Refining method for recovery of solvent and unpolymerized monomers in the production process of wet compound rubber
A production process and wet mixing technology, which is applied in the field of refining solvents and unpolymerized monomers in the wet mixing rubber production process, and can solve the problem of large loss of solvent monomers, large consumption of washing water, and failure to achieve polymerization Level requirements and other issues, to achieve the effect of low cost and simple operation
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Embodiment 1
[0039] (1) the mixture (the water that contains 0.02wt% of water, the ethanol of 0.05wt% and other impurity with the solvent normal hexane that reclaims in the solution polymerization styrene-butadiene glue wet mixing process and unpolymerized monomer, the unpolymerized monomer Content is 0wt%) enters from the middle part of the rectifying tower that the number of theoretical plate is 20, wherein, mixture flow rate is 50000kg / h, rectifying tower operating pressure 0.1MPaG, reflux ratio 1, tower top temperature 65 ℃, tower bottom temperature 90 ℃; the mixture 1 of solvent and unpolymerized monomer is extracted at the bottom of the tower (the content of water and ethanol is all less than 0.0001wt%), and the azeotropic mixture 2 of solvent, unpolymerized monomer, ethanol and water is extracted at the top of the tower;
[0040] (2) Wash the azeotropic mixture 2 of the solvent, unpolymerized monomer, ethanol and water extracted from the top of the tower in step (1) with water (three...
Embodiment 2
[0053] (1) the solvent hexane that reclaims in the rare earth isoprene rubber glue wet mixing process and the mixture of unpolymerized monomer (containing the water of 0.02wt%, the ethanol of 0.05wt%, the isoprene of 1wt% and Other impurities) enter from the middle of a rectification tower with a theoretical plate number of 20, wherein the flow rate of the mixture is 50000kg / h, the operating pressure of the rectification tower is 0.2MPaG, the reflux ratio is 5, the temperature at the top of the tower is 68°C, and the temperature at the bottom of the tower is 100°C; A mixture 1 of solvent and unpolymerized monomer is taken out at the bottom of the tower (the content of water and ethanol is all less than 0.0001wt%), and an azeotropic mixture 2 of solvent, unpolymerized monomer, ethanol and water is taken out at the top of the tower;
[0054] (2) Wash the azeotropic mixture 2 of the solvent, unpolymerized monomer, ethanol and water extracted from the top of the tower in step (1) w...
Embodiment 3
[0067] (1) The mixture of solvent hexane and unpolymerized monomers recovered in the rare earth isoprene rubber glue wet mixing process (containing 0.02wt% of water, 0.2wt% of ethanol, 5wt% of isoprene and other Impurities) with a flow rate of 50000kg / h, first wash with an aqueous sodium hydroxide solution with a flow rate of 5000kg / h, a concentration of 0.2mol / L, and a temperature of 40°C, and then enter from the middle of a rectification tower with a theoretical plate number of 20. Rectification column operating pressure 0.2MPaG, reflux ratio 5, tower top temperature 68 ℃, tower bottom temperature 100 ℃; The mixture 1 of extraction solvent and unpolymerized monomer (the content of water and ethanol all is less than 0.0005wt%) at the bottom of the tower, The azeotropic mixture 2 of solvent, unpolymerized monomer, ethanol and water is withdrawn from the tower top;
[0068] (2) Wash the azeotropic mixture 2 of the solvent, unpolymerized monomer, ethanol and water extracted from...
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