. 2014;170:267-86. doi: 10.1039/c3fd00144j.
The scale-up of the Knoevenagel-condensation between vanillin and barbituric acid carried out in planetary ball mills is investigated from an engineering perspective. Generally, the reaction proceeded in the solid state without intermediate melting and afforded selectively only one product. The reaction has been used as a model to analyze the influence and relationship of different parameters related to operation in planetary ball mills. From the viewpoint of technological parameters the milling ball diameter, dMB, the filling degree with respect to the milling balls' packing, ΦMB,packing, and the filling degree of the substrates with respect to the void volume of the milling balls' packing, ΦGS, have been investigated at different reaction scales. It was found that milling balls with small dMB lead to higher yields within shorter reaction time, treaction, or lower rotation frequency, rpm. Thus, the lower limit is set considering the technology which is available for the separation of the milling balls from the product after the reaction. Regarding ΦMB,packing, results indicate that the optimal value is roughly 50% of the total milling beakers' volume, VB,total, independent of the reaction scale or reaction conditions. Thus, 30% of VB,total are taken by the milling balls. Increase of the initial batch sizes changes ΦGS significantly. However, within the investigated parameter range no negative influence on the yield was observed. Up to 50% of VB,total can be taken over by the substrates in addition to 30% for the total milling ball volume. Scale-up factors of 15 and 11 were realized considering the amount of substrates and the reactor volume, respectively. Beside technological parameters, variables which influence the process itself, treaction and rpm, were investigated also. Variation of those allowed to fine-tune the reaction conditions in order to maximize the yield and minimize the energy intensity.
从工程学角度研究了在行星式球磨机中进行的香草醛与巴比妥酸之间的克诺文纳格尔缩合反应的放大过程。一般来说,该反应在固态下进行,没有中间熔融过程,并且仅选择性地生成一种产物。该反应已被用作模型,以分析与行星式球磨机操作相关的不同参数的影响和关系。从工艺参数的角度来看,研究了磨球直径dMB、相对于磨球填充的填充度ΦMB,packing以及底物相对于磨球填充空隙体积的填充度ΦGS在不同反应规模下的情况。发现dMB较小的磨球在较短的反应时间treaction或较低的旋转频率rpm下能获得更高的产率。因此,下限是根据反应后从产物中分离磨球的可用技术来设定的。关于ΦMB,packing,结果表明最佳值大致为总研磨烧杯体积VB,total的50%,与反应规模或反应条件无关。因此,磨球占VB,total的30%。初始批量的增加会显著改变ΦGS。然而,在所研究的参数范围内,未观察到对产率有负面影响。除了磨球总体积的30%外,底物最多可占VB,total的50%。分别考虑底物量和反应器体积,实现了15倍和11倍的放大因子。除了工艺参数外,还研究了影响过程本身的变量treaction和rpm。对这些变量的变化进行调整可以微调反应条件,以实现产率最大化和能量强度最小化。