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Preparation process for plasticizer-tributyl citrate

A plasticizer citric acid, production process technology, applied in the direction of carboxylic acid ester preparation, organic compound preparation, chemical recovery, etc., can solve the problem that no recovery and recycling method has been found, large amount of catalyst used, serious corrosion of equipment, etc., Achieve the effect of reducing material consumption, short reaction time and reducing pollution discharge

Inactive Publication Date: 2014-05-14
东营金明工贸有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The traditional production method of tributyl citrate uses concentrated sulfuric acid as a catalyst, which has side reactions such as oxidation, difficult refining, serious equipment corrosion, and environmental pollution.
In recent years, some factories have used p-toluenesulfonic acid as a catalyst, which has a good catalytic effect, but the amount of catalyst used is relatively large, the price is relatively expensive, and no recycling method has been found, and the production cost is relatively high

Method used

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  • Preparation process for plasticizer-tributyl citrate
  • Preparation process for plasticizer-tributyl citrate
  • Preparation process for plasticizer-tributyl citrate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] In the 5 m3 enamel kettle equipped with three-layer paddle agitator, temperature display instrument, esterification tower, condenser, and water separator, 1600kg of butanol was dropped into for the first time (all recovered alcohol in the previous batch was added after 100% discount, and then added Add fresh butanol to 1600kg, accounting for 70% of the total feeding amount), start stirring, add p-toluenesulfonic acid 25kg, activated carbon 8kg, quickly add citric acid monohydrate 1450kg, pass N 2 (N 2 , about 2m3 per hour). Steam through the jacket to make the temperature of the material rise steadily to 125-130°C, slowly add 700kg of fresh butanol for the second time, control the esterification temperature at 125-135°C, the pressure of the kettle is ≤0.015Mpa, and measure the acid value every 30min. When the acid value is ≤2.3mgKOH / g, it is the end point of esterification, and the reaction time is about 7-8 hours. Carry out the first dealcoholization in the esterific...

Embodiment 2

[0027] Except the input amount adjustment of each raw material, all the other reaction parameters are identical with embodiment 1, and detailed experimental data are as follows: .

Embodiment 3

[0029] Except the input amount adjustment of each raw material, all the other reaction parameters are identical with embodiment 1, and detailed experimental data are as follows:

[0030] .

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Abstract

The invention belongs to the field of fine chemical synthesis, and particularly relates to a synthesis process for tributyl citrate. The synthesis process comprises the steps as follows: (1) mixing citric acid monohydrate with n-butyl alcohol, then adding p-toluenesulfonic acid and active carbon, and adding nitrogen for performing esterification reaction to obtain an esterified substance; (2) dealcoholizing the esterified substance for the first time until the flash point is not less than 162 DEG C; (3) dissolving and recovering the p-toluenesulfonic acid in the esterified substance after dealcoholization by water, and adding the separated water phase into the preparation step (1) of next batch for recycling; (4) adding an alkali solution into an oil phase for neutralizing, removing the water phase, and washing the oil phase to be neutral by water; (5) adding the active carbon into the esterified substance after washing, and dealcoholizing again until the flash point is not less than 180 DEG C so as to obtain raw ester; and (6) filtering the raw ester to obtain the tributyl citrate as the industrial product. According to the synthesis process, the esterification reaction conversion rate reaches up to above 99.0%, the yield of the tributyl citrate can reach above 98%, and the unit consumption and the cost are reduced; and the catalyst, namely the p-toluenesulfonic acid has a good catalytic effect, the recovery rate reaches above 75% after the esterification reaction is ended, the p-toluenesulfonic acid can be repeatedly used as the catalyst, the pollution discharge is reduced, and the COD (Chemical Oxygen Demand) and BOD (Biochemical Oxygen Demand) in wastewater are reduced.

Description

technical field [0001] The invention belongs to the field of fine chemical synthesis, and in particular relates to a synthesis process of tributyl citrate. Background technique [0002] Tributyl citrate is a green and environment-friendly plasticizer, widely used in food and medical device packaging, cosmetics, daily necessities and other industries. It has gradually replaced traditionally used phthalates and has become the main plasticizer in the plastics industry. The traditional production method of tributyl citrate uses concentrated sulfuric acid as a catalyst, which has the disadvantages of oxidation and other side reactions, difficult refining, serious equipment corrosion, and environmental pollution. In recent years, some factories have used p-toluenesulfonic acid as a catalyst, which has a good catalytic effect, but the amount of catalyst used is relatively large, and the price is relatively expensive. There is no recovery and recycling method found, and the producti...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C69/704C07C67/08
CPCY02P20/584
Inventor 李建忠张莹李会来
Owner 东营金明工贸有限公司
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