CN110240614A - A kind of chemical synthesis process of diphenyl phosphate chloride - Google Patents

A kind of chemical synthesis process of diphenyl phosphate chloride Download PDF

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Publication number
CN110240614A
CN110240614A CN201910473644.5A CN201910473644A CN110240614A CN 110240614 A CN110240614 A CN 110240614A CN 201910473644 A CN201910473644 A CN 201910473644A CN 110240614 A CN110240614 A CN 110240614A
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CN
China
Prior art keywords
diphenyl phosphate
chloride
chemical synthesis
synthesis process
certain amount
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CN201910473644.5A
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Chinese (zh)
Inventor
张文杰
王尚启
李娟�
尚杰超
丁红军
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Heze Di Czech Chemical Industry Ltd By Share Ltd
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Heze Di Czech Chemical Industry Ltd By Share Ltd
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Priority to CN201910473644.5A priority Critical patent/CN110240614A/en
Publication of CN110240614A publication Critical patent/CN110240614A/en
Priority to PCT/CN2019/119001 priority patent/WO2020244162A1/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/06Phosphorus compounds without P—C bonds
    • C07F9/08Esters of oxyacids of phosphorus
    • C07F9/09Esters of phosphoric acids
    • C07F9/14Esters of phosphoric acids containing P(=O)-halide groups
    • C07F9/1406Esters of phosphoric acids containing P(=O)-halide groups containing the structure Hal-P(=O)-O-aryl

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)

Abstract

The present invention relates to a kind of synthetic methods of diphenyl phosphate chloride, the following steps are included: using a certain amount of organic amine as catalyst, 1-10h is reacted in organic solvent with a certain amount of two (trichloromethyl) carbonic esters after one of a certain amount of diphenyl phosphate or diphenyl phosphate salt or two kinds are mixed with arbitrary proportion, the reaction temperature is 0-60 DEG C, and the diphenyl phosphate salt is any one of diphenyl phosphate sodium salt or diphenyl phosphate sylvite;To above-mentioned steps 1) in after reaction, by product cooling washing, dry, normal pressure or solvent is recovered under reduced pressure, cooling is filtered to remove insoluble matter and diphenyl phosphate chloride is made.It is simple that the beneficial effects of the invention are as follows process routes, and reaction condition is mild, and post-processing energy consumption is small, and without high vacuum, high temperature distillation, production cost is low, product yield and all higher advantage of quality, and avoids lead to the problem of a large amount of phosphorus-containing wastewaters and solid waste simultaneously.

Description

A kind of chemical synthesis process of diphenyl phosphate chloride
Technical field
The present invention relates to chemical technology field more particularly to a kind of chemical synthesis process of diphenyl phosphate chloride.
Background technique
Diphenyl phosphate chloride is for synthesizing penem-like pharmaceutical, phosphonium flame retardant and the important intermediate of liquid crystal material, such as Drug Meropenem and 4- biphenylyloxy diphenyl phosphate etc. are produced with it.
Before the present invention provides, the chemical synthesis process of diphenyl phosphate chloride is mostly with phosphorus oxychloride and benzene in the prior art Phenol is raw material, is synthesized under Louis acid catalysis.
Synthetic route is as follows:
What is such as: chemical research 2012,23(6) proposed is warming up to 60 DEG C with 0.8g aluminum trichloride (anhydrous) and 15.3g phosphorus oxychloride, to The mixed liquor of 10ml dichloroethanes and 18.8g phenol is added dropwise in reaction system, 70 DEG C of temperature control is added dropwise hereinafter, drop, which finishes, is warming up to 70 DEG C, insulation reaction 15 hours, suitable quantity of water is added dropwise, filtering, low boilers are evaporated off in filtrate elder generation normal pressure, then are evaporated under reduced pressure, collection 140~ 160 DEG C/3mmHg fraction.
The process has used phosphorus oxychloride, severe corrosion to equipment, and a large amount of high phosphorus waste water are difficult to handle, and pollution is tight Weight;The process byproducts are more simultaneously, need high vacuum high temperature distillation product, energy consumption is high, bottoms generate a large amount of solid wastes. The problems such as this method the problems such as there are high corrosion, high energy consumption, high pollutions, yield is low, high production cost, is badly in need of solving.
Summary of the invention
In view of the deficiencies of the prior art, the present invention relates to a kind of chemical synthesis process of diphenyl phosphate chloride, this method tools Standby simple process, the feature of working condition mildly, in high yield, inexpensive, the three wastes are few.
To achieve the above object, the invention provides the following technical scheme:
A kind of synthetic method of diphenyl phosphate chloride, which comprises the following steps:
1) using a certain amount of organic amine as catalyst, by one of a certain amount of diphenyl phosphate or diphenyl phosphate salt or Two kinds mixed with arbitrary proportion after with a certain amount of two (trichloromethyl) carbonic esters react 1-10h in organic solvent, it is described Reaction temperature is 0-60 DEG C, and the diphenyl phosphate salt is any in diphenyl phosphate sodium salt or diphenyl phosphate sylvite Kind;
2) to above-mentioned steps 1) in after reaction, by product cooling washing, dry, normal pressure or solvent is recovered under reduced pressure, cools down It is filtered to remove insoluble matter and diphenyl phosphate chloride is made.
Its reaction equation is as follows:
Or
Wherein, M=sodium or potassium
The step 1) is by one of a certain amount of diphenyl phosphate or diphenyl phosphate salt or two kinds with arbitrary proportion 3-6h is reacted in organic solvent with a certain amount of two (trichloromethyl) carbonic esters after mixing.
Product described in the step 2) is cooled to 10 DEG C or less and is washed, dried, normal pressure or is recovered under reduced pressure Solvent, cooling are filtered to remove insoluble matter and diphenyl phosphate chloride are made.
The diphenyl phosphate (or diphenyl phosphate salt): two (trichloromethyl) carbonic esters: the object of organic amine catalyst The amount ratio of matter is 1:0.35-1.0:0.01-1.5.
The diphenyl phosphate (or diphenyl phosphate salt): two (trichloromethyl) carbonic esters: the object of organic amine catalyst The amount ratio of matter is 1:0.35-0.5:0.1-0.5.
The organic amine catalyst is one of following or more than one arbitrary proportion mixtures: triethylamine, diisopropyl Ethamine, pyridine, morpholine, imidazoles, 2-methylimidazole, tetramethylguanidine, tetramethylurea, n,N-Dimethylformamide, N, N- dimethyl Acetamide, N, N- dibutyl formamide, N- methylpyrrole, N- methyl nafoxidine.
The organic amine catalyst is n,N-Dimethylformamide.
The organic solvent is one of following or more than one arbitrary proportion mixtures: benzene,toluene,xylene, chlorobenzene, Dichloro-benzenes, n-hexane, hexamethylene, Di Iso Propyl Ether, dibutyl ethers, tetrahydrofuran, ethyl acetate, methylene chloride, chloroform Or dichloroethanes.
The organic solvent is methylene chloride.
The consumption of organic solvent is 3-8 times of diphenyl phosphate or diphenyl phosphate salt quality, is lower than this dosage object Material reaction is insufficient, will cause increased costs, reaction efficiency decline higher than this dosage.
Compared with prior art, the beneficial effects of the present invention are: with diphenyl phosphate (or diphenyl phosphate salt) and two (three Chloromethyl) carbonic ester is raw material, synthesize diphenyl phosphate chloride under organic amine catalysis, this programme instead of it is existing with phenol and Phosphorus oxychloride is the synthetic method of raw material, is compared compared with scheme, and technical solution used herein has process route letter Single, reaction condition is mild, and post-processing energy consumption is small, and without high vacuum, high temperature distillation, production cost is low, and product yield and quality are all Higher advantage, and avoid lead to the problem of a large amount of phosphorus-containing wastewaters and solid waste simultaneously, the synthetic method of the diphenyl phosphate chloride With biggish economic value and the value of environmental protection.
Specific embodiment
The following is a clear and complete description of the technical scheme in the embodiments of the invention, it is clear that described embodiment Only a part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, the common skill in this field Art personnel every other embodiment obtained without making creative work belongs to the model that the present invention protects It encloses.
Embodiment 1
120g methylene chloride, 7.3g are put into equipped with tetra- mouthfuls of thermometer, reflux condensing tube and churned mechanically 500ml reaction flasks N,N-Dimethylformamide, stirring 10 DEG C of temperature control hereinafter, investment 28g bis- (trichloromethyl) carbonic ester, stream be added 50g di(2-ethylhexyl)phosphate The solution of phenyl ester and 120g methylene chloride, finishes, and reacts 3 hours, and after reaction, 10 DEG C of temperature control hereinafter, be slowly added to for detection Water 20g, stirs liquid separation, and organic phase is dry with anhydrous sodium sulfate;It is filtered to remove desiccant, methylene chloride is evaporated off in filtrate normal pressure, drop Temperature is filtered to remove insoluble matter to 0 DEG C, obtains diphenyl phosphate chloride 48.9g, and GC detects purity 99.2%, yield 90.3%.
Embodiment 2
120g methylene chloride, 3.6g are put into equipped with tetra- mouthfuls of thermometer, reflux condensing tube and churned mechanically 500ml reaction flasks N,N-Dimethylformamide, stirring 10 DEG C of temperature control hereinafter, investment 28g bis- (trichloromethyl) carbonic ester, stream be added 50g di(2-ethylhexyl)phosphate The solution of phenyl ester and 120g methylene chloride, finishes, and reacts 3 hours, and after reaction, 10 DEG C of temperature control hereinafter, be slowly added to for detection Water 20g, stirs liquid separation, and organic phase is dry with anhydrous sodium sulfate;It is filtered to remove desiccant, methylene chloride is evaporated off in filtrate normal pressure, drop Temperature is filtered to remove insoluble matter to 0 DEG C, obtains diphenyl phosphate chloride 47.2g, and GC detects purity 98.1%, yield 86.2%.
Embodiment 3
330g methylene chloride, 7.3g are put into equipped with tetra- mouthfuls of thermometer, reflux condensing tube and churned mechanically 500ml reaction flasks N,N-Dimethylformamide, stirring 10 DEG C of temperature control hereinafter, investment 28g bis- (trichloromethyl) carbonic ester, 55g phosphoric acid is added portionwise Hexichol ester sodium salt, finishes, and reacts 5 hours, and after reaction, 10 DEG C of temperature control stirs liquid separation hereinafter, be slowly added to water 20g for detection, Organic phase is dry with anhydrous sodium sulfate;It is filtered to remove desiccant, methylene chloride is evaporated off in filtrate normal pressure, is cooled to 0 DEG C, is filtered to remove Insoluble matter, obtains diphenyl phosphate chloride 47.5g, and GC detects purity 99.3%, yield 87.8%.
It should also be noted that, the terms "include", "comprise" or its any other variant are intended to nonexcludability It include so that the process, method, commodity or the equipment that include a series of elements not only include those elements, but also to wrap Include other elements that are not explicitly listed, or further include for this process, method, commodity or equipment intrinsic want Element.In the absence of more restrictions, the element limited by sentence "including a ...", it is not excluded that including element There is also other identical elements in process, method, commodity or equipment.
Although the present invention is described in detail referring to the foregoing embodiments, for those skilled in the art, It is still possible to modify the technical solutions described in the foregoing embodiments, or part of technical characteristic is carried out etc. With replacement, all within the spirits and principles of the present invention, any modification, equivalent replacement, improvement and so on should be included in this Within the protection scope of invention.

Claims (10)

1. a kind of synthetic method of diphenyl phosphate chloride, which comprises the following steps:
1) using a certain amount of organic amine as catalyst, by one of a certain amount of diphenyl phosphate or diphenyl phosphate salt or Two kinds mixed with arbitrary proportion after with a certain amount of two (trichloromethyl) carbonic esters react 1-10h in organic solvent, it is described Reaction temperature is 0-60 DEG C, and the diphenyl phosphate salt is any in diphenyl phosphate sodium salt or diphenyl phosphate sylvite Kind;
2) to above-mentioned steps 1) in after reaction, by product cooling washing, dry, normal pressure or solvent is recovered under reduced pressure, cools down It is filtered to remove insoluble matter and diphenyl phosphate chloride is made.
2. a kind of chemical synthesis process of diphenyl phosphate chloride as described in claim 1, it is characterised in that the step 1) After one of a certain amount of diphenyl phosphate or diphenyl phosphate salt or two kinds are mixed with arbitrary proportion with it is a certain amount of Two (trichloromethyl) carbonic esters react 3-6h in organic solvent.
3. a kind of chemical synthesis process of diphenyl phosphate chloride as described in claim 1, it is characterised in that the step 2) Described in product be cooled to 10 DEG C or less and washed, dried, normal pressure or solvent being recovered under reduced pressure, cooling is filtered to remove insoluble Diphenyl phosphate chloride is made in object.
4. a kind of chemical synthesis process of diphenyl phosphate chloride as described in claim 1, it is characterised in that the di(2-ethylhexyl)phosphate Phenyl ester (or diphenyl phosphate salt): two (trichloromethyl) carbonic esters: the mass ratio of the material of organic amine catalyst is 1:0.35-1.0: 0.01-1.5。
5. a kind of chemical synthesis process of diphenyl phosphate chloride as claimed in claim 4, it is characterised in that the di(2-ethylhexyl)phosphate Phenyl ester (or diphenyl phosphate salt): two (trichloromethyl) carbonic esters: the mass ratio of the material of organic amine catalyst is 1:0.35-0.5: 0.1-0.5。
6. a kind of chemical synthesis process of diphenyl phosphate chloride as described in claim 1, it is characterised in that the organic amine Catalyst is one of following or more than one arbitrary proportion mixtures: triethylamine, diisopropylethylamine, pyridine, morpholine, imidazoles, 2-methylimidazole, tetramethylguanidine, tetramethylurea, n,N-Dimethylformamide, n,N-dimethylacetamide, N, N- dibutyl formyl Amine, N- methylpyrrole, N- methyl nafoxidine.
7. a kind of chemical synthesis process of diphenyl phosphate chloride as claimed in claim 6, it is characterised in that the organic amine Catalyst is n,N-Dimethylformamide.
8. a kind of chemical synthesis process of diphenyl phosphate chloride as described in claim 1, it is characterised in that described is organic molten Agent is one of following or more than one arbitrary proportion mixtures: benzene,toluene,xylene, chlorobenzene, dichloro-benzenes, n-hexane, hexamethylene Alkane, Di Iso Propyl Ether, dibutyl ethers, tetrahydrofuran, ethyl acetate, methylene chloride, chloroform or dichloroethanes.
9. a kind of chemical synthesis process of diphenyl phosphate chloride as claimed in claim 8, it is characterised in that described is organic molten Agent is methylene chloride.
10. a kind of chemical synthesis process of diphenyl phosphate chloride as described in any one of claim 1-9, it is characterised in that The consumption of organic solvent is 3-8 times of diphenyl phosphate or diphenyl phosphate salt quality.
CN201910473644.5A 2019-06-01 2019-06-01 A kind of chemical synthesis process of diphenyl phosphate chloride Pending CN110240614A (en)

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CN201910473644.5A CN110240614A (en) 2019-06-01 2019-06-01 A kind of chemical synthesis process of diphenyl phosphate chloride
PCT/CN2019/119001 WO2020244162A1 (en) 2019-06-01 2019-11-15 Chemical synthesis method of diphenyl chlorophosphate

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020244162A1 (en) * 2019-06-01 2020-12-10 菏泽帝捷化工股份有限公司 Chemical synthesis method of diphenyl chlorophosphate

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JP5212665B2 (en) * 2008-03-11 2013-06-19 国立大学法人 奈良先端科学技術大学院大学 Photolabile protecting group
CN106810575A (en) * 2017-03-03 2017-06-09 常州沃腾化工科技有限公司 A kind of preparation method of chlorinated diphenyl phosphate

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CN105037419B (en) * 2015-09-10 2017-08-25 巨野帝捷化工有限公司 A kind of preparation method of chlorination diphenyl phosphate
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JP5212665B2 (en) * 2008-03-11 2013-06-19 国立大学法人 奈良先端科学技術大学院大学 Photolabile protecting group
CN102408364A (en) * 2010-09-26 2012-04-11 中化蓝天集团有限公司 Method for preparing paratoluensulfonyl chloride
CN106810575A (en) * 2017-03-03 2017-06-09 常州沃腾化工科技有限公司 A kind of preparation method of chlorinated diphenyl phosphate

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020244162A1 (en) * 2019-06-01 2020-12-10 菏泽帝捷化工股份有限公司 Chemical synthesis method of diphenyl chlorophosphate

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Application publication date: 20190917