首页> 外文期刊>Journal of Surfactants and Detergents >Alkylaromatics in Detergents Manufacture: Modeling and Optimizing Linear Alkylbenzene Sulfonation
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Alkylaromatics in Detergents Manufacture: Modeling and Optimizing Linear Alkylbenzene Sulfonation

机译:洗涤剂制造中的烷基芳族学:建模和优化直链烷基苯磺化

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摘要

Linear alkylbenzene sulfonic acid (ASA) is the main ingredient of many commercial formulations for industrial and domestic synthetic detergents. The current industrial ASA production method includes sulfonation of linear alkylbenzene (LAB) with sulfur trioxide in tubular falling-film reactors. The present study investigates the influence of light alkylaromatics on the efficiency of ASA production. After dealkylation and polymerization, these aromatic compounds form viscous components in the sulfonation reactor. This increases the organic liquid viscosity and disrupts the uniformity of sulfonation. We present the results of IR analysis of the LAB and ASA samples, which indicate that the viscous components are sulfones that are part of the unsulfonated matter. With due consideration of the sulfonation process reaction network, we developed a mathematical model for a sulfonation reactor considering the alkylaromatics content in the feed flow and its effect on the reaction rates. The results allowed the improvement of sulfonation process in terms of increasing the number of days between the reactor washings. The sulfur flow rate increased from 371.7 to 380.9 kg h(-1) at the end of this period for the aromatics content in LAB of 4 wt.% and from 372.1 to 380.1 kg h(-1) for aromatics content in LAB of 6 wt.%. The proposed modifications of the process modes can increase the SO3 conversion up to 98%.
机译:线性烷基苯磺酸(ASA)是工业和国内合成洗涤剂的许多商业配方的主要成分。目前的工业ASA制备方法包括用三氧化硫致膜反应器中三氧化硫的直链烷基苯(实验室)的磺化。本研究研究了轻烷基芳族学对ASA生产效率的影响。在促使和聚合后,这些芳族化合物在磺化反应器中形成粘性组分。这增加了有机液体粘度并破坏了磺化的均匀性。我们介绍了对实验室和ASA样品的IR分析的结果,表明粘性组分是亚砜,是未挤出物质的一部分。随着磺化过程反应网络的适当考虑,考虑到进料流动中的烷基甘油醇含量及其对反应速率的影响,我们开发了一种磺化反应器的数学模型。结果在增加反应器洗涤型之间的天数方面允许改善磺化过程。在该期间的亚芳族含量为4重量%的芳烃含量和372.1至380.1kg h(-1)的情况下,硫流量从371.7〜380.9 kg h(-1)增加到6个wt.%。该过程模式的建议修改可以将SO3转换增加到98%。

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