Sulfuryl chloride waste gas treatment device and method
A waste gas treatment device and waste gas treatment technology, applied in the direction of thionyl chloride, chemical instruments and methods, sulfur compounds, etc., can solve the problems of waste gas emission and low purity, and achieve the effect of less equipment investment and good tail gas treatment effect
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Embodiment 1
[0049] The sulfuryl chloride waste gas treatment device described in Example 1 includes a tail gas condenser 1, and the tail gas condenser 1 is connected to the mist catcher 2 through a pipeline, and the mist catcher 2 is connected to the preheater 3 through a pipeline, and the preheater 3 is connected to the first-level reactor 4 through pipelines, and the first-level reactor 4 is connected to the sulfur monochloride header tank 8 through pipelines; the first-level reactor 4 is connected to the second-level reactor 5 through pipelines, and the first-level reactor 4 and the upper part of the secondary reactor 5 are connected to the liquid sulfur feed pipe 9, and the secondary reactor 5 is connected to the sulfur furnace 11 through pipelines.
[0050] in:
[0051] The bottom of the secondary reactor 5 is connected to the secondary dump pump 7 through a pipeline, and the secondary dump pump 7 is connected to the upper feed port of the primary reactor 4 through a pipeline.
[00...
Embodiment 2
[0067] The sulfuryl chloride exhaust gas treatment method described in present embodiment 2 may further comprise the steps:
[0068] (1) Control the outlet temperature of the tail gas condenser at 15°C, and the condensing medium of the tail gas condenser is circulating water;
[0069] (2) After condensing, enter the mist catcher, capture the remaining less part of sulfuryl chloride, and completely eliminate sulfuryl chloride;
[0070] (3) The gas phase from the mist catcher enters the preheater, increases the temperature of the gas phase entering the reactor, and controls the steam feed rate of the preheater, thereby controlling the gas phase outlet temperature of the preheater to remain at 90°C;
[0071] (4) with preheated waste gas gas phase, in volume fraction, waste gas is made up of chlorine 40%, sulfur dioxide 40% and air 20%, passes into primary reactor, and primary reactor reaction medium is sulfur monochloride, At the same time, part of the liquid sulfur is input thr...
Embodiment 3
[0077] The sulfuryl chloride exhaust gas treatment method described in the present embodiment 3 may further comprise the steps:
[0078] (1) Control the outlet temperature of the tail gas condenser at 30°C, and the condensing medium of the tail gas condenser is circulating water;
[0079] (2) After condensing, enter the mist catcher, capture the remaining less part of sulfuryl chloride, and completely eliminate sulfuryl chloride;
[0080] (3) The gas phase coming out of the mist catcher enters the preheater, increases the temperature of the gas phase entering the reactor, and controls the steam feed rate of the preheater, thereby controlling the gas phase outlet temperature of the preheater to remain at 112° C.;
[0081] (4) with preheated waste gas gas phase, in volume fraction, waste gas is made up of chlorine 40%, sulfur dioxide 40% and air 20%, passes into primary reactor, and primary reactor reaction medium is sulfur monochloride, At the same time, part of the liquid sul...
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Abstract
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