CN103570763A - Novel method for synthesizing and purifying phosphonitrilic chloride trimer - Google Patents

Novel method for synthesizing and purifying phosphonitrilic chloride trimer Download PDF

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Publication number
CN103570763A
CN103570763A CN201210254611.XA CN201210254611A CN103570763A CN 103570763 A CN103570763 A CN 103570763A CN 201210254611 A CN201210254611 A CN 201210254611A CN 103570763 A CN103570763 A CN 103570763A
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chlorobenzene
ammonium chloride
purifying
lewis acid
hexa chloro
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CN201210254611.XA
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Chinese (zh)
Inventor
金伊男
陈恒伟
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SHANGHAI YONGHONG INDUSTRY GROUP CHEMICAL TECHNOLOGY CO LTD
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SHANGHAI YONGHONG INDUSTRY GROUP CHEMICAL TECHNOLOGY CO LTD
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Priority to CN201210254611.XA priority Critical patent/CN103570763A/en
Publication of CN103570763A publication Critical patent/CN103570763A/en
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Abstract

The invention discloses a novel method for synthesizing and purifying phosphonitrilic chloride trimer by taking Lewis acid as the catalyst and adopting the sublimation method. The method disclosed by the invention is characterized by comprising the following steps of: synthesizing phosphonitrilic chloride trimer in chlorobenzene as the solvent by selecting Lewis acid as the catalyst and taking ammonium chloride and phosphorus pentachloride as the raw materials, after removing chlorobenzene, dissolving phosphonitrilic chloride trimer by using normal hexane to eliminate linear polymer, and finally, purifying by adopting the sublimation method to obtain phosphonitrilic chloride trimer with the purity of above 99%, wherein the total yield is about 60%. Compared with the prior art, the catalytic system is optimized; the purity of the prepared phosphonitrilic chloride trimer is high; and the novel method disclosed by the invention is applied to industrialized mass production.

Description

A kind of novel method of synthesizing and purifying hexa chloro cyclotripolyphosphazene
Technical field
The present invention relates to a kind of novel method of preparing purifying fine-chemical intermediate, particularly relate to a kind of novel method of synthesizing and purifying hexa chloro cyclotripolyphosphazene, belong to chemical industry synthesizing and purifying field.
Background technology
Phosphazene compound be a class skeleton by the inorganic-organic compound of phosphorus atom and nitrogen-atoms alternative arrangement, can be divided into ring phosphonitrile and polyphosphonitrile.Cyclic phosphazene compound be a class to take the polynary ring of phosphorus nitrogen-atoms alternative arrangement be skeleton, the class inorganics forming by two substituting groups that change on phosphorus atom.Its material qualitative diversity after polymerization is given in the variation of phosphazene compound Side base, as good flame retardant resistance, high temperature resistant, anti-oxidant and organic solvent-resistant etc.At aspects such as material fuel batteries, there is good purposes.Therefore, having development and application values widely, is one of the most rising inorganic macromolecule material.
Hexachlorocyclotriphosphazene is the phosphazene compound obtaining the earliest, and the chlorine on its phosphorus atom is very active, easily by various affinity reagent, is replaced and obtains various not isoplastic cyclic phosphazene compounds.Hexa chloro cyclotripolyphosphazene is the most basic compound in phosphonitrile chemistry, to the development of phosphonitrile chemistry, plays a part very important.
Publication number is traditional preparation method that the patent of US4567028 and CN101157704A discloses hexachlorocyclotriphosphazene, is with PCl 5and NH 4cl is raw material, the pyridine etc. of take is catalyzer, certain hour refluxes in inert solvent, then steam except chlorobenzene, recrystallization obtains product, but in fact adopting pyridine is the recycling that catalyzer is unfavorable for chlorobenzene, and recrystallization cannot remove the cyclic tetramer in system completely, can not get highly purified product.Also have the patent that publication number is US4605539 to adopt washing to remove cyclic tetramer, but to cyclic trimer, also can damage simultaneously, cannot obtain the product that purity is high, yield is also affected.The making method that these are traditional, yield is low, and product purity is low, and cost is high, is not suitable for industrialized production.Therefore, find a technique economical and practical and applicable industrialized production extremely urgent.
Summary of the invention
The object of the invention is the operational path that finds can be applicable to industrialized production, improve the yield of hexa chloro cyclotripolyphosphazene, reduce costs, obtain highly purified hexa chloro cyclotripolyphosphazene product.
The invention provides one can the highly purified hexa chloro cyclotripolyphosphazene of industrialized production novel method, step comprises:
Step 1, in reaction flask, adds appropriate ammonium chloride as reaction medium, take ammonium chloride and phosphorus pentachloride as raw material, and adds a certain amount of Lewis acid as catalyzer, at a certain temperature reacting by heating certain hour;
Step 2, normal pressure evaporates part chlorobenzene, is cooled to 40-50 oafter C, remove by filter unnecessary ammonium chloride, then decompression removes remaining chlorobenzene, be cooled to after room temperature, add n-hexane dissolution hexa chloro cyclotripolyphosphazene, filter to remove linear polymer, decompression is removed hexane solution and is obtained the thick product of hexa chloro cyclotripolyphosphazene.
Step 3, adopts subliming method purifying, obtains purity and reaches more than 99% hexa chloro cyclotripolyphosphazene.
Method as mentioned above, wherein, used catalyst Lewis acid comprises ZnCl 2,feCl 3,alCl 3,coCl 2,mnCl 2,mgCl 2deng.
Method as mentioned above, wherein, temperature of reaction is 100 oc-130 oc, the reaction times is 8-16 hour.
Method as mentioned above, wherein, the consumption of ammonium chloride is 150-160%, the consumption of catalyzer Lewis acid is 0.5-0.6%.
Method as mentioned above, wherein, preferred ZnCl 2for catalyzer.
Method as mentioned above, wherein, preferable reaction temperature is 128 oc.
Method as mentioned above, wherein, the more than 99% hexa chloro cyclotripolyphosphazene yield obtaining is 60%.
In sum, the present invention has been owing to having adopted technique scheme, makes chlorobenzene and the normal hexane can recycling, improved the yield of hexa chloro cyclotripolyphosphazene, reduced cost, obtained highly purified hexa chloro cyclotripolyphosphazene product, economical and practical and applicable industrialized production.
Embodiment
Below by embodiment, specifically describe the present invention, but embodiment does not limit the scope of the invention.
Embodiment 1:
In tri-mouthfuls of reaction flasks of 500 mL, add the ammonium chloride of 20 g, 300 mL chlorobenzenes and 50.8 g phosphorus pentachlorides, and add 0.4 g FeCl 3catalyzer, react on 125 oc thermotonus 8 hours, normal pressure evaporates part chlorobenzene, is cooled to 40-50 oc removes by filter unnecessary ammonium chloride, then decompression removes remaining chlorobenzene, is cooled to room temperature, adds n-hexane dissolution product to filter to remove linear polymer, and decompression is removed hexane solution and obtained the thick product of hexa chloro cyclotripolyphosphazene.By sublimation purification, obtain more than 99% hexa chloro cyclotripolyphosphazene 10 g, yield 35%.
Embodiment 2:
In tri-mouthfuls of reaction flasks of 500 mL, add the ammonium chloride of 20 g, 300 mL chlorobenzenes and 50.8 g phosphorus pentachlorides, and add 0.4 g AlCl 3catalyzer, react on 125 oc thermotonus 8 hours, normal pressure evaporates part chlorobenzene, is cooled to 40-50 oc removes by filter unnecessary ammonium chloride, then decompression removes remaining chlorobenzene, is cooled to room temperature, adds n-hexane dissolution product to filter to remove linear polymer, and decompression is removed hexane solution and obtained the thick product of hexa chloro cyclotripolyphosphazene.By sublimation purification, obtain more than 99% hexa chloro cyclotripolyphosphazene 12 g, yield 42%.Embodiment 3:
In tri-mouthfuls of reaction flasks of 5 L, add the ammonium chloride of 200 g, 3000 mL chlorobenzenes and 500 g phosphorus pentachlorides, and add 2.0 g ZnCl 2catalyzer, react on 128 oc thermotonus 15 hours, normal pressure evaporates part chlorobenzene, is cooled to 40-50 oc removes by filter unnecessary ammonium chloride, then decompression removes remaining chlorobenzene, is cooled to room temperature, adds n-hexane dissolution product to filter to remove linear polymer, and decompression is removed hexane solution and obtained the thick product of hexa chloro cyclotripolyphosphazene.By sublimation purification, obtain more than 99% hexa chloro cyclotripolyphosphazene 166 g, yield 60%.
Embodiment 4:
In tri-mouthfuls of reaction flasks of 5 L, add the ammonium chloride of 200 g, 3000 mL chlorobenzenes (embodiment 2 reclaims chlorobenzene) and 500 g phosphorus pentachlorides, and add 2.0 g ZnCl 2catalyzer, react on 128 oc thermotonus 15 hours, normal pressure evaporates part chlorobenzene, is cooled to temperature 40-50 oc removes by filter unnecessary ammonium chloride, then decompression removes remaining chlorobenzene, is cooled to room temperature, adds normal hexane (embodiment 2 reclaim normal hexanes) dissolved product to filter to remove linear polymer, and decompression is removed hexane solution and obtained the thick product of hexa chloro cyclotripolyphosphazene.By sublimation purification, obtain more than 99% hexa chloro cyclotripolyphosphazene 164 g, yield 58%.
Above specific embodiments of the invention be have been described in detail, but it is just as example, the present invention is not restricted to specific embodiment described above.To those skilled in the art, any equivalent modifications that the present invention is carried out and alternative also all among category of the present invention.Therefore, equalization conversion and the modification done without departing from the spirit and scope of the invention, all should contain within the scope of the invention.

Claims (7)

1. a novel method for synthesizing and purifying hexa chloro cyclotripolyphosphazene, is characterized in that, step comprises:
Step 1, take ammonium chloride and phosphorus pentachloride as raw material, take Lewis acid as catalyzer, at a certain temperature reacting by heating certain hour in chlorobenzene medium;
Step 2, removes after chlorobenzene and unnecessary ammonium chloride, with n-hexane dissolution hexa chloro cyclotripolyphosphazene, removes linear polymer, and decompression is removed hexane solution and obtained the thick product of hexa chloro cyclotripolyphosphazene;
Step 3, adopts subliming method purifying, obtains purity and reaches more than 99% hexa chloro cyclotripolyphosphazene.
2. method according to claim 1, is characterized in that, used catalyst Lewis acid comprises ZnCl 2,feCl 3,alCl 3,coCl 2,mnCl 2,mgCl 2deng.
3. method according to claim 1, is characterized in that, temperature of reaction is 100 oc-130 oc, the reaction times is 8-16 hour.
4. method according to claim 1, is characterized in that, the consumption of ammonium chloride is 150-160%, and the consumption of catalyzer Lewis acid is 0.5-0.6%.
5. method according to claim 1, is characterized in that, the method for removing chlorobenzene and unnecessary ammonium chloride is: normal pressure evaporates part chlorobenzene, is cooled to 40-50 oafter C, remove by filter unnecessary ammonium chloride, then decompression remove remaining chlorobenzene, be then cooled to room temperature.
6. Lewis acid according to claim 2, is characterized in that ZnCl 2for catalyzer.
7. temperature of reaction according to claim 3, is characterized in that, temperature of reaction is 128 oc.
CN201210254611.XA 2012-07-23 2012-07-23 Novel method for synthesizing and purifying phosphonitrilic chloride trimer Pending CN103570763A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104558044A (en) * 2015-02-13 2015-04-29 湖北诺邦科技股份有限公司 Synthesis method of hexachlorocyclotriphosphazene

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US4382914A (en) * 1980-06-11 1983-05-10 Nippon Fine Chemical Company, Ltd. Process for preparing cyclic phosphonitrilic chloride oligomers
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CN1916007A (en) * 2006-09-13 2007-02-21 上海氯碱化工股份有限公司 Preparing hexachlorocyclotriphosphazene, and purification method
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US4382914A (en) * 1980-06-11 1983-05-10 Nippon Fine Chemical Company, Ltd. Process for preparing cyclic phosphonitrilic chloride oligomers
CN1850832A (en) * 2006-05-23 2006-10-25 郑州大学 Catalytic synthesizing method of hexa chloro cyclotripolyphosphazene
CN1916007A (en) * 2006-09-13 2007-02-21 上海氯碱化工股份有限公司 Preparing hexachlorocyclotriphosphazene, and purification method
CN101157704A (en) * 2007-11-08 2008-04-09 河北大学 Method for micro-wave synthesis of hexachloride ring polyphosphazenes
CN101602780A (en) * 2009-06-26 2009-12-16 四川东材科技集团股份有限公司 The process for catalytic synthesis of hexachlorocyclotriphosphazene
CN102070672A (en) * 2011-01-18 2011-05-25 宁波职业技术学院 Method for preparing hexachlorocyclotriphosphazene

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104558044A (en) * 2015-02-13 2015-04-29 湖北诺邦科技股份有限公司 Synthesis method of hexachlorocyclotriphosphazene

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Application publication date: 20140212