CN1468838A - Prepn process of 2,6-dichloro-4-trifluoro methylaniline - Google Patents

Prepn process of 2,6-dichloro-4-trifluoro methylaniline Download PDF

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CN1468838A
CN1468838A CNA02132607XA CN02132607A CN1468838A CN 1468838 A CN1468838 A CN 1468838A CN A02132607X A CNA02132607X A CN A02132607XA CN 02132607 A CN02132607 A CN 02132607A CN 1468838 A CN1468838 A CN 1468838A
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浩 吴
吴浩
杨春河
黄耀师
谢春艳
李永惠
关山月
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Shenyang Sinochem Agrochemicals R&D Co Ltd
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Abstract

The preparation process of 2, 6-dichloro-4-trifluoro methylaniline with 3, 4-dichloro trifluoro toluene as initial material and dimethylamine as methylaminating agent includes four reaction steps of dimethylamination, halogenation, catalytic side chain methyl halogenation and hydrolysis. The said process is easy to realize in industrial production and has easy-to-obtain material, high yield and high product purity.

Description

A kind of preparation 2, the novel method of 6-dichlor-4-trifluoromethyl aniline
Technical field: the present invention relates to the new preparation method of a kind of many halogen aromatic amines, specifically, the invention provides a kind of novel process that is suitable for industrial preparation multi-halogenated aniline.
Background technology: 2, the 6-dichlor-4-trifluoromethyl aniline is a kind of important pesticide intermediate, is used to prepare pyrazole compound 5-amino-1-aryl-3-cyano pyrazole for example that insecticidal activity is arranged.In the prior art 2, the 6-dichlor-4-trifluoromethyl aniline has multiple preparation method: as US4, and 096,185; US4 has explained making 4-5-trifluoromethylaniline post chlorization by 4-chloro-phenylfluoroform and ammonia gas react and obtain in 388,472.This method needs high temperature, reaction under high pressure, is catalyzer with similar cuprous chloride and Potassium monofluoride mixture, and yield and transformation efficiency are all undesirable.2, the 6-dichlor-4-trifluoromethyl aniline also can be as EP0, and 384,392; US5 makes the 4-4-trifluoromethylbenzonitrile by 4-chloro-phenylfluoroform and sodium cyanide reaction described in 410,082, makes the 4-5-trifluoromethylaniline through hydrolysis and hoffman degradation reaction, and chlorination makes again.This method step long and the prussiate of use severe toxicity and the Ni (PPh that is difficult to prepare 3) 2Cl 2, technology is comparatively complicated, and yield is lower.Explained by 3 among the WO 00/59862, hydrogenation made 2-chloro-4-5-trifluoromethylaniline after 4-two chlorobenzotrifluorides and hydrazine hydrate reaction made 2-chloro-4-trifluoromethyl phenyl hydrazine, and chlorination makes 2 again, the method for 6-dichlor-4-trifluoromethyl aniline.The employed hydrazine hydrate explosive of this method, pyridine are made the solvent costliness and are had strong stink; Make in addition that pressure is difficult to control in the reaction process of 2-chloro-4-5-trifluoromethylaniline.US5 has explained with N in 401,882, and dinethylformamide is done the methylamine agent and obtained 2, and 6-two chloro-4-methyl fluoride-N, make 2 with sodium-hydroxide treatment, the method for 6-dichlor-4-trifluoromethyl aniline at accelerine after the ultraviolet lighting chlorination; Though halogenation and pendant methyl halogenation can be carried out under UV-irradiation, and light intensity and wavelength are had particular requirement, its suitability for industrialized production is had difficulties; The insolubles that produces influences illumination in the reaction process in addition, causes reaction later stage speed slow, is unfavorable for industrialization.While N, the dinethylformamide price is also more expensive.In sum, there are 3 deficiencies in prior art in preparation 2 in the method for 6-dichlor-4-trifluoromethyl aniline: 1, technology is complicated, and the industrialization difficulty is bigger; 2, raw material ratio is than costliness or poor stability; 3, reaction conversion ratio and product yield are lower.
Summary of the invention: in order to overcome deficiency of the prior art, inventors of the present invention develop one be easy to that industrialization, raw material are cheap and easy to get, reaction yield and product content are more high-new 2, the preparation method of 6-dichlor-4-trifluoromethyl aniline.
Provided by the invention 2, the preparation method of 6-dichlor-4-trifluoromethyl aniline (Compound I) comprises four-step reaction:
(1) diformazan amination reaction:
Figure A0213260700051
Compound (VII) compound (VI) (2) halogenating reaction:
Compound (V) compound (IV) (3) pendant methyl halogenating reaction:
Compound (III) (4) hydrolysis reaction
Figure A0213260700054
Compound (II)
Figure A0213260700055
Compound (I)
Inventors of the present invention select suitable catalyzer for use, replace N with low-cost dimethylamine in the diformazan amination reaction, the N dimethyl formamide is in order to preparation N, accelerine compounds.Reaction pressure is stable, helps suitability for industrialized production.
In the diformazan amination reaction, in 1 mole compound (VII): add 1-20 mole dimethylamine, suitable be the 4-8 mole, preferably the 4-5 mole.
This is reflected under two kinds of catalyzer existence and carries out: catalyst A is selected from alkali-metal halogenide, as iodine, bromine or the villiaumite of potassium, sodium or caesium, and preferred potassiumiodide or sodium iodide; Catalyst B is selected from phase-transfer catalyst such as quaternary amine, quaternary alkylphosphonium salt, crown ether, open chain glymes, preferred benzyltriethylammoinium chloride.The catalyst A add-on is the 0.1-10% of starting compound (VII) weight, preferred 0.5-1.5%; The catalyst B add-on is the 0.1-10% of starting compound (VII) weight, preferred 2-4%.
Reaction is carried out in the presence of solvent usually, can select water, alcohol, acetonitrile, N usually, dinethylformamide or dioxane isopolarity solvent; Preferred inexpensive and easily and the isolating C of product 1-C 6Alcohols is made solvent; Further preferred dehydrated alcohol.Reaction also can be carried out under solvent-free situation.
The reaction pair temperature range requires not strict, and be reflected between the 100-250 ℃ of temperature and all can carry out, be 150-220 ℃ than optimal temperature, preferred 190-195 ℃.
Reaction pressure is decided with temperature of reaction is different with coefficient.Usually reaction pressure is 0.8-8Mpa, and that suitable is 2-5Mpa, preferred 3.5-4Mpa.
Reaction times was generally 3-24 hour, preferred 6-15 hour, most preferably was 8-12 hour.
Another notable feature of the present invention is to use initiator to replace ultraviolet lighting to carry out the pendant methyl halogenation, and in same reactor, under than the demulcent condition, carry out halogenation and pendant methyl halogenation, improved reaction yield, thereby make preparation 2, the method for 6-dichlor-4-trifluoromethyl aniline is realized industrially scalable smoothly.
The available halogenating agent scope of halogenation and pendant methyl halogenation is very wide: can use halogen, as Cl 2, Br 2Deng, preferred Cl 2Also can use the halogenation sulfone, as the chlorination sulfone, bromination sulfone, preferred chlorination sulfone; Can also use Phosphorates phosphorus Halides reagent such as phosphorus pentachloride, phosphorus trichloride; Perhaps use as the N-bromo-succinimide free radical reaction reagent of N-chlorosuccinimide class; And the mix reagent of above any halogenating agent.
In same reactor, carry out halogenation and pendant methyl halogenating reaction, in 1 mole compound (VI): add 3-10 mole halogenating agent; When using the halogenation sulfone, preferably add 4 moles as halogenating agent; When using halogen, preferably add the 4-5 mole as halogenating agent.
The pendant methyl halogenation need be carried out under the initiator catalytic condition, and its initiator can be radical initiators such as peroxide, percarboxylate class, azo-compound class as Diisopropyl azodicarboxylate, benzoyl peroxide; Preferred Diisopropyl azodicarboxylate.The initiator add-on is the 0.1-10% of raw material weight, preferred 2-4%.
Halogenation and pendant methyl halogenating reaction are carried out in the presence of the solvent of free radical reaction can be used for usually.As acetonitrile, methylene dichloride, ethylene dichloride, 1,1,2,2, inertia halohydrocarbon and aromatic hydrocarbons such as-tetrachloroethane, chlorobenzene, dichlorobenzene, trichlorobenzene; Suitable is the lower halogenated hydrocarbon, as tetracol phenixin, methylene dichloride, ethylene dichloride, 1,1,2,2 ,-tetrachloroethane; Preferred tetracol phenixin.The consumption of solvent is generally: every kilomol raw material adds 0.1-2 kilolitre solvent; Preferred 0.5-1.5; Most preferably be 1-1.2.Reaction also can be carried out under solvent-free.
The halogenated temperature of reaction of halogenation and pendant methyl is 0-100 ℃, preferred 40-80 ℃; Reaction times is 1-10 hour, preferred 3-8 hour.
Hydrolysis reaction can carry out according to a conventional method.Usually with alcohol or water as medium, preferably under water medium, carry out.Reaction system can be acid, neutral or alkaline, preferred alkalescence.Usually used alkali is: alkali metal hydroxide, and alkaline carbonate, alkali metal acetate, ammoniacal liquor, or phosphoric acid hydrogen disalt etc., preferred sodium hydroxide or potassium hydroxide.
The pendant methyl halogenation preferentially generates the product that each halogen atom of N-methyl replaces, and also produces the many halogenated product of a certain amount of N-methyl in the reaction process, the more single halo difficulty of its hydrolysis reaction.Compound described in the present invention (VI) is easy to Quantitative yield and becomes compound (I) 2,6-dichlor-4-trifluoromethyl aniline.Hydrolysis reaction can produce formaldehyde, or produces by products such as formic acid and methyl alcohol by formaldehyde disproportionation under alkaline condition, all can wash and remove.
The purpose product can separate with ordinary method and obtain, and for example can obtain 2 by wet distillation, 6-dichlor-4-trifluoromethyl aniline crude product, and rectifying afterwards can obtain content greater than 98% product.
Adopt present method preparation 2, the most significant advantage of 6-dichlor-4-trifluoromethyl aniline is: technology is simple, reaction conditions relaxes and is easy to industrialization.Select for use raw material cheap and easy to get.The reaction yield height.
Embodiment: following embodiment is used to illustrate the present invention, but the present invention is not limited only to following embodiment.Embodiment 1:
2-chloro-4-trifluoromethyl-N, the preparation of accelerine:
Drop into 200g 98%3,4-two chloro-4-phenylfluoroforms, anhydrous potassiumiodide 2g to the 1000ml autoclave, anhydrous benzyltriethylammoinium chloride 6g, the 200g dimethylamine is dissolved in 500ml solution that dehydrated alcohol is joined, and is warming up to 195-200 ℃ of reaction, and reaction is 8-9 hour under this temperature, chromatogram tracking to raw material is finishing reaction below 1%, cooling discharge gets 204g 2-chloro-4-trifluoromethyl-N, accelerine, content 90%, yield 90%.
Embodiment 2-example 8
Device and operation steps change partial reaction conditioned disjunction material proportion with embodiment 1, the results are shown in Table-1:
Table-1:
??a ??b Solvent Catalyst A Catalyst B Temperature (℃) Content (%) Yield (%)
??200g ??200g Ethanol ?c(2g) ?------ ?195-200 ??90 ??85
??200g ??200g Ethanol ?------ ?d(6g) ?195-200 ??88 ??70
??200g ??200g Ethanol ?c(2g) ?e(6g) ?190-195 ??91 ??86
??200g ??200g Ethanol ?c(2g) ?f(6g) ?190-195 ??89 ??84
??200g ??400g Ethanol ?c(2g) ?d(6g) ?170-175 ??91 ??86
??200g ??200g Acetonitrile ?c(2g) ?d(6g) ?190-195 ??89 ??87
??200g ??200g ??DMF ?c(2g) ?d(6g) ?190-195 ??88 ??83
In the table: a-3,4-two chloro-4-phenylfluoroform b-dimethylamine c-potassiumiodide d-benzyltriethylammoinium chloride e-Tetrabutyl amonium bromide f-Polyethylene Glycol-600s
Embodiment 9:
2, the preparation of 6-dichlor-4-trifluoromethyl aniline:
In the 200ml reaction flask, drop into 25g 2-chloro-4-trifluoromethyl-N, accelerine (99%), the 200g tetracol phenixin is warming up to 60-65 ℃, drips 20g SO in 1-2 hour 2Cl 2(85%), dropwise and stir half an hour, cooling adds 0.75g Diisopropyl azodicarboxylate (98%), is warming up to 55-60 ℃, Dropwise 5 0g SO in 4-5 hour 2Cl 2(85%), chromatogram tracking detection reaction terminal point, reaction finishes and boils off tetracol phenixin, the aqueous sodium hydroxide solution of Dropwise 5 0g 30% in residuum, back flow reaction 2-3 hour, reactants water was washed till PH=9, steam distillation gets 23g 2, the 6-dichlor-4-trifluoromethyl aniline, content 94%, yield 85%.
Embodiment 10:
Use benzoyl peroxide 0.75g to replace Diisopropyl azodicarboxylate to make initiator, repeat embodiment 9, obtain similar results, content 94%, yield: 84%
Embodiment 11:
Use chlorobenzene to make solvent and repeat embodiment 9 experiments, content 92%, yield: 73%.
Embodiment 12:
Use dichlorobenzene to make solvent and repeat embodiment 9 experiments, content 93%, yield 64%.
Embodiment 13:
2, the preparation of 6-dichlor-4-trifluoromethyl aniline:
In the 200ml reaction flask, drop into 25g 2-chloro-4-trifluoromethyl-N, accelerine (99%), the 200g tetracol phenixin, be warming up to 55-60 ℃, feed the about 9.5g of chlorine, reacted 3-4 hour, cooling adds 0.75g Diisopropyl azodicarboxylate (98%), be warming up to 50-55 ℃, feed the about 23.5g of chlorine again, chromatogram tracking detection reaction terminal point, reaction finishes and boils off tetracol phenixin, Dropwise 5 0g 30% aqueous sodium hydroxide solution in residuum, back flow reaction 2-3 hour, reactants water was washed till PH=9, steam distillation gets 2,6-dichlor-4-trifluoromethyl aniline 23g, content 89%, yield 80%.
Embodiment 14:
Use the 0.75g benzoyl peroxide to make initiator, repeat embodiment 13 experiments and obtain similar results, content 89%, yield: 79%
Embodiment 15:
Use chlorobenzene to make solvent and repeat embodiment 13 experiments, content 85%, yield: 68%.Embodiment 16:
Use dichlorobenzene to make solvent and repeat embodiment 13 experiments, content 86%, yield 56%.
Embodiment 17:
2-chloro-4-trifluoromethyl-N, the preparation of accelerine:
Drop into 200Kg 98%3,4-two chloro-4-phenylfluoroforms, anhydrous potassiumiodide 2Kg to the 1000L autoclave, anhydrous benzyltriethylammoinium chloride 6Kg, the 200Kg dimethylamine is dissolved in 500L solution that dehydrated alcohol is joined, and is warming up to 190-195 ℃ of reaction, reaction is 10 hours under this temperature, chromatogram tracking is finishing reaction to raw material below 1%, cooling discharge, and rectifying gets 175Kg2-chloro-4-trifluoromethyl-N, accelerine, content 99%, yield 85%, 134-136 ℃/50mmHg.
Embodiment 18:
2, the preparation of 6-dichlor-4-trifluoromethyl aniline:
In the 200L reactor, drop into 25Kg 2-chloro-4-trifluoromethyl-N, accelerine (99%), the 200Kg tetracol phenixin is warming up to 60-65 ℃, drips 20Kg SO in 1-2 hour 2Cl 2(85%), dropwise and stir half an hour, cooling adds 750g Diisopropyl azodicarboxylate (98%), is warming up to 55-60 ℃, Dropwise 5 0Kg SO in 4-5 hour 2Cl 2(85%), chromatogram tracking detection reaction terminal point, reaction finishes and boils off tetracol phenixin, the aqueous sodium hydroxide solution of Dropwise 5 0Kg 30% in residuum, back flow reaction 2-3 hour, reactants water was washed till PH=9, steam distillation gets 22.8Kg 2, the 6-dichlor-4-trifluoromethyl aniline, content 95%, yield 85%.
Embodiment 19:
2, the preparation of 6-dichlor-4-trifluoromethyl aniline:
In the 200L reactor, drop into 25Kg 2-chloro-4-trifluoromethyl-N, accelerine (99%), the 200Kg tetracol phenixin, be warming up to 55-60 ℃, feed the about 9.5Kg of chlorine, reacted 3-4 hour, cooling adds 750g Diisopropyl azodicarboxylate (98%), be warming up to 50-55 ℃, feed the about 23.5Kg of chlorine again, chromatogram tracking detection reaction terminal point, reaction finishes and boils off tetracol phenixin, Dropwise 5 0Kg 30% aqueous sodium hydroxide solution in residuum, back flow reaction 2-3 hour, reactants water was washed till PH=9, steam distillation gets 2,6-dichlor-4-trifluoromethyl aniline 23Kg, content 90%, yield 81%.
More than two examples resulting 2,6-dichlor-4-trifluoromethyl aniline crude product can obtain content greater than 98% product, rectifying yield 90% by rectifying.
According to U.S. Pat 5,401,882 use the comparative examples of UV-light: reference examples 1:
2, the preparation of 6-dichlor-4-trifluoromethyl aniline:
In the 250ml there-necked flask, drop into 25g 2,6-chloro-4-trifluoromethyl-N, accelerine (99%), the 200g tetracol phenixin, under 10-20 ℃, UV-irradiation adds 75g SO 2Cl 2(85%), chromatogram tracking detection reaction terminal point, reaction finishes and boils off tetracol phenixin, Dropwise 5 0g50% sodium hydroxide solution in the residuum, back flow reaction 2-3 hour, reactants water was washed till PH=9, and steam distillation gets 2,6-dichlor-4-trifluoromethyl aniline 17.5g, content is about 90%, yield 71%.Reference examples 2:
2, the preparation of 6-dichlor-4-trifluoromethyl aniline:
In the 250ml there-necked flask, drop into 25g 2,6-chloro-4-trifluoromethyl-N, accelerine (99%), the 200g tetracol phenixin, under 10-20 ℃, UV-irradiation, feed the about 30g of chlorine, chromatogram tracking detection reaction terminal point, reaction finishes and boils off tetracol phenixin, Dropwise 5 0g50% sodium hydroxide solution in the residuum, back flow reaction 2-3 hour, reactants water was washed till PH=9, steam distillation gets 2,6-dichlor-4-trifluoromethyl aniline 17.2g, content is about 85%, yield 66%.

Claims (6)

1, a kind of preparation 2, the novel method of 6-dichlor-4-trifluoromethyl aniline comprises following four-step reaction:
(1) diformazan amination reaction:
Figure A0213260700021
Compound (VII) compound (VI)
(2) halogenating reaction:
Figure A0213260700022
Compound (V) compound (IV)
(3) pendant methyl halogenating reaction:
Figure A0213260700023
Compound (III)
(4) hydrolysis reaction
Figure A0213260700024
Compound (II)
Figure A0213260700031
Compound (I)
2, according to the described preparation method of claim 1, it is characterized in that: in the diformazan amination reaction, dimethylamine with, the mol ratio of 4-two chlorobenzotrifluorides is 1-20: 1; Catalyst A is selected from iodine, bromine or the villiaumite of potassium, sodium or caesium; Catalyst B is selected from quaternary amine, quaternary alkylphosphonium salt, crown ether, open chain glymes phase-transfer catalyst; The consumption of catalyst A and B is respectively 3, the 0.1-10% of 4-two chlorobenzotrifluoride weight; Temperature of reaction is 100-250 ℃, and the reaction times is 1-30 hour, and reaction pressure is 0.5-5Mp.
3, according to the described preparation method of claim 2, it is characterized in that: dimethylamine and 3, the mol ratio of 4-two chlorobenzotrifluorides is 4-8; The consumption of catalyst A is 3, and the 0.5-1% of 4-two chlorobenzotrifluoride weight, the consumption of catalyst B are 3, the 2-4% of 4-two chlorobenzotrifluoride weight; Temperature of reaction is 150-220 ℃, and the reaction times is 5-15 hour, and reaction pressure is 1.5-4Mp.
4, according to the described preparation method of claim 3, it is characterized in that: catalyst A is selected from potassiumiodide or sodium iodide; Catalyst B is selected from benzyltriethylammoinium chloride.
5, according to the described preparation method of claim 1, it is characterized in that: in halogenation and the pendant methyl halogenating reaction halogenating agent be 3-10 by halid mol ratio: 1, temperature of reaction is 0-100 ℃, the reaction times is 1-10 hour; The pendant methyl halogenation is carried out in the presence of radical initiator, and initiator is selected from Diisopropyl azodicarboxylate or benzoyl peroxide, and consumption is by the 0.1-10% of halide weight.
6, according to the described preparation method of claim 5, it is characterized in that: in halogenation and the pendant methyl halogenating reaction halogenating agent be 4-5 by the halogenide mol ratio: 1, temperature of reaction is 40-80 ℃, and the reaction times is 3-8 hour, and initiator amount is by the 2-4% of halide weight.
CN 02132607 2002-07-16 2002-07-16 Prepn process of 2,6-dichloro-4-trifluoro methylaniline Expired - Lifetime CN1209341C (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011058577A1 (en) * 2009-11-12 2011-05-19 Keki Hormusji Gharda Process for synthesizing polyhalogenated perhaloalkylaniline compounds
CN101289400B (en) * 2008-03-24 2011-07-20 浙江巍华化工有限公司 Process for synthesizing 2,6- dichlor-4-trifluoromethyl aniline
CN101289401B (en) * 2008-03-24 2011-07-20 浙江巍华化工有限公司 Process for preparing 2,6- dichlor-4-trifluoromethyl aniline
CN103408437A (en) * 2013-08-30 2013-11-27 江苏丰华化学工业有限公司 Method for preparing 2,6-dichloro-4-trifluoromethyl phenylamine
CN106117145A (en) * 2016-07-12 2016-11-16 潍坊鑫诺化工有限公司 The preparation method of 5 amino 1 (2,6 dichloro-4,4 trifluoromethyl) 3 cyano pyrazoles
CN111039792A (en) * 2019-12-11 2020-04-21 苏州开元民生科技股份有限公司 Preparation method of aniline compound

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101289400B (en) * 2008-03-24 2011-07-20 浙江巍华化工有限公司 Process for synthesizing 2,6- dichlor-4-trifluoromethyl aniline
CN101289401B (en) * 2008-03-24 2011-07-20 浙江巍华化工有限公司 Process for preparing 2,6- dichlor-4-trifluoromethyl aniline
WO2011058577A1 (en) * 2009-11-12 2011-05-19 Keki Hormusji Gharda Process for synthesizing polyhalogenated perhaloalkylaniline compounds
CN103408437A (en) * 2013-08-30 2013-11-27 江苏丰华化学工业有限公司 Method for preparing 2,6-dichloro-4-trifluoromethyl phenylamine
CN106117145A (en) * 2016-07-12 2016-11-16 潍坊鑫诺化工有限公司 The preparation method of 5 amino 1 (2,6 dichloro-4,4 trifluoromethyl) 3 cyano pyrazoles
CN111039792A (en) * 2019-12-11 2020-04-21 苏州开元民生科技股份有限公司 Preparation method of aniline compound
CN111039792B (en) * 2019-12-11 2022-10-14 苏州开元民生科技股份有限公司 Preparation method of aniline compound

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