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Method for preparing tri(1,3-dichloro-2-propyl) phosphonate

A technology of propyl and phosphonic acid, applied in chemical instruments and methods, compounds of Group 5/15 elements of the periodic table, phosphorus organic compounds, etc., can solve the problems of product quality to be improved, flammability, and many by-products, etc. It is easy to achieve large-scale industrial production, reduce reaction steps, and reduce reaction costs.

Active Publication Date: 2018-12-14
SHANDONG TAIHE WATER TREATMENT TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This type of preparation method has serious disadvantages: first, the catalyst itself is unstable, easily decomposed in the air, difficult to separate after the reaction, the catalyst cannot be recycled and reused, and pollutes the environment; secondly, epichlorohydrin is 1,3-di The product of cyclization of chloro-2-propanol is volatile, unstable, potentially carcinogenic, and flammable. Its vapor and air can easily form explosive mixtures, and the reaction between epichlorohydrin and phosphorus oxychloride is an exothermic reaction , has higher requirements on temperature, when the temperature is low, it is easy to accumulate, and when it reaches a certain amount, it is easy to react instantaneously and cause bumping phenomenon, and epichlorohydrin is prone to self-polymerization reaction, resulting in high color of the product and more by-products , low raw material utilization
Again, epichlorohydrin is added dropwise, which is complicated to operate
[0004] Yu Chunhong et al. improved the reaction catalyst by using rare earth solid superacid SO 2- 4 / TiO 2 -Al 2 o 3 / La 3+ Catalyst catalyzes the reaction of epichlorohydrin and phosphorus oxychloride to synthesize phosphonic acid tris (1,3-dichloro-2-propyl) ester. The catalyst has good stability, is easy to recycle and can be reused, but epoxy chloride There are many by-products in the reaction between propane and phosphorus oxychloride, the utilization rate of raw materials is low, and the product quality needs to be improved, which is not conducive to industrial production

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] (1) TiCl 4 Add precipitant concentrated ammonia water to the solution to adjust the pH value of the system to 9~10; filter, wash and dry the obtained titanium hydroxide precipitate, then impregnate it with sulfuric acid or ammonium sulfate for 2 hours; filter, dry, and calcinate at 550°C for 4 hours , ground to get SO 4 2- / TiO 2 catalyst. (2) Phosphorus oxychloride, 1,3-dichloro-2-propanol, and SO 5% of the mass fraction of phosphorus oxychloride with a substance ratio of 1:6 4 2- / TiO 2 The catalyst was added to the reactor at one time, and the temperature was raised to 150°C to react for 4.0 hours. At the same time, the hydrogen chloride gas generated was evaporated within the pressure range of -0.2~0MPa. The crude product was washed with alkali, washed with water, and distilled under reduced pressure to remove water. Under the same operating conditions, The catalyst was recycled 10 times, and the yield of tris(1,3-dichloro-2-propyl) phosphonate was 96.8% based...

Embodiment 2

[0024] ZrCl 4 Add the precipitating agent carbonamide to the solution to adjust the pH value of the system to 9~10; filter, wash, and dry the obtained zirconium hydroxide precipitate, then impregnate it with sulfuric acid or ammonium sulfate for 3 hours; filter, dry, and calcinate at 400°C for 6 hours , ground to get SO 4 2- / ZrO 2 catalyst. (2) Phosphorus oxychloride, 1,3-dichloro-2-propanol, and 6% of the mass fraction of phosphorus oxychloride were SO 4 2- / ZrO 2 The catalyst was added to the reactor at one time, and the temperature was raised to 140°C to react for 5.0 hours. At the same time, the hydrogen chloride gas generated was evaporated within the pressure range of -0.2~0MPa. The crude product was washed with alkali, washed with water, and distilled under reduced pressure to remove water. Under the same operating conditions, The catalyst was recycled 10 times, and the yield of tris(1,3-dichloro-2-propyl) phosphonate was 95.8% based on the amount of phosphorus t...

Embodiment 3

[0026] (1) ZrCl 4 , FeCl 3 The solution is added with concentrated ammonia water as a precipitating agent to adjust the pH value of the system to 9~10; after filtering, washing and drying the precipitated zirconium hydroxide and ferric hydroxide obtained, impregnate with sulfuric acid or ammonium sulfate for 3 hours; Calcined for 6 hours and ground to get SO 4 2- / ZrO 2 -Fe 2 o 3 catalyst. (2) Phosphorus oxychloride, 1,3-dichloro-2-propanol, and 4% SO in mass fraction of phosphorus oxychloride with a substance ratio of 1:5 4 2- / ZrO 2 -Fe 2 o 3 The catalyst was added to the reactor at one time, and the temperature was raised to 120°C to react for 6.0 hours. At the same time, the hydrogen chloride gas generated was evaporated within the pressure range of -0.2~0MPa. The crude product was washed with alkali, washed with water, and distilled to remove water under reduced pressure. Under the same operating conditions, The catalyst was recycled 10 times, and the yield of ...

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PUM

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Abstract

The invention provides a method for preparing tri(1,3-dichloro-2-propyl) phosphonate, which relates to the technical field of a preparation method of a fire retardant. The method adopts a self-made catalyst, and uses phosphorus oxychloride and 1,3-dichloro-2-propanol as a raw material, and adopts the following steps: phosphorus oxychloride, 1,3-1,3-dichloro-2- propanol and the self-made solid acidcatalyst are added to a reaction kettle, the materials are heated to the temperature of 100-160 DEG C for 4-6 hours, the generated hydrogen chloride gas is distilled under vacuum of -0.2-0 MPa, a crude product is washed with alkali, washed with water, and is subjected to underpressure distillation to remove water. A reaction equation is shown as the specification. The raw materials of the invention are easy to obtain, the catalyst has good catalytic performance, the product has high purity, the yield is high, the reaction is mild, the operation is simple, and the product is more suitable forindustrial production.

Description

technical field [0001] The invention belongs to the field of chemical synthesis, and specifically relates to a method for synthesizing phosphonic acid tris(1,3-dichloro-2-propyl) by using a self-made solid acid catalyst to catalyze the reaction of phosphorus oxychloride and 1,3-dichloro-2-propanol ) Preparation method of ester. Background technique [0002] Phosphonic acid tris (1,3-dichloro-2-propyl) ester is an additive general-purpose chlorine-containing and phosphorus-containing flame retardant. Compression performance, the halogen atoms generated by decomposition at high temperature have the function of trapping and burning active free radicals, making highly active hydroxyl or hydrogen atoms generate water or hydrogen, thereby interrupting the chain oxidation reaction. And the thermal decomposition of tris(1,3-dichloro-2-propyl) phosphonate can be converted into glassy polymetaphosphonic acid, forming a solid charcoal layer on the surface of the material to insulate a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07F9/09
CPCC07F9/091
Inventor 周荣奇程终发赵坤王燕平李鹏飞陆久田齐晓婧王东海
Owner SHANDONG TAIHE WATER TREATMENT TECH CO LTD
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