Tri-n-butylamine recycling method and recycling device used thereby
A technology of tri-n-butylamine and recovery device, applied in separation methods, chemical instruments and methods, distillation separation and other directions
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Embodiment 1
[0021] Embodiment 1, a kind of tri-n-butylamine recovery method,
[0022] At the beginning, the overhead distillate of the tri-n-butylamine light removal tower is used as a raw material, and the subsequent mixture of the tower overhead liquid of the tri-n-butylamine light removal tower and the bottom liquid of the molecular distillation tower 2 is used as a mixed raw material ; The volume ratio of the overhead distillate of the tri-n-butylamine lightening tower and the bottom liquid of the molecular distillation tower 2 in the mixed raw material is 2:1;
[0023] Raw material / mixed raw material enters rectification tower 1 from the feed port of rectification tower 1 and carries out rectification, and the tower bottom liquid that rectification tower 1 bottom obtains is tri-n-butylamine (mass fraction is greater than 99.5%), and this tri-n-butylamine Discharge from the tower bottom liquid outlet of rectifying tower 1;
[0024] The overhead distillate of rectifying tower 1 enters...
Embodiment 2
[0027] Embodiment 2, a kind of tri-n-butylamine recovery method,
[0028] The volume ratio of the overhead distillate of the tri-n-butylamine delightening tower and the bottom liquid of the molecular distillation tower 2 in the mixed raw material is 1:1;
[0029] The top pressure of rectification column 1 is 9kPa, the temperature at the bottom of the column is 98°C, and the reflux ratio is 5:1;
[0030] The tower top pressure of molecular distillation tower 2 is 50Pa, and the temperature in tower is controlled at 70 ℃;
[0031] The rest are equal to Example 1.
Embodiment 3
[0032] Embodiment 3, a kind of tri-n-butylamine recovery method,
[0033] The volume ratio of the overhead distillate of the tri-n-butylamine delightening tower and the bottom liquid of the molecular distillation tower 2 in the mixed raw material is 5:1;
[0034] The top pressure of rectification column 1 is 10kPa, the bottom temperature is 100°C, and the reflux ratio is 5:1;
[0035] The tower top pressure of molecular distillation tower 2 is 100Pa, and the temperature in tower is controlled at 75 ℃;
[0036] The rest are equal to Example 1.
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