表面活性剂生产中硫化过程的系统分析

O. Dzevochko, M. Podustov, A. Dzevochko
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引用次数: 0

摘要

提供了乌克兰工业各个领域使用表面活性物质的数据。显示了表面活性物质生产的快速发展。给出了表面活性物质生产的主要阶段。结果表明,硫化阶段是主要的硫化阶段,在此阶段得到的产品具有较高的质量指标。介绍了表面活性物质(表面活性剂)技术中硫酸化剂的主要缺点和优点。介绍了有机物磺化工艺的设备特点和工艺方案。据称,在工业条件下,使用具有向下流动相的管状膜吸收器是目前最有前途的。给出了Lewis - Whitman, Levich, Higby, dankvert等简化模型的对流扩散方程。拟目前硫酸盐化作用的过程与以下阶段:管式膜吸收传质过程气体三氧化硫的界面、表面吸收的过程中三氧化硫的有机物质通过放热化学反应,之间的热交换过程液态和气态空气流动,液相之间的换热过程和冷却水的流动。给出了传质系数的计算公式,使计算结果与Gutierrez的实验数据接近。给出了有机原料吸附三氧化硫过程中连续化学反应的过程。给出了反应的动力学方程和磺化度及产物颜色的计算方法。给出了计算传热系数和传热系数的基本方程。本文给出了管式膜吸收器硫化过程的数学模型。所得产品达到高质量指标的可能性为:磺化度为97.9%,在碘标度上颜色为1单位。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
SYSTEM ANALYSIS OF THE SULFATION PROCESS IN THE PRODUCTION OF SURFACTANT SUBSTANCES
Data on the use of surface-active substances in various areas of Ukrainian industry are given. The rapid development of the production of surface-active substances is shown. The main stages of the production of surface-active substances are given. It is shown that the sulfation stage is the main one, at which high quality indicators of the obtained products are achieved. The main disadvantages and advantages of sulfating agents in the technology of surface-active substances (surfactants) are given. The characteristics of the equipment and technological schemes of the sulfation process of organic substances are given. It is claimed that the use of tubular film absorbers with a downward flow of phases is currently the most promising for use in industrial conditions. Convective diffusion equations for the simplified models of Lewis – Whitman, Levich, Higby, Dankverts are given. It is proposed to present the process of sulfation in a tubular film absorber with the following stages: the process of mass transfer of gaseous sulfur trioxide to the surface of the interface, the process of absorption of sulfur trioxide by an organic substance with the passage of an exothermic chemical reaction, the process of heat exchange between the liquid phase and the gaseous air flow, the process of heat exchange between the liquid phase and the flow of cooling water. The equation for calculating the mass transfer coefficient is given, which allows obtaining data close to Gutierrez's experimental data. The passage of successive chemical reactions during the absorption of sulfur trioxide by organic raw materials is shown. Kinetic equations and methods of calculating the degree of sulfation and color of the obtained products are given. Basic equations for calculating heat transfer coefficients and heat transfer coefficients are given. The results of mathematical modeling of the sulfation process in a tubular film absorber are given. The possibility of achieving high quality indicators of the obtained product is shown: the degree of sulfation is 97,9 %, the color is 1 unit on the iodine scale.
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