Summary of the invention
In view of the foregoing deficiencies of prior art, the purpose of the present invention is to provide chloro- 2, the 4- difluoros of 3,5- of one kind bis-
The preparation method of aniline, for solving the problems of the prior art.The preparation method phase of the chloro- 2,4 difluorobenzene amine of the 3,5- bis-
, safety more economical for existing synthetic route and environmental protection also reduce costs while improving yield and quality, save
Resource and the energy, the technique for being suitble to heavy industrialization.
In order to achieve the above objects and other related objects, first aspect present invention provides chloro- 2, the 4- difluoro of 3,5- of one kind bis-
The preparation method of aniline, includes the following steps:
1) with 1,2,3- trichloro-benzenes for raw material, nitration reaction prepares 2,3,4- trichloronitrobenzenes;Reaction equation is such as
Under:
2) 2,3,4- trichloronitrobenzenes are restored, prepares 2,3,4- trichloroanilines;Reaction equation is as follows:
3) 2,3,4- trichloroanilines prepare 1,2,3,4- tetrachlorobenzenes by diazo-reaction;Reaction equation is as follows:
4) 1,2,3,4- tetrachlorobenzene is nitrified, reaction obtains 2,3,4,5- tecnazenes;Reaction equation is as follows:
5) 2,3,4,5- tecnazenes are prepared into chloro- 2, the 4- difluoro nitrobenzene of 3,5- bis- by fluorination reaction;Instead
Answer equation as follows:
6) chloro- 2, the 4- difluoro nitrobenzene of 3,5- bis- is restored, that is, prepares chloro- 2, the 4- difluoroaniline of 3,5- bis-.Reaction
Equation is as follows:
Preferably, the preparation method of chloro- 2, the 4- difluoroaniline of 3, the 5- bis- specifically comprises the following steps:
1) nitration reaction: 1,2,3- trichloro-benzenes being dissolved in reaction dissolvent, then nitration mixture is added dropwise, and nitration reaction prepares 2,
3,4- trichloronitrobenzenes, the nitration mixture are the mixed liquor of nitric acid and the concentrated sulfuric acid.
It is furthermore preferred that the weight ratio of nitric acid and the concentrated sulfuric acid is 1:3-10 in mixed liquor in the step 1.
It is furthermore preferred that during nitration mixture is added dropwise, reaction temperature is 50-60 DEG C in the step 1.
It is furthermore preferred that after nitration mixture is added dropwise, keeping the temperature 30-45min at 40-60 DEG C in the step 1.
Under normal circumstances, reaction temperature is kept during being added dropwise.To the 1,2,3- trichlorine in solvent in reaction process
Benzene is monitored, and controls reaction process.
It is furthermore preferred that in the step 1, described 1, the weight ratio of 2,3- trichloro-benzenes and nitration mixture is 1:1.5-2.
It is furthermore preferred that the reaction dissolvent of nitration reaction includes but is not limited to dichloroethanes, tetrahydrofuran in the step 1
With one of 1,4- dioxane or a variety of combinations.
In a preferred embodiment, the reaction dissolvent is dichloroethanes.
It is furthermore preferred that the post-processing step in the step 1 are as follows: extract gained reaction solution using organic solvent, will have
Machine is mutually washed till alkalescent, and separation obtains organic phase and removes solvent up to step 1 product.
It is further preferred that also being recrystallized after removing solvent.In a preferred embodiment, recrystallization is made
Solvent is preferably n-hexane.
2) reduction reaction: reducing agent, salt electrolyte and water being mixed with reaction dissolvent, then are added portionwise 2,3,4- trichlorines
Nitrobenzene carries out reduction and prepares 2,3,4- trichloroaniline.
It is furthermore preferred that during 2,3,4- trichloronitrobenzene is added, reaction temperature is 40-70 DEG C in the step 2.
Be added portionwise can be it is point multiple batches of feed intake, also 2,3,4- trichloronitrobenzenes can be dissolved in appropriate reaction dissolvent
In, it is added in reaction system by way of dropwise addition.After the completion of the charging of 2,3,4- trichloronitrobenzenes, reaction system is protected
Temperature, and monitor reaction process.Preferred holding temperature is 50-70 DEG C, and soaking time is 1-4 hours.It is preferred real in the present invention one
It applies in example, the time of heat preservation is 2 hours or so.
It is furthermore preferred that in the step 2,2,3,4- trichloronitrobenzenes are with reducing agent, water, the electrolytelike weight ratio of salt
1:0.5-1.0:8-12:0.15-0.3.
It is furthermore preferred that the reducing agent is selected from iron powder or palladium charcoal in the step 2.
In a preferred embodiment, reducing agent is iron powder.
It is furthermore preferred that the salt electrolyte includes but is not limited to one of ammonium chloride, ammonium sulfate in the step 2
Or a variety of combination.
In a preferred embodiment, salt electrolyte is ammonium chloride.
It is furthermore preferred that the reaction dissolvent of reduction reaction includes but is not limited to dichloroethanes, toluene, first in the step 2
One of alcohol, ethyl alcohol or a variety of combinations.
In a preferred embodiment, the reaction dissolvent is dichloroethanes.
It is furthermore preferred that the post-processing step in the step 2 are as follows: filtering by filtrate water extracting and washing, is layered and merges
Organic phase removes solvent up to step 2 product.
3) diazo-reaction: 2,3,4- trichloroanilines, inorganic acid, ammonium chloride are dissolved in reaction dissolvent, Asia is added portionwise
Nitrate carries out diazotising;Gained reaction solution is added dropwise in the mixed liquor of concentrated hydrochloric acid and stannous chloride, it is anti-by sandmeyer
1,2,3,4- tetrachlorobenzene should be prepared.
It is furthermore preferred that the nitrite is selected from one of sodium nitrite, potassium nitrite or a variety of in the step 3
Selection.Be added portionwise can be it is point multiple batches of feed intake, nitrite can be also dissolved in appropriate solvent, pass through dropwise addition
Mode is added in reaction system.The process that feeds intake of nitrite need to generally be completed at low temperature.In one embodiment of the present invention
In, the nitrite is sodium nitrite or potassium nitrite, and the solvent is water, temperature model during nitrous acid aqueous solution is added dropwise
System is contained at -5-5 DEG C.
In a preferred embodiment, nitrite is sodium nitrite.
It is furthermore preferred that the inorganic acid includes but is not limited to hydrochloric acid, sulfuric acid, hydrobromic acid, nitric acid, crosses chlorine in the step 3
One of acid and fluoboric acid or a variety of combinations.
In a preferred embodiment, salt used in the mixed liquor of the inorganic acid, hydrochloric acid and stannous chloride
Acid is 36~38% concentrated hydrochloric acid.
It is furthermore preferred that in the step 3, -5-5 DEG C of heat preservation 1-2h after nitrite is added.
It is furthermore preferred that in the step 3, in the mixed liquor that gained reaction solution is added dropwise to hydrochloric acid and stannous chloride
Dropping temperature is 40-60 DEG C, and 70-90 DEG C is warming up to after being added dropwise to complete, and keeps the temperature 1-2h.
It is furthermore preferred that 2,3,4- trichloroanilines, inorganic acid, ammonium chloride are dissolved in reaction dissolvent in the step 3, point
Batch be added nitrite carry out it is diazotizing during, the weight of 2,3,4- trichloroanilines, inorganic acid, ammonium chloride, sodium nitrite
Than for 1:2-3:0.2-0.4:0.4-0.6.
It is furthermore preferred that gained reaction solution being added dropwise in the mixed liquor of hydrochloric acid and stannous chloride, being passed through in the step 3
During sandmeyer reaction prepares 1,2,3,4- tetrachlorobenzenes, the weight of 2,3,4- trichloroanilines, hydrochloric acid, stannous chloride
Than for 1:5-7:0.6-1.
It is furthermore preferred that the post-processing step in the step 3 are as follows: extract gained reaction solution using organic solvent, separate
It obtains organic phase and removes organic solvent up to step 3 product.
4) nitration reaction: 1,2,3,4- tetrachlorobenzene is dissolved in reaction dissolvent, then nitration mixture is added dropwise, nitration reaction prepares
2,3,4,5- tecnazenes, the nitration mixture are the mixed liquor of nitric acid and the concentrated sulfuric acid.
It is furthermore preferred that the weight ratio of nitric acid and the concentrated sulfuric acid is 1:3-4 in mixed liquor in the step 4.
It is furthermore preferred that during nitration mixture is added dropwise, reaction temperature is 40-50 DEG C in the step 4.
It is furthermore preferred that after nitration mixture is added dropwise, keeping the temperature 8-12 hours at 40-60 DEG C in the step 4.
Under normal circumstances, reaction temperature is kept during being added dropwise.To the 1,2,3,4- tetra- in solvent in reaction process
Chlorobenzene is monitored, and controls reaction process.
It is furthermore preferred that in the step 4, described 1, the weight ratio of 2,3,4- tetrachlorobenzenes and nitration mixture is 1:1.5-2.
It is furthermore preferred that the reaction dissolvent of nitration reaction includes but is not limited to dichloroethanes, tetrahydrofuran in the step 4
With one of 1,4- dioxane or a variety of combinations.
It is furthermore preferred that the post-processing step in the step 4 are as follows: extract gained reaction solution using organic solvent, will have
Machine is mutually washed till alkalescent, and separation obtains organic phase and removes solvent up to step 4 product.
5) fluorination reaction: 2,3,4,5- tecnazene, fluorization agent and phase transfer catalyst are carried out in reaction dissolvent
Fluorination reaction prepares the chloro- 2,4- difluoro nitrobenzene of 3,5- bis-.
It is furthermore preferred that fluorization agent is selected from one of potassium fluoride, sodium fluoride and ammonium fluoride or a variety of in the step 5
Combination.
In a preferred embodiment, the fluorization agent is potassium fluoride.
It is furthermore preferred that in the step 5, phase transfer catalyst be selected from tetrabutylammonium bromide, trimethylphenyl ammonium chloride and
One of hexadecyl tributyl phosphonium phosphine or a variety of combinations.
It is furthermore preferred that in the step 5,2,3,4,5- tecnazenes, fluorization agent, phase transfer catalyst weight ratio be
1:0.58-0.8:0.09-0.15 reaction condition is to react 12-20h at 120-150 DEG C.
It is furthermore preferred that the reaction dissolvent of fluorination reaction includes but is not limited in sulfolane, DMSO and DMF in the step 5
One or more combinations.
In a preferred embodiment, the reaction dissolvent is sulfolane.
It is furthermore preferred that the post-processing step in the step 5 are as follows: it is added toluene in gained reaction solution, cooled and filtered,
Solid phase is washed with toluene, and washing lotion merges with filtrate, removes solvent up to step 5 product.
6) reduction reaction: reducing agent, salt electrolyte and water are mixed with reaction dissolvent, then are added portionwise 3,5- bis- is chloro-
2,4- difluoro nitrobenzenes are restored, that is, prepare chloro- 2, the 4- difluoroaniline of 3,5- bis-.
It is furthermore preferred that 3,5- bis- chloro- 2,4- difluoro nitrobenzenes and reducing agent, water, salt are electrolytelike in the step 6
Weight ratio is 1:0.5-1.0:8-12:0.15-0.3, and reaction temperature is 70-100 DEG C.
It is furthermore preferred that the reducing agent is selected from iron powder or palladium charcoal in the step 6.
In a preferred embodiment, reducing agent is iron powder.
It is furthermore preferred that the salt electrolyte includes but is not limited to one of ammonium chloride, ammonium sulfate in the step 6
Or a variety of combination.
In a preferred embodiment, salt electrolyte is ammonium chloride.
It is furthermore preferred that the reaction dissolvent of reduction reaction includes but is not limited to dichloroethanes, tetrahydrofuran in the step 6
With one of 1,4- dioxane or a variety of combinations.
In a preferred embodiment, the reaction dissolvent is dichloroethanes.
It is furthermore preferred that reaction temperature is 70-90 DEG C during chloro- 2, the 4- difluoro nitrobenzene of 3,5- bis- is added.
Be added portionwise can be it is point multiple batches of feed intake, chloro- 2, the 4- difluoro nitrobenzene of 3,5- bis- can be also dissolved in right amount
In reaction dissolvent, it is added in reaction system by way of dropwise addition.It is right after the completion of 3,5- bis- chloro- 2,4- difluoro nitrobenzene chargings
Reaction system is kept the temperature, and monitors reaction process.Preferred holding temperature is 80-100 DEG C, and soaking time is 2-5 hours.?
In one embodiment of the present invention, the time of heat preservation is 2 hours or so.
It is furthermore preferred that the post-processing step in the step 6 are as follows: filtering, by filtrate water extracting and washing, layering is associated with
Machine phase, solvent evaporated is up to step 6 product.
As described above, the preparation method of chloro- 2, the 4- difluoroaniline of 3,5- bis- provided by the present invention be extremely easy to industrial production,
Cost is relatively low, the route of safety and environmental protection.The preparation method is that starting is former with cheap chemical products 1,2,3- trichloro-benzenes
Material, through nitrification, reduction, diazotising chlorination three-step reaction be made high-purity 1,2,3,4- tetrachlorobenzenes, then again it is perfluorinated and also
The obtained chloro- 2,4 difluorobenzene amine of 3,5- bis- of original.Each step reaction is all popular response, and yield is very high;And it gets around on chlorine
The reaction of chlorine, uses chlorine in diazotising instead, and reaction condition as mild as a dove, is suitble to large-scale production.
Second aspect of the present invention provides the preparation method of the chloro- 2,4 difluorobenzene amine of the 3,5- bis- in Teflubenzuron, quinolone
The purposes of the preparation fields such as class candidates against infection, anti-parasite medicine bioactive molecule.
The purposes refers specifically to
Intermediate, synthesis Teflubenzuron, quinolones candidates against infection, anti-parasite medicine bioactive molecule etc..
The preparation method of the chloro- 2,4 difluorobenzene amine (I) of 3,5- bis- provided by the present invention has the advantages that
1) reaction condition is mild, stably and controllable, and active site is few, is not susceptible to side reaction, whole route yield and quality
Preferably
2) supplementary material is cheap and easy to get, can be effectively reduced cost, energy saving, avoids the use of chlorine, environment friend
It is good.