Method for separating dimethyl benzene and butyl acetate from industrial waste solvent
The technology of butyl acetate and waste solvent is applied in the separation field of industrial waste solvent, which can solve the problems of high equipment requirements, low solvent purity and low separation efficiency, and achieves the effects of wide application fields, remarkable economic benefits and good separation effect.
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Embodiment 1
[0013] a. Carry out simple atmospheric pressure distillation on industrial waste solvents, and distill at 120°C for 3 hours to remove suspended solids and high-boiling impurities in industrial waste solvents to obtain colorless and transparent waste solvents to be separated. The sum of the content of toluene and butyl acetate is 93% by mass percentage, and other heavy impurity components are 7% by mass percentage;
[0014] b. Mixing the waste solvent to be separated obtained after the simple distillation at atmospheric pressure with water in a ratio of 1:1 by weight to form a heterogeneous azeotropic system, and carry out rectification separation operation in a batch rectification tower;
[0015] c. After 30 minutes of total reflux in the batch rectification column, continue to reflux for 30 minutes under the conditions of maintaining the reflux ratio of 5, the temperature of the tower bottom at 92°C, and the temperature at the top of the tower at 89°C, and distill butyl acetat...
Embodiment 2
[0017] a. Carry out simple atmospheric pressure distillation on industrial waste solvents, and distill at 200°C for 5 hours to remove suspended solids and high-boiling impurities in industrial waste solvents to obtain colorless and transparent waste solvents to be separated. The sum of the content of toluene and butyl acetate is 97% by mass percentage, and other heavy impurity components are 3% by mass percentage;
[0018] b. Mixing the waste solvent to be separated obtained after the simple distillation at atmospheric pressure with water in a ratio of 3:1 by weight to form a heterogeneous azeotropic system, and carry out rectification and separation operations in a batch rectification tower;
[0019] c. After 60 minutes of total reflux in the batch rectification tower, continue to reflux for 100 minutes under the conditions of maintaining a reflux ratio of 15, a temperature of the bottom of the tower at 150°C, and a temperature of the top of the tower at 100°C, and distill but...
Embodiment 3
[0021] a. Carry out simple atmospheric pressure distillation on industrial waste solvents, distill at 150°C for 4 hours, remove suspended solids and high-boiling impurities in industrial waste solvents, and obtain colorless and transparent waste solvents to be separated. The sum of the content of toluene and butyl acetate is 95% by mass percentage, and other heavy impurity components are 5% by mass percentage;
[0022] b. Mixing the waste solvent to be separated obtained after the simple distillation at atmospheric pressure with water in a ratio of 2:1 by weight to form a heterogeneous azeotropic system, and carry out rectification separation operation in a batch rectification tower;
[0023] c. After 45 minutes of total reflux in the batch rectification tower, continue to reflux for 70 minutes under the conditions of maintaining a reflux ratio of 10, a temperature of the bottom of the tower of 120°C and a temperature of the top of the tower of 92°C, and sequentially distill bu...
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