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Method for preparing diisobutyl ketone

A technology of diisobutyl ketone and methyl isobutyl ketone, which is applied in the separation/purification of carbonyl compounds, organic chemistry, etc., can solve the problems of inability to be better utilized, low purity, etc., and reduce the steps of operation , Improve distillation efficiency, improve the effect of purity

Active Publication Date: 2016-11-09
ZHEJIANG OCEANKING DEVELOPMENT CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In this process, the enterprise generally sends the mixture with diisobutyl ketone as the main liquid extracted from the tower tank during the production of methyl isobutyl ketone into the rectification tower for rectification treatment, and then The finished product diisobutyl ketone is produced from the side line of the rectification tower, and the purity of diisobutyl ketone obtained therefrom is generally 84-90%, so the purity is generally relatively low and cannot be better utilized

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] The mixture raw material based on the diisobutyl ketone extracted from the tower kettle of the light component tower of methyl isobutyl ketone is transferred to the reaction tank with a flow rate of 500Kg / h; Silica gel desiccant, and stirring, the stirring speed is 100 rpm; the mixture raw material in the reaction tank is filtered through the filter; the filtrate obtained after filtering is transported to the preheater for preheating, and the preheating temperature is up to 76-94°C; transport the preheated filtrate to the rectification tower for rectification, and control the temperature at the top of the tower to 104-126°C, the temperature of the side line to 156-177°C, and the temperature of the bottom of the tower to 167-189°C; The finished diisobutyl ketone is produced from the side line of the rectification tower at 200Kg / h, wherein the finished diisobutyl ketone produced is returned to the reaction tank at 130Kg / h to be mixed with the filtrate, and the rest of the ...

Embodiment 2

[0028] The mixture raw material based on the diisobutyl ketone extracted from the tower kettle of the light component tower of methyl isobutyl ketone is transferred to the reaction tank with a flow rate of 500Kg / h; Silica gel desiccant, and stirring, the stirring speed is 100 rpm; the mixture raw material in the reaction tank is filtered through the filter; the filtrate obtained after filtering is transported to the preheater for preheating, and the preheating temperature is up to 76-94°C; transport the preheated filtrate to the rectification tower for rectification, and control the temperature at the top of the tower to 104-126°C, the temperature of the side line to 156-177°C, and the temperature of the bottom of the tower to 167-189°C; The finished diisobutyl ketone is produced from the side line of the rectification tower at 300Kg / h, among which, the finished diisobutyl ketone produced is returned to the reaction tank at 200Kg / h to be mixed with the filtrate, and the rest of...

Embodiment 3

[0031] The mixture raw material based on the diisobutyl ketone extracted from the tower kettle of the light component tower of methyl isobutyl ketone is transferred to the reaction tank with a flow rate of 500Kg / h; Silica gel desiccant, and stirring, the stirring speed is 100 rpm; the mixture raw material in the reaction tank is filtered through the filter; the filtrate obtained after filtering is transported to the preheater for preheating, and the preheating temperature is up to 76-94°C; transport the preheated filtrate to the rectification tower for rectification, and control the temperature at the top of the tower to 104-126°C, the temperature of the side line to 156-177°C, and the temperature of the bottom of the tower to 167-189°C; The finished diisobutyl ketone is produced from the side line of the rectification tower at 250Kg / h, among which, the finished diisobutyl ketone produced is returned to the reaction tank at 167Kg / h to be mixed with the filtrate, and the rest of...

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PUM

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Abstract

The invention discloses a method for preparing diisobutyl ketone. The method comprises the following steps: 1, transferring a mixture raw material extracted from a tower kettle of a methyl isobutyl ketone light component tower and mainly containing diisobutyl ketone into a reaction tank; 2, adding a silica-gel drier into the reaction tank, and performing stirring at rotating speed of 100 revolutions / min; 3, filtering the mixture raw material in the reaction tank by virtue of a filter; 4, delivering filtrate obtained by filtration into a preheater for preheating at preheating temperature of 76 to 94 DEG C; 5, delivery the preheated filtrate into a rectification tower for rectification, wherein the temperature of the top of the tower is controlled to be 104 to 126 DEG C, the side stream temperature is 156 to 177 DEG C, and the temperature of a tower kettle is 167 to 189 DEG C; 6, producing a diisobutyl ketone finished product from a side stream of the rectification tower, and charging the diisobutyl ketone finished product. According to the method, the temperature difference of boiling points of each substance is increased, and the rectification efficiency of the rectification tower is favorably improved, so that the purity of the diisobutyl ketone is improved on the premise of simplifying a purification process, and the economic benefits of the diisobutyl ketone are further greatly improved.

Description

technical field [0001] The invention relates to chemical raw materials, in particular to a method for preparing diisobutyl ketone. Background technique [0002] Diisobutyl ketone, also commonly known as 2,6-dimethyl-4-heptanone, 4,6-dimethyl-2-heptanone, is a low-toxicity chemical, and inhalation of high concentrations is harmful to the nose and throat It has a irritating effect, and the maximum allowable concentration in the air is 240mg / m3, but this chemical can be used as a solvent for industrial coatings, such as: plastic paint and vacuum plating paint, and is also a solvent for nitrocellulose, acrylic resin, vinyl paint and organic An excellent solvent for dispersants; its main features are non-biting, strong solvency, improved coating leveling, gloss, recoatability and wettability to plastic substrates, and increased adsorption. It can also be used as a dispersant for the manufacture of organic sols, a solvent for food refining, and an intermediate for some drugs and ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C45/82C07C45/78C07C49/04
CPCC07C45/78C07C45/82C07C49/04
Inventor 王时良郑金成谢毅龙章晓麟赵洪彬
Owner ZHEJIANG OCEANKING DEVELOPMENT CO LTD
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