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N-propyl acetate backing material treatment process

A technology of n-propyl acetate and treatment process, which is applied in the field of n-propyl acetate, can solve problems such as the difficult handling of base material, and achieve the effects of reducing production, prolonging service life, and increasing yield

Active Publication Date: 2020-11-17
ZHEJIANG JIANYE CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In order to overcome the problem that the bottom material is difficult to handle in the process of preparing n-propyl acetate with sulfuric acid catalyst, the present invention provides a n-propyl acetate bottom material treatment process, which can process the bottom material with high water content of n-propyl acetate or high sulfuric acid content. material, extending the service life of the n-propyl acetate esterification heater

Method used

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  • N-propyl acetate backing material treatment process
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Examples

Experimental program
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Effect test

Embodiment 1

[0024] The preparation method of the anti-corrosion coating is as follows: first mix and disperse 30 parts of epoxy resin, 20 parts of solvent, and 1 part of dispersant evenly, then add 20 parts of filler to disperse evenly, and then add 0.5 parts of corrosion inhibitor benzotriazole to disperse evenly , to obtain anti-corrosion coatings.

Embodiment 2

[0026] The preparation method of the anti-corrosion coating is: (1) 0.5 parts of corrosion inhibitor benzotriazole, 10 parts of chitosan, 50 parts of curing agent and 10 parts of the solvent are mixed and dispersed uniformly;

[0027] (2) Mix and disperse 30 parts of epoxy resin, 20 parts of solvent and 1 part of dispersant evenly, then add 20 parts of filler to disperse evenly, and then add 0.5 parts of the product of step (1) to disperse evenly to obtain an anti-corrosion coating.

Embodiment 3

[0029] The preparation method of anti-corrosion coating is: (1) get the chitosan of molecular weight 3000, add the chlorobenzenemethane of 0.6eq and the potassium carbonate of 0.3eq, take DMF as solvent, react under heating reflux condition to obtain modified chitosan;

[0030] (2) 1 part of corrosion inhibitor benzotriazole, 20 parts of modified chitosan, 70 parts of curing agent and 20 parts of the solvent are mixed and uniformly dispersed;

[0031] (3) 30 parts of epoxy resin, 20 parts of solvent, and 1 part of dispersant were mixed and dispersed uniformly, then 20 parts of filler were added to disperse uniformly, and then 0.5 parts of the product of step (2) were added to disperse uniformly to obtain an anti-corrosion coating.

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Abstract

The invention relates to the field of n-propyl acetate, and provides an n-propyl acetate backing material treatment process aiming at the problem that a backing material is difficult to treat in a process for preparing n-propyl acetate by adopting a sulfuric acid catalyst, the backing material comprises one or more of sulfuric acid, acetic acid, n-propyl acetate, water and n-propyl alcohol, and the backing material is stored in a backing material storage tank; wherein the bottom material storage tank is connected with the treatment kettle, the bottom material of the treatment kettle is discharged to the circulating pump, the circulating pump conveys the bottom material to the graphite heater for heating, the heated bottom material returns to the treatment kettle, a gas phase outlet in thetreatment kettle is communicated to the treatment tower, the top of the treatment tower is connected with the condenser, and the bottom of the treatment tower is communicated with the circulating pump. According to the invention, the backing material with high n-propyl acetate water content or high sulfuric acid content can be treated, so that the service life of the n-propyl acetate esterification heater is prolonged.

Description

technical field [0001] The invention relates to the field of n-propyl acetate, in particular to a process for treating n-propyl acetate bottom material. Background technique [0002] N-propyl acetate is usually produced by the reaction of acetic acid and n-propanol under the catalysis of concentrated sulfuric acid. The advantages of sulfuric acid catalyst are low catalytic temperature and low energy consumption. For example, patent CN110981721A discloses a "continuous production method of n-propyl acetate": mixing glacial acetic acid and n-propanol as a mixed raw material; first adding a catalyst to the mixed raw material and heating it to 80-108 ° C in the esterification kettle E2 For the esterification reaction, after the reaction starts to distill, the mixed raw materials are continuously injected into the esterification kettle E2; the reacted materials obtained in the esterification kettle E2 enter the esterification tower E1 for separation, and the top of the esterifica...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C67/08C07C67/54C07C69/14C07C29/80C07C31/10C09D163/00C09D5/08
CPCC07C67/08C07C67/54C07C29/80C09D163/00C09D5/08C07C69/14C07C31/10C08L5/08C08K5/3475C08K5/17Y02P20/10
Inventor 冯烈吴方丽陈云斌钱晔崔元存余婉凤王鹏程
Owner ZHEJIANG JIANYE CHEM
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