水含量对Ca(OH)2与烷基苯磺酸中和反应动力学的影响。

IF 0.1 Q4 ENGINEERING, CHEMICAL
K. Javed, Mahood Saleem, A. Durrani
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引用次数: 0

摘要

在反应开始时加入重量5% ~ 10%的水,催化了Ca(OH)2与烷基苯磺酸(ABS)的中和反应。水分离的运行成本很高,因此水应在反应系统中处于最低水平,以使水分离的运行成本最小化。Â在恒温343 K和不同初始水含量(1.5%、4.4%和8.7%)条件下完成了反应动力学研究,确定了反应动力学参数以及水含量对反应速率、转化率和完全转化所需时间的影响。采用积分法对实验数据进行数据分析,由浓度时间曲线确定速率方程。Ca(OH)2与ABS的中和反应为二级自催化反应,反应速率常数为0.0081 l /mol。最小温度为343 K,初始含水量为1.5%重量%。最高反应速率为0.024 mol/lit。当初始水含量增加时,反应速率也随之提高,当初始水含量分别为4.4和8.7%时,反应速率在160 min和120 min内基本实现完全转化。当反应开始时初始含水量分别为1.5、4.4和8.7%时,反应结束时的含水量分别为5.02、7.86和12%。不需要超过4.4重量%的初始水含量,因为在此之后,反应速率的增加就不显著了。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Impact of water content on kinetics of Ca(OH)2 and alkyl benzene sulphonic acid neutralization reaction.
The neutralization reaction of Ca(OH)2 and alkyl benzene sulphonic acid (ABS) is catalyzed by the water which was added about 5 to 10% by weight in start of the reaction. The operational cost for separation of water is high and so the water should be at its minimum level in the reaction system to minimize the operational cost for separation of water.  Kinetic study was completed at constant temperature 343 K and different initial water content (1.5, 4.4 and 8.7 weight percent) to determine the reaction kinetic parameters and impact of water content on the rate of reaction, conversion and reaction time for complete conversion. Integral method was used for data analysis of experimental data and to determine the rate equation from concentration time profiles. The neutralization reaction of Ca(OH)2 and ABS is the second order autocatalytic reaction and estimated values of rate constant was 0.0081 liter/mol.min at 343 K and initial water content 1.5 weight percent. The highest rate of reaction was 0.024 mol/lit.min at 343 K and 1.5 weight percent of initial water and about 99.5 % conversion was achieved in 220 min. On increasing the initial water content, the rate of reaction also increased, and almost complete conversion was achieved in 160 min and 120 min when initial water content was 4.4 and 8.7 weight percent respectively. The water content in the end of the reaction was 5.02, 7.86 and 12 weight percent determined when the initial water content was 1.5, 4.4 and 8.7 weight percent respectively charged in the start of the reaction. More than 4.4 weight percent of initial water content is not necessary because after that increment in the rate of reaction was not significant.
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