Method for purifying trichloracetic aldehyde waste sulfuric acid
A technology of trichloroacetaldehyde and waste sulfuric acid, applied in sulfur trioxide/sulfuric acid, chemical instruments and methods, organic chemistry, etc., can solve the problems of harsh operating conditions, large water addition, high energy consumption, etc., and achieve low treatment cost, The effect of large production volume and simple process
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Embodiment 1
[0016] Put 40mL of chloral aldehyde waste sulfuric acid with a chloral concentration of 20mg / mL in a packed tower, feed 100mL / min of carbon dioxide, and at 25°C, the chloral concentration of 20mg / mL waste sulfuric acid The chloral is desorbed for 3 hours, and the desorption gas is passed into the packed tower to react with 30% dimethyl phosphite aqueous solution at 50°C to obtain trichlorfon, and the tail gas passes through an absorption pool with water as the absorption liquid. emptying. After desorption, the aldehyde content of waste sulfuric acid is 468ppm, and the aldehyde content of discharged water is 15ppm.
Embodiment 2
[0018] Put 40mL of chloral waste sulfuric acid with a chloral concentration of 20mg / mL in a packed tower, feed 300mL / min of air, and desorb the chloral in the waste sulfuric acid at 45°C for 3.5h, The desorption gas is passed into the packed tower to react with 60% dimethyl phosphite solution at 60°C to obtain trichlorfon, and the tail gas is then emptied after passing through an absorption pool with water as the absorption liquid. After desorption, the aldehyde content of the waste sulfuric acid was 18 ppm, and the aldehyde content of the discharged water was 11 ppm.
Embodiment 3
[0020] Put 40mL of chloral waste sulfuric acid with a chloral concentration of 20mg / mL in a packed tower, feed 500mL / min of nitrogen, and desorb the chloral in the waste sulfuric acid at 55°C for 4.0h, The desorption gas is passed into the packed tower to react with 80% dimethyl phosphite solution at 25°C to obtain trichlorfon, and the tail gas is then emptied after passing through an absorption pool with water as the absorption liquid. After desorption, the aldehyde content of the waste sulfuric acid was 16 ppm, and the aldehyde content of the discharged water was 17 ppm.
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