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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.

Inactive Publication Date: 2010-05-26
BINZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The incineration method not only wastes a large amount of organic solvents with important economic value, but also produces a large amount of toxic waste gas during the combustion process, causing secondary pollution to the atmospheric environment; the dilution method wastes a large amount of water resources and is likely to cause serious water pollution. Shortage is not desirable today
The vacuum distillation recovery requires high equipment, high energy consumption, and high recovery cost; the solvent recovery machine has the disadvantages of high energy consumption, low processing capacity, low separation efficiency, and low purity of the recovered solvent, especially for multi-component complex mixtures. The degree of separation is poor, and high-quality industrial-grade solvents cannot be obtained

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention provides a method for separating dimethyl benzene and butyl acetate from industrial waste solvent. The method comprises the following steps of: a, performing atmospheric simple distillation to the industrial waste solvent to obtain colorless and transparent waste solvent to be separated; b, mixing the waste solvent to be separated processed through simple atmospheric distillation with water in weight ratio of 1 to 3:1 to obtain a heterogeneous azeotropic system, and then performing rectification separation operation to the heterogeneous azeotropic system in a batch rectificationtower; and c, performing continuous reflux for 30 to 100 minutes after performing infinite reflux for 30 to 60 minutes in the batch rectification tower, and sequentially distilling off butyl acetate and dimethyl benzene from the top of the tower. The method for separating dimethyl benzene and butyl acetate from industrial waste solvent has the advantages that the separation effect is good, the heating temperature of the method is 50 to 80 DEG C lower than that of conventional homogeneous batch rectification, the yield coefficient of the butyl acetate is 80 to 99 percent, the yield coefficientof the dimethyl benzene is 84 to 87 percent, the separated dimethyl benzene and butyl acetate can be reused, the entrainer can be recycled, no pollution is produced during the separation process, theenergy consumption is low, and the processing cost is low.

Description

technical field [0001] The invention provides a method for separating industrial waste solvents, in particular a method for separating xylene and butyl acetate from industrial waste solvents. Background technique [0002] A large amount of industrial waste solvents are produced in the production process of automobiles and parts, pesticide intermediates, paints, electronic equipment, petrochemical industries, etc. These waste solvents contain xylene, butyl acetate, alkyd, amino, acrylic and other paints, which are easy to Volatile, flammable, explosive, and highly toxic, it is listed as a first-class hazardous industrial waste, which is extremely harmful to the environment and human health. However, the solvent components in waste solvents have high economic value. With the shortage of oil supply and the continuous increase of paint production and varieties, the demand for p-xylene in various countries in the world is on the rise year by year, and its price has risen from 4,...

Claims

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Application Information

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IPC IPC(8): C07C69/14C07C67/54C07C15/08
Inventor 李长海李贞玉李跃金贾冬梅
Owner BINZHOU UNIV