Author:
Kurbanova Dilafruz,Fayzullaev Normurot,Bobomurodova Sanobar
Abstract
In the work, a catalytic optimal system was selected for the hydrochlorination of important components of chlorinated organic waste in the production of vinyl chloride. Information on the active and selective effect of various substances increasing the speed of the reaction in the hydrogen chloride release reaction was given. Operating modes of the reactor selected for oxidative chlorination of ethylene with hydrogen chloride in the presence of oxygen, designed for oxidative chlorination of ethylene with hydrogen chloride in the presence of atmospheric oxygen, were calculated. Also, the operating modes of the reactor were calculated, the kinetic equations of the rate of formation were constructed, and the equations of the relationship between the reactants and the reaction products were studied. As a result of the experiments, important kinetic parameters of simm-dichloroethane were determined to create a model of the simm-dichloroethane (1,2-dichloroethane) synthesis process. Kinetic studies were carried out in a temperature range of 300-350 ℃ in an ideal displacement flow reactor. In it, the reaction proceeded with no more than 70% conversion of sym-dichloroethane (1,2-dichloroethane). In addition, the material and heat balance of the reactor designed for oxidative chlorination of ethylene with hydrogen chloride in the presence of air oxygen was calculated. The purpose of the work is to study the optimal conditions and kinetic laws of hydrogen chloride separation reaction from simm-dichloroethane (1,2-dichloroethane).