Preparing method of thionyl chloride
A technology of thionyl chloride and chlorine gas, which is applied in the direction of thionyl chloride, sulfur and halogen compounds, etc., can solve problems such as complex processes, and achieve the effects of increasing product yield, strong system safety, and low energy consumption
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Embodiment 1
[0016] The raw material mixture gas composed of sulfur dioxide, chlorine and sulfur dichloride enters from the upper part of the reactor, the gas phase of the crude thionyl chloride directly enters the rectification tower from the lower part of the reactor, and the gas phase at the top of the rectification tower is circulated back to the reactor, and the rectification tower Qualified products are produced in the middle; the pressure of the reactor and the rectification tower are both normal pressure, the temperature of the reactor is 100°C, the gas phase at the top of the rectification tower is controlled by the fan for circulation, and the middle of the rectification tower is equipped with a liquid accumulator. The temperature of the liquid vessel is controlled at 77°C, and the temperature of the rectifying column tank is 140°C. The product yield is 99.95%.
Embodiment 2
[0018] The raw material mixture gas composed of sulfur dioxide, chlorine and sulfur dichloride enters from the upper part of the reactor, the gas phase of the crude thionyl chloride directly enters the rectification tower from the lower part of the reactor, and the gas phase at the top of the rectification tower is circulated back to the reactor, and the rectification tower Qualified products are produced in the middle; the pressure of the reactor and the rectification tower are both normal pressure, the temperature of the reactor is 400°C, the gas phase at the top of the rectification tower is controlled by the fan for circulation, and the middle of the rectification tower is equipped with a liquid accumulator. The temperature of the liquid vessel is controlled at 76°C, and the temperature of the rectifying column tank is 110°C. The product yield is 99.96%.
Embodiment 3
[0020] The raw material mixture gas composed of sulfur dioxide, chlorine and sulfur dichloride enters from the upper part of the reactor, the gas phase of the crude thionyl chloride directly enters the rectification tower from the lower part of the reactor, and the gas phase at the top of the rectification tower is circulated back to the reactor, and the rectification tower Qualified products are produced in the middle; the pressure of the reactor and the rectification tower is normal pressure, the temperature of the reactor is 300 ° C, the gas phase at the top of the rectification tower is controlled by the fan, and a liquid accumulation device is installed in the middle of the rectification tower. The temperature of the liquid vessel is controlled at 78°C, and the temperature of the rectifying column tank is 120°C. The product yield is 99.98%.
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