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Processing process for ketene dimer rectification residue

A technology of ketene essence and residue, which is applied in the field of diketene distillation residue treatment process, can solve the problems of waste of resources, high risk factor, inability to effectively recover acetone, etc., and achieve the effect of avoiding pollution and high social value

Active Publication Date: 2009-01-07
安徽天成新材料有限公司
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Problems solved by technology

[0002] The existing treatment method for diketene distillation residue is direct incineration, which has a high risk factor and high pollution, and wastes diketene and acetic anhydride in the recyclables
Patent No. 200610085796.0, the residue is hydrolyzed to effectively recover the active ingredients in the residue. Although a cooling device is used in the hydrolysis process, acetone cannot be recovered effectively. The volatile acetone is accompanied by the generated CO 2 Discharge together, and the residue after hydrolysis is treated as solid waste, which wastes resources and pollutes the environment

Method used

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  • Processing process for ketene dimer rectification residue

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Embodiment Construction

[0014] The specific implementation manner of this invention will be described in detail below in conjunction with embodiment:

[0015] (1), hydrolysis: add 40% acetic acid 600kg in 2000L reaction kettle, hydrolysis temperature is 95 ℃, dropwise add 1200kg diketene rectification residue, stir, make mixing evenly, after dropwise addition, heat insulation with jacket for 1 hour, Obtain 1200kg of 65% acetic acid solution containing about 20% acetone content. A cyclone-type tube condenser was installed on the reaction kettle, and the temperature was lowered with -15°C brine, and the tail gas discharged from the reaction kettle was condensed into a condensate to obtain acetone with a purity of 95%.

[0016] (2), separation: the above-mentioned hydrolyzate is placed in the continuous distillation tower, maintains tower top temperature 55-57 ℃, separates acetone, until there is no obvious discharge, obtains about 100kg of acetone more than 95%.

[0017] (3), mixing, the acetone obtai...

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Abstract

The invention discloses a process for processing diketene rectification residues, which is characterized in that the process comprises the following steps: (1) diluting the diketene rectification residues, hydrolyzing the diluted residues, cooling and recovering the tail gas of the hydrolysis process; (2) recovering acetone in the hydrolytic solution; (3) mixing condensate of the step (1) with acetone recovered in the step (2), mixing with the hydrolytic residues in the step (1) at a ratio and dissolving; and (4) combusting the mixture and emitting without pollution. The process can effectively recover chemical components in the tail gas to prevent the air pollution caused by organic solvents such as acetone, etc. The residues are combusted fully to generate CO2 and water to achieve non-pollution emission, thereby meeting the environmental protection requirements and achieving high social value.

Description

technical field [0001] The invention relates to a treatment process for diketene distillation residue, which belongs to the technical field of chemical industry. Background technique [0002] The existing method for treating diketene distillation residue is direct incineration, which has a high risk factor and great pollution, and wastes diketene and acetic anhydride in the recyclables. Patent No. 200610085796.0, the residue is hydrolyzed to effectively recover the active ingredients in the residue. Although a cooling device is used in the hydrolysis process, acetone cannot be recovered effectively. The volatile acetone is accompanied by the generated CO 2 Discharge together, and the residue after hydrolysis is treated as solid waste, which wastes resources and pollutes the environment. Contents of the invention [0003] In order to overcome the deficiencies of the existing technology, the purpose of this paper is to provide a diketene rectification residue treatment proc...

Claims

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Application Information

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IPC IPC(8): C07C49/08C07C45/78A62D3/38A62D3/35A62D101/20
Inventor 陈正荣陈敏陈正崔惠忠
Owner 安徽天成新材料有限公司
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