Method for treating fetid exhaust gas in production process of sulfo-amino ester
A technology for the production process of thioamino esters, which is applied in the field of treatment of malodorous waste gas in the production process of thioamino esters, can solve problems such as inconvenient operation, and achieve the effects of simple method, low investment and operation cost, and stable effect
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Embodiment 1
[0019] (1) The malodorous gas with low boiling point produced in the thioamino ester production process is passed into the buffer tank through vacuuming, and the control pressure is -0.04MPa;
[0020] (2) The gas in the buffer tank is cooled by a cryogenic device, and the freezing temperature is 30° C., and the hydrogen sulfide and VOSC (mercaptan, sulfide) therein are recovered.
[0021] The content of hydrogen sulfide in the collected gas is 160mg / g, the content of VOSC (mercaptan, sulfide) is 2mg / g, the content of hydrogen sulfide in the tail gas after cryogenic treatment is 80mg / g, and the content of VOSC (mercaptan, sulfide) ) content is 750μg / g.
Embodiment 2
[0023] (1) The malodorous gas with low boiling point produced in the thioamino ester production process is passed into the buffer tank through vacuuming, and the control pressure is -0.1MPa;
[0024] (2) The gas in the buffer tank is cooled by a cryogenic device, and the freezing temperature is -50°C, and the hydrogen sulfide and VOSC (mercaptan, sulfide) therein are recovered.
[0025] The content of hydrogen sulfide in the collected gas is 160mg / g, the content of VOSC (mercaptan, sulfide) is 2mg / g, the content of hydrogen sulfide in the tail gas after cryogenic treatment is 100μg / g, and the content of VOSC (mercaptan, sulfide) ) content of 95 μg / g.
Embodiment 3
[0027] (1) The malodorous gas with low boiling point produced in the thioamino ester production process is passed into the buffer tank through vacuuming, and the control pressure is -0.06MPa;
[0028] (2) The gas in the buffer tank is cooled by a cryogenic device, and the freezing temperature is -10°C, and the hydrogen sulfide and VOSC (mercaptan, sulfide) therein are recovered.
[0029] The content of hydrogen sulfide in the collected gas is 160mg / g, the content of VOSC (mercaptan, sulfide) is 2mg / g, the content of hydrogen sulfide in the tail gas after cryogenic treatment is 80μg / g, and the content of VOSC (mercaptan, sulfide) ) content of 15 μg / g.
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