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A kind of preparation method of high-purity tributyl phosphate

A technology of high-purity tributyl phosphate and pure tributyl phosphate, applied in the field of purification, can solve the problems of low purity, inability to recycle, environmental pollution, etc., and achieve the effects of reducing the amount of alkali, mild conditions, and cost reduction

Active Publication Date: 2017-03-01
成都富鼎鑫瑞科技股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method needs to consume a large amount of alkali, and the neutralization process will also cause the degradation of tributyl phosphate due to the local excessive concentration of alkali, release a large amount of heat, increase energy consumption, and the potassium chloride and sodium chloride solutions produced cannot be recycled. , causing environmental pollution
The conditions of vacuum distillation are harsh, the energy consumption is high, the requirements for equipment are high, and the production cost is high, resulting in low technical and economic value of the process
At present, the yield of tributyl phosphate is lower than 85%, and the purity is not high

Method used

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  • A kind of preparation method of high-purity tributyl phosphate
  • A kind of preparation method of high-purity tributyl phosphate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Add 296.48g (i.e. 4mol) of n-butanol into the esterification kettle, turn on the frozen brine to keep the temperature in the kettle below 10°C, add 76.67g (i.e. 0.5mol) of phosphorus oxychloride dropwise under stirring, and control the reaction temperature at 20°C. ℃-25℃, stirring until the reaction is completed. Add 150 ml of water to the reacted mixture and wash it with a multi-stage water washing tower, and let it stand to separate into layers. The aqueous phase yields a 24.7% hydrochloric acid solution. The organic phase was neutralized to pH 7 with ammonia gas. Ammonium chloride was crystallized from the neutralized aqueous phase, and then solid-liquid separation was performed to obtain 8.475 g of ammonium chloride. The mother liquor returns to the neutralization stage for circulation.

[0029] The organic phase was washed with 200ml of water and the pH was controlled to be 6-7, and the crude dealcoholization was carried out by distillation under the conditions ...

Embodiment 2

[0031] Add 296.48g (i.e. 4mol) of n-butanol into the esterification kettle, turn on the frozen brine to keep the temperature in the kettle below 10°C, add 76.67g (i.e. 0.5mol) of phosphorus oxychloride dropwise under stirring, and control the reaction temperature at 20°C. ℃-25℃, stirring until the reaction is completed. Add 180 ml of water to the reacted mixture and wash it with a multi-stage water washing tower, and let it stand to separate layers. The aqueous phase yields a 27.5% hydrochloric acid solution. The organic phase was neutralized to pH 7 with ammonia gas. Ammonium chloride was crystallized from the neutralized aqueous phase, and then solid-liquid separation was performed to obtain 8.475 g of ammonium chloride. The mother liquor returns to the neutralization stage for circulation.

[0032] The organic phase was washed with 200ml of water and the pH was controlled to be 6-7, and the crude dealcoholization was carried out by distillation under the conditions of 15...

Embodiment 3

[0034] Add 296.48g (i.e. 4mol) of n-butanol into the esterification kettle, turn on the frozen brine to keep the temperature in the kettle below 10°C, add 76.67g (i.e. 0.5mol) of phosphorus oxychloride dropwise under stirring, and control the reaction temperature at 20°C. ℃-25℃, stirring until the reaction is completed. Add 160ml of water to the reacted mixture and wash it with a multi-stage water washing tower, and let it stand to separate layers. The aqueous phase yields a 24.7% hydrochloric acid solution. The organic phase was neutralized to pH 7 with ammonia gas. Ammonium chloride was crystallized from the neutralized aqueous phase, and then solid-liquid separation was performed to obtain 1.695 g of ammonium chloride. The mother liquor returns to the neutralization stage for circulation.

[0035] The organic phase was washed with 200ml of water and the pH was controlled to be 6-7, and the crude dealcoholization was carried out by distillation under the conditions of 15k...

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Abstract

The invention discloses a method for preparing high-purity tributyl phosphate. The method includes steps of enabling butanol and phosphorus oxychloride to react with each other to generate mixtures, carrying out tower washing on the mixtures, layering the mixtures after the mixtures stand still, acquiring 25-28% of hydrochloric acid solution from water phase, neutralizing organic phase by the aid of gaseous ammonia until a pH (potential of hydrogen) value of the organic phase reaches 7, allowing the mixtures to stand still, separating the water phase from the organic phase, crystallizing the water phase, separating solid from liquid to obtain ammonium chloride solid, recycling mother liquid, adding water into the organic phase to wash the organic phase, keeping the pH of 6-7 under the control, coarsely removing alcohol from coarse ester layers under the pressures of 7-15kPa at the temperatures of 80-110 DEG C after the water phase is separated from the organic phase, recycling the most butanol; adding water into the coarse ester layers to be used as entrainers, and carrying out reduced pressure distillation under the conditions of pressures of 7-15kPa and temperatures of 80-110 DEG C; recycling the butanol in distilled mixtures of the butanol and the water; obtaining the high-purity tributyl phosphate from column reactors. A mass ratio of the water added into the coarse ester layers to distillates is 0.5-1.5:1. The method for preparing the high-purity tributyl phosphate has the advantages that consumption of a large quantity of alkali, degradation of the tributyl phosphate and generation of chloride waste liquid can be prevented, conditions of high required pressures and high temperature can be omitted, and energy consumption and the cost can be reduced; the tributyl phosphate obtained by the aid of the method is high in purity, the purity of the tributyl phosphate can reach 99.9% at least, and export-grade requirements can be met.

Description

technical field [0001] The invention relates to a purification method, in particular to a preparation method of high-purity tributyl phosphate. Background technique [0002] Tributyl phosphate is referred to as TBP, and its molecular formula is (C 4 h 9 O) 3 PO, a colorless liquid with a pungent odor, is an important chemical product with a wide range of uses. It can be used as industrial defoamer, plasticizer, metal extractant, solvent extractant, etc. It also has an important use in purifying phosphoric acid. [0003] At present, the industrial production of TBP generally uses butanol and phosphorus oxychloride as raw materials, and reacts at room temperature to obtain tributyl phosphate. The chemical reaction equation is as follows: POCl 3 +3C 4 h 9 OH→(C 4 h 9 O) 3 PO+3HCl [0004] The methods currently used for the purification of tributyl phosphate are: 1. acid-binding method, adding sodium formate (or sodium acetate, sodium butoxide) in advance to remove t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07F9/11
Inventor 李维
Owner 成都富鼎鑫瑞科技股份有限公司
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