Treatment technology for tail gas generated from production process of cis-Z-3-(2-chloro-3, 3, 3-triflulo-1-propenyl)-2, 2-dimethyl cyclopropane carbonyl chloride
A production process, the technology of kung fu acid chloride, applied in the direction of dispersion particle separation, chemical instruments and methods, separation methods, etc., can solve the problems of high processing cost and complicated process, and achieve the effect of reducing processing cost, simple process and improving economic benefits
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Embodiment 1
[0026] Firstly, the tail gas is passed into the falling film absorption tower and passes through the first-level falling film absorber. After the hydrogen chloride gas in the tail gas is absorbed by the first-level falling film absorber, most of the hydrogen chloride gas is absorbed to generate hydrochloric acid, which is released from the absorption tower. The gas is sulfur dioxide and part of hydrogen chloride gas, when the concentration of hydrochloric acid reaches more than 20%, start pumping hydrochloric acid into the hydrochloric acid storage tank;
[0027] (2) The released gas enters the secondary falling film absorber for absorption again, the hydrogen chloride gas is completely absorbed, and the gas released from the absorption tower is sulfur dioxide;
[0028] (3) The released sulfur dioxide gas is passed into 18% soda ash aqueous solution for tertiary absorption, and most of the sulfur dioxide reacts with soda ash to form sodium bisulfite;
[0029] (4) After the th...
Embodiment 2
[0031] Test Data
[0032] According to the production capacity of the company's kung fu acid chloride production device, the use of the present invention can produce about 274.5 tons of hydrochloric acid (30%) by-product a year, which can be used for pH adjustment in the company's acetamiprid production process, which is conducive to reducing production costs . The by-product of 30% sodium bisulfite is about 780 tons a year, worth more than 1.56 million yuan. In terms of cost, only 120 tons of soda ash is needed, about 300,000 yuan. In contrast, the original process used about 190 tons of caustic soda to absorb hydrogen chloride and sulfur dioxide, and about 1,900 tons of sodium chloride and sodium sulfite wastewater were produced (the absorption solution was prepared at 10%). This part of high-salt wastewater needs to be desalinated by a three-effect evaporator before entering the sewage biochemical treatment system, which consumes 1,140 tons of steam and is worth 279,300 y...
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