The production process of thionyl chloride
A technology for thionyl chloride and production process, which is applied in the field of production technology of thionyl chloride, can solve the problems of reduced device safety performance, inability to condense tail gas, complicated process and the like, and achieves the advantages of small heat loss, improved safety and short process route. 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 product thionyl chloride generated by the reaction in the reactor directly enters the rectification tower in gaseous form, and the recombination produced at the bottom of the rectification tower The sub-circulation is applied back to the synthesis kettle, and the gas phase at the top of the rectification tower enters the reflux tank after being condensed;
[0021] (2) Part of the liquid phase in the reflux tank is pumped to the rectifying tower to reflux through the first machine pump, and the remaining liquid phase in the reflux tank is taken out and used as a synthesis kettle; the volume ratio of part of the liquid phase to the remaining liquid phase is 10:1;
[0022] (3) The gas phase in the reflux tank enters the evacuation tank through the injector and then circulates back to the synthesis kettle, and the qu...
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 product thionyl chloride generated by the reaction in the reactor directly enters the rectification tower in gaseous form, and the recombination produced at the bottom of the rectification tower The sub-circulation is applied back to the synthesis kettle, and the gas phase at the top of the rectification tower enters the reflux tank after being condensed;
[0025] (2) Part of the liquid phase in the reflux tank is pumped to the rectifying tower to reflux through the first machine pump, and the remaining liquid phase in the reflux tank is taken out and used as a synthesis kettle; the volume ratio of part of the liquid phase to the remaining liquid phase is 4:1;
[0026] (3) The gas phase in the reflux tank enters the evacuation tank through the injector and then circulates back to the synthesis kettle, and the qua...
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 product thionyl chloride generated by the reaction in the reactor directly enters the rectification tower in gaseous form, and the recombination produced at the bottom of the rectification tower The sub-circulation is applied back to the synthesis kettle, and the gas phase at the top of the rectification tower enters the reflux tank after being condensed;
[0029] (2) Part of the liquid phase in the reflux tank is pumped to the rectifying tower to reflux through the first machine pump, and the remaining liquid phase in the reflux tank is taken out and used as a synthesis kettle; the volume ratio of part of the liquid phase to the remaining liquid phase is 6:1;
[0030] (3) The gas phase in the reflux tank enters the evacuation tank through the injector and then circulates back to the synthesis kettle, and the qua...
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