Method for recycling wastes of trifluoromethyl phenylamine kettle residue
A technology for trifluoromethylaniline and waste, applied in the direction of amino compound purification/separation, etc., can solve problems such as polymerization reaction, achieve the effects of simple operation process, comprehensive utilization of resources, and reduction of pollutant discharge
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Embodiment 1
[0019] Add 800g of trifluoromethylaniline residue and 24g of sodium carbonate to a 3L reactor, control the temperature at 140°C, and distill under reduced pressure (system internal pressure is 10mmHg) to obtain 480g of m-trifluoromethylaniline and p-trifluoromethylaniline The light components are collected for the next step of rectification.
[0020] Add 3000g of light components of m-trifluoromethylaniline and p-trifluoromethylaniline obtained in the previous step to a 5L rectification device, 90g of sodium carbonate, control the temperature at 140°C, and carry out rectification under reduced pressure (10mmHg in the system) , to obtain 702g of m-trifluoromethylaniline, with a purity of 98.5%, to obtain 63g of transition fractions (35.1% of m-trifluoromethylaniline, and 64.2% of p-trifluoromethylaniline), to obtain 2003g of p-trifluoromethylaniline, with a purity of 98.1% . Example 2
Embodiment 2
[0021] Add 800g of trifluoromethylaniline residue, 16g of potassium hydroxide to a 3L reactor, control the temperature at 80°C, and distill under reduced pressure (5mmHg in the system) to obtain 482g of m-trifluoromethylaniline and p-trifluoromethylaniline. Light components are collected for the next step of rectification.
[0022] Add 3000g of light components of m-trifluoromethylaniline and p-trifluoromethylaniline obtained in the previous step to a 5L rectification device, 60g of potassium hydroxide, control the temperature at 80°C, and carry out refining under reduced pressure (5mmHg in the system). Distillation, to obtain 702g m-trifluoromethylaniline, purity 98.5%, to obtain 61g of transition fraction (m-trifluoromethylaniline 35.1%, p-trifluoromethylaniline 64.2%), to obtain 2005g p-trifluoromethylaniline, purity 98.1 %.
Embodiment 3
[0024] Add 800g of trifluoromethylaniline residue and 20g of sodium hydroxide to the 3L reactor, control the temperature at 90°C, and distill under reduced pressure (6mmHg in the system) to obtain 481g of m-trifluoromethylaniline and p-trifluoromethylaniline. Light components are collected for the next step of rectification.
[0025] Add 3000g light components of m-trifluoromethylaniline and p-trifluoromethylaniline obtained in the previous step to a 5L rectification device, 80g of sodium hydroxide, control the temperature at 90°C, and carry out refining under reduced pressure (6mmHg in the system). Distillation, to obtain 702g m-trifluoromethylaniline, purity 98.5%, to obtain 62g transition fraction (m-trifluoromethylaniline 35.1%, p-trifluoromethylaniline 64.2%), to obtain 2004g p-trifluoromethylaniline, purity 98.1 %.
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