设计有机物质混合物硫化工艺的新硬件和技术方案

O. Dzevochko, M. Podustov, A. Dzevochko
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摘要

文章指出,以C12 - C14高醇为基础的表面活性剂主要用于各种个人卫生产品,如洗发水、沐浴发泡剂、牙膏、洗洁精和精细洗衣液。使用基于C12 - C14的高级醇和椰子油中高级脂肪酸的单乙醇酰胺的混合物的表面活性剂,可以显著改善个人卫生产品的质量特性。介绍了一种以管状膜吸收器为主要元件的有机混合物硫化工艺装置及工艺方案。结果表明,对于以C12 - C14为基础的高醇类有机物质和椰子油的高脂肪酸类单乙醇酰胺为基础的双组分混合物的磺化,必须使用管状膜吸收器,该吸收器有两段冷却,上部为吸收器长度的1/3,下部为吸收器长度的2/3。气气流速度保持在Vg = 20 m/s,试剂摩尔比为1.08:1.0,气气流中三氧化硫浓度为3.7% vol.,初始反应物温度:液相为313 K,气气流为303 K,冷却水- 293 K。基于这些初始数据,对工业管式吸收塔进行了计算。给出了计算的数据。根据所开发的算法和程序在MatLab语言中进行了工业管状膜吸收器的计算,程序采用迭代法进行计算。给出了工业吸收塔管道数的计算方法。结果表明,吸收器由以下主要部件组成:一个上椭圆罩、一个气-气流动分配板、一个分配有机物混合物的室、成膜器、两个冷却室和一个下椭圆罩。介绍了在工业管状膜吸收器的基础上,设计并提出了一种新的设备和工艺方案。介绍了实现该系统的主要技术指标、经济指标和环境指标。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
DESIGNING OF A NEW HARDWARE AND TECHNOLOGICAL SCHEME OF THE PROCESS OF ORGANIC SUBSTANCES MIXTURES SULPHING
The article states that surfactants based on higher alcohols fr. C12 - C14 are mainly used in a wide range of personal hygiene products, such as shampoos, foaming agents for baths, toothpastes, dishwashing liquid, and delicate laundry detergents. The use of surfactants based on a mixture of higher alcohols fr. C12 - C14 and monoethanolamides of higher fatty acids of coconut oil makes it possible to significantly improve the quality characteristics of personal hygiene products. It is stated that the main element of the apparatus and technological scheme of the sulfation process of mixtures of organic substances is a tubular film absorber. It is shown that for the sulfation of two-component mixtures of organic substances based on higher alcohols fr. C12 - C14 and monoethanolamides of higher fatty acids of coconut oil must use a tubular film absorber, which has two-stage cooling - the upper part 1/3 of the length of the absorber, the lower part 2/3 of the length of the absorber. The speed of the gasair flow is maintained at Vg = 20 m/s, the molar ratio of reagents is 1.08 : 1.0, the concentration of sulfur trioxide in the gas-air flow is 3.7% vol., the temperature of the initial reactants: liquid phase is 313 K, gas-air flow is 303 K, cooling water - 293 K. Based on such initial data, an industrial tubular absorber was calculated. The data of such a calculation are given. It is stated that the calculation of the industrial tubular film absorber was carried out according to the developed algorithm and program in the MatLab language, the iterative method of calculation was used in the program. The calculation of the number of pipes of an industrial absorber is given. It is shown that the absorber consists of the following main elements - an upper elliptical cover, a gas-air flow distribution plate, a chamber for distributing a mixture of organic substances, film formers, two cooling chambers, and a lower elliptical cover. It is stated that on the basis of an industrial tubular film absorber, a new equipment and technological scheme has been designed and presented. The main technical, economic and environmental indicators of the implementation of such a hardware and technological scheme are presented.
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