The production method of thionyl chloride
A technology of thionyl chloride and its production method, which is applied in the direction of thionyl chloride, sulfur and halogen compounds, can solve the problems of increasing the production load of the rectification tower, reducing the safety performance of the device, and not being able to condense the tail gas, so as to reduce energy consumption, Ease of operation and load reduction effect
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Embodiment 1
[0020] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesizer enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly passes through the absorption tower in gaseous form and then enters the decomposer and the absorption tower The liquid phase enters the receiving tank;
[0021] (2) The gas phase crude product thionyl chloride from the decomposer enters the rectification tower, the liquid phase in the receiving tank is recycled to the synthesis kettle, the heavy components generated at the bottom of the rectification tower are recycled back to the synthesis kettle, and the gas phase at the top of the rectification tower is recycled After condensing, it enters the reflux tank. Part of the liquid phase in the reflux tank is pumped to the rectification tower for reflux by the first machine pump. The remaining liquid phase in the reflux tank is extracted and reused in the syn...
Embodiment 2
[0024] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesizer enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly passes through the absorption tower in gaseous form and then enters the decomposer and the absorption tower The liquid phase enters the receiving tank;
[0025] (2) The gas phase crude product thionyl chloride from the decomposer enters the rectification tower, the liquid phase in the receiving tank is recycled to the synthesis kettle, the heavy components generated at the bottom of the rectification tower are recycled back to the synthesis kettle, and the gas phase at the top of the rectification tower is recycled After condensing, it enters the reflux tank. Part of the liquid phase in the reflux tank is pumped to the rectification tower for reflux by the first machine pump. The remaining liquid phase in the reflux tank is extracted and reused in the syn...
Embodiment 3
[0028] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesizer enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly passes through the absorption tower in gaseous form and then enters the decomposer and the absorption tower The liquid phase enters the receiving tank;
[0029] (2) The gas phase crude product thionyl chloride from the decomposer enters the rectification tower, the liquid phase in the receiving tank is recycled to the synthesis kettle, the heavy components generated at the bottom of the rectification tower are recycled back to the synthesis kettle, and the gas phase at the top of the rectification tower is recycled After condensing, it enters the reflux tank. Part of the liquid phase in the reflux tank is pumped to the rectification tower for reflux through the first machine pump. The remaining liquid phase in the reflux tank is extracted and reused in th...
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