Method and device for removing acid in tail gas from reaction for producing 2-butyl acetate
A technology for the removal of sec-butyl acetate, which is applied in separation methods, carboxylate preparation, chemical instruments and methods, etc., can solve the problems of small amount of acid gas, influence on economic benefits, high operating costs, etc., and reduce production Reasonable cost, technical solutions, and easy processing and manufacturing
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Embodiment 1
[0029] Take the tail gas treatment of 30,000 tons / year sec-butyl acetate production line as an example. According to the above-mentioned technological process and steps, a 10% sodium hydroxide solution for circulating absorption is prepared, and the tail gas containing 99% acetic acid is released at an amount of 5.9t / h during operation, and the temperature control system of the deacidification tower is started, and two alkalis, large and small, are The liquid circulation pump started to run, and the accident treatment was completed after 10 minutes. The concentration of alkali solution was 5.6% after sampling and analysis. The acetic acid content in the tail gas after deacidification could not be measured, and the quality of the tail gas met the requirements.
Embodiment 2
[0031] Take the tail gas treatment of 30,000 tons / year sec-butyl acetate production line as an example. According to the above technological process and steps, prepare 10% circulating absorption sodium hydroxide solution, the tail gas containing 82ppm concentration of acetic acid is discharged at the amount of 3.9t / h during the operation, and the small lye circulation pump of the deacidification tower runs, after 10 minutes The accident treatment was completed, the concentration of lye was almost unchanged in sampling and analysis, the acetic acid content in the tail gas after deacidification was undetectable, and the quality of the tail gas met the requirements.
Embodiment 3
[0033] Take the tail gas treatment of 30,000 tons / year sec-butyl acetate production line as an example. According to the above-mentioned technological process and steps, prepare 10% circulating absorption sodium hydroxide solution, the tail gas containing 52ppm concentration of acetic acid is discharged at the amount of 8.5t / h during the operation, and the small lye circulating pump of the deacidification tower runs, after 15 minutes The accident treatment was completed, the concentration of lye was almost unchanged in sampling and analysis, the acetic acid content in the tail gas after deacidification was undetectable, and the quality of the tail gas met the requirements.
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