Production process of sulfoxide chloride
A technology of thionyl chloride and production process, applied in the field of production technology of thionyl chloride, can solve the problems of increasing the production load of a rectifying tower, reducing the safety performance of the device, and being unable to condense tail gas, thereby reducing energy consumption and ensuring conversion. Efficiency 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 synthesis kettle enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly enters the decomposer after being decolorized in the sulfur tank in gaseous form, and the sulfur tank The bottom liquid phase circulation is applied to the synthesis kettle;
[0021] (2) The crude sulfur oxychloride in the gas phase from the decomposer enters the rectification tower, and the heavy components produced at the bottom of the rectification tower are recycled to the synthesis kettle, and the gas phase at the top of the rectification tower enters the reflux tank after condensation, and part of the liquid The phase is pumped by the first machine to the reflux of the rectifying tower, and the remaining liquid phase in the reflux tank is taken out and put back into the synthesis kettle; the volume ratio of part of the liquid phase to the re...
Embodiment 2
[0024] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesis kettle enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly enters the decomposer after being decolorized in the sulfur tank in gaseous form, and the sulfur tank The bottom liquid phase circulation is applied to the synthesis kettle;
[0025] (2) The crude sulfur oxychloride in the gas phase from the decomposer enters the rectification tower, and the heavy components produced at the bottom of the rectification tower are recycled to the synthesis kettle, and the gas phase at the top of the rectification tower enters the reflux tank after condensation, and part of the liquid The phase is pumped by the first machine to the reflux of the rectification tower, and the remaining liquid phase in the reflux tank is taken out and put back into the synthesis kettle; the volume ratio of part of the liquid phase to the...
Embodiment 3
[0028] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesis kettle enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly enters the decomposer after being decolorized in the sulfur tank in gaseous form, and the sulfur tank The bottom liquid phase circulation is applied to the synthesis kettle;
[0029] (2) The crude sulfur oxychloride in the gas phase from the decomposer enters the rectification tower, and the heavy components produced at the bottom of the rectification tower are recycled to the synthesis kettle, and the gas phase at the top of the rectification tower enters the reflux tank after condensation, and part of the liquid The phase is pumped by the first machine to the reflux of the rectifying tower, and the remaining liquid phase in the reflux tank is taken out and put back into the synthesis kettle; the volume ratio of part of the liquid phase to the re...
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