冷却干燥而制得的氯化氢按一定的比例混合，进入固定床反应器反应，反应器内

The hydrogen chloride obtained by cooling and drying is mixed in a certain proportion and enters the fixed bed reactor for reaction. The reactor is equipped with catalyst HgCl2 and the carrier is activated carbon. The reaction is exothermic, and the heat released is circulated outside the tubular reactor. The cooling water is taken away. The vinyl chloride produced by the reaction is crude vinyl chloride, which contains acidic impurities such as HCl and CO2. It needs to pass through a water washing tower and an alkali washing tower to remove impurities to obtain clean VCM gas. The clean gas is then dried, compressed, and liquefied through a dryer and a total condenser to obtain liquid vinyl chloride. The liquid vinyl chloride is rectified and refined, and then passes through a low boiling point tower and a high boiling point tower to remove low-component impurities and high-component respectively. Impurities to obtain refined liquid VCM. The production process flow chart of the vinyl chloride synthesis section is shown in Figure 3.

The hydrogen chloride produced by cooling and drying is mixed in a certain proportion and enters the fixed bed reactor reaction, which is equipped with the catalyst HgCl2, the carrier is activated carbon, the reaction is the heat release reaction, and the heat released is taken away by circulating cooling water outside the column reactor. The reaction produces vinyl chloride as coarse vinyl chloride, containing HCl, CO2 and other acidic impurities, need to be washed through the water tank and alkali washing tower, remove impurities, to obtain clean VCM gas. Clean gas is then dried, compressed and liquefyed by dryers and full condensers, and liquid vinyl chloride is refined and refined, followed by low boiling point towers and high boiling point towers, which remove low component impurities and high component impurities, respectively, to obtain refined liquid VCM. The production process flow diagram for the vinyl chloride synthesis segment is shown in Figure 3.

The hydrogen chloride produced by cooling and drying is mixed according to a certain proportion and goes into a fixed bed reactor for reaction. HgCl2 catalyst is installed in the reactor, and the carrier is activated carbon. The reaction is exothermic, and the heat released is taken away by circulating cooling water outside the tubular reactor. The vinyl chloride produced by the reaction is crude vinyl chloride, which contains HCl, CO2 and other acidic impurities. The impurities need to be removed through water washing tower and alkali washing tower to get clean VCM gas. The clean gas is dried, compressed and liquefied by dryer and full condenser to obtain liquid vinyl chloride. The liquid vinyl chloride is refined by distillation. The low component impurities and high component impurities are removed by low boiling point tower and high boiling point tower in turn to obtain refined liquid VCM. The production process flow chart of vinyl chloride synthesis section is shown in Figure 3.<br>