CN101851148A - Preparation method of 4,4'-dibromobiphenyl - Google Patents

Preparation method of 4,4'-dibromobiphenyl Download PDF

Info

Publication number
CN101851148A
CN101851148A CN201010179508A CN201010179508A CN101851148A CN 101851148 A CN101851148 A CN 101851148A CN 201010179508 A CN201010179508 A CN 201010179508A CN 201010179508 A CN201010179508 A CN 201010179508A CN 101851148 A CN101851148 A CN 101851148A
Authority
CN
China
Prior art keywords
dibromobiphenyl
reaction system
preparation
temperature
oxidant
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201010179508A
Other languages
Chinese (zh)
Inventor
周永达
路趁霄
佘德兵
金柏峰
张徐飞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Vinno Technology Suzhou Co Ltd
Original Assignee
Vinno Technology Suzhou Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Vinno Technology Suzhou Co Ltd filed Critical Vinno Technology Suzhou Co Ltd
Priority to CN201010179508A priority Critical patent/CN101851148A/en
Publication of CN101851148A publication Critical patent/CN101851148A/en
Pending legal-status Critical Current

Links

Abstract

The invention discloses a preparation method of 4,4'-dibromobiphenyl, which comprises the following steps of: with water and glacial acetic acid as solvents, reacting biphenyl with bromine to generate the 4,4'-dibromobiphenyl under the heating condition in the presence of oxidant and aulixilary oxidant, then leaching through methanol and drying to obtain a finished product. The preparation method of the 4,4'-dibromobiphenyl not only has high product purity and yield and short reaction time, but also has simple operation and is easy for industrialized production.

Description

4, the preparation method of 4 '-'-dibromobiphenyl
Technical field
The present invention relates to the organic chemical industry field, be specifically related to a kind of 4, the preparation method of 4 '-'-dibromobiphenyl.
Background technology
4,4 '-'-dibromobiphenyl is a kind of important organic synthesis intermediate, because of its hydrolysis preparation 4, the succeeding in developing of 4 '-dihydroxybiphenyl method makes this product at rubber, dyestuff, petroleum product additive and make and all be widely used aspect good engineering plastics and the matrix material.Especially the raw material as liquid crystalline polymers has reached the industrialization practical stage.This base polymer has multifrequency nature, and is of many uses, can weave and make high strength fibre, is used for fibre-optic enhancing, makes matrix material and rope etc., and the application prospect that very induces one is arranged.
Learn by retrieval, Lee now surely waits " 4, synthesizing of 4 '-'-dibromobiphenyl " (" University Of Qingdao's journal " the 24th volume, 2003.9) literary composition has disclosed in the laboratory with compound haloalkane is solvent, and make catalyzer with binary metal, synthetic method at normal temperatures obtains product purity 99.7%, yield 84.6%.But the author does not provide the concrete title of employed catalyzer, and does not see that this method is applied to the report of large-scale industrial production.
U.S. Pat 4935562 (" METHOD FOR PRODUCING 4,4 '-DIBROMOBIPHENYL ") disclose a kind of 4, the preparation method of 4 '-'-dibromobiphenyl: biphenyl and bromine are dissolved in the organic solvent, react as catalyzer with Lewis acid, preparation 4,4 '-'-dibromobiphenyl, the purity 92.1% of the product that obtains, yield about 90%.Mainly there are following these shortcomings in this preparation technology:
1. need in the reaction system to add Lewis acid, the subsequent product purifying is brought difficulty as catalyzer;
2. degree of purity of production is lower, can not satisfy present need of industrial production;
3. this arts demand adds a large amount of bromines, has increased production cost, and the bromine contaminate environment;
With an organic solvent equipment is had certain corrosive nature, shortened the work-ing life of equipment.
More than these drawbacks limit the large-scale application of this technology in actual production.
Summary of the invention
For overcoming deficiency of the prior art, the object of the present invention is to provide a kind ofly 4, the preparation method of 4 '-'-dibromobiphenyl, this method have solved that existing production technique moderate purity is low, and the purifying difficulty is big, problems such as the high and contaminate environment of cost.
For solving the problems of the technologies described above, the present invention has adopted following technical scheme:
A kind of 4, the preparation method of 4 '-'-dibromobiphenyl, it comprises the steps:
1) add solvent and oxygenant successively in reaction system, wherein, described solvent is mixed and made into by water and Glacial acetic acid;
2) temperature of reaction system is remained on 0-20 ℃ scope, in reaction system, slowly drip pro-oxidant then, after dropwising, stirred 15 minutes;
3) temperature of reaction system is remained on 0-20 ℃ scope, in reaction system, add biphenyl then;
4) temperature of reaction system is remained on 15-25 ℃ scope, in reaction system, slowly drip bromine then;
5) temperature of reaction system is warming up to 30-40 ℃ scope, stirred 2 hours, reaction system is warming up to 90 ℃ then, react and obtain containing 4 after 4 hours, the mixture of 4 '-'-dibromobiphenyl, its reaction equation is as follows:
Figure GSA00000125147400021
6) with reaction system cooling, filter solid crude product;
7) wash described solid crude product with water until neutrality, again with methyl alcohol drip washing;
8) dry finished product.
Further, the mass ratio of described water and Glacial acetic acid is 1: 3-3.5.
Further, described oxygenant can be sodium perchlorate, ammonium persulphate, Sodium Persulfate or Potassium Persulphate.
Preferably, described pro-oxidant is the vitriol oil.
Further, the mass ratio of described oxygenant and described pro-oxidant is 1.5-5: 1.
Preferably, the mass ratio of described oxygenant and described pro-oxidant is 2.5: 1.
Further, the mass ratio of described solid crude product and described methyl alcohol is 1: 1.
Compared with prior art, the present invention has following advantage:
1. of the present invention 4, in the preparation method's of 4 '-'-dibromobiphenyl the process, under the effect of pro-oxidant, make the oxygenizement of oxygenant stronger, thereby accelerated bromine and biphenyl reaction generation 4,4 '-'-dibromobiphenyl, shortened the reaction times, improved reaction efficiency, reduced usage quantity, reduced the risk of contaminate environment bromine.
2. among the preparation method of the present invention, the growing amount of impurity such as 4-bromo biphenyl is few, uses the methyl alcohol drip washing of equivalent once can remove impurity, simplifies the operation, and has reduced the use to organic solvent.
3. of the present invention 4, the preparation method of 4 '-'-dibromobiphenyl has optimized reaction times and temperature of reaction, has simplified reaction process greatly, satisfies the demand of suitability for industrialized production.
The present invention is described in further detail below in conjunction with specific embodiment.
Embodiment
Implement 1:
In three mouthfuls of reactors of a 3L, add 300g water successively, 1000g Glacial acetic acid, 250g sodium perchlorate, slowly drip the vitriol oil then to 50g, keeping dripping the process system temperature is 15 ℃, dropwises, and is stirring 15 minutes below 15 ℃, add 308g biphenyl then, finish, system is cooled to below 20 ℃, slowly drips bromine until 330g, keep dripping bromine process system temperature at 20 ℃, after bromine dropwised, system can be warming up to 35 ℃, and stirred 2 hours under this temperature, be warming up to 90 ℃ of degree reactions 4 hours then, reaction finishes postcooling, filters solid phase prod, and washes solid with water to neutral, again with the drip washing of equivalent methyl alcohol, dry at last finished product 559.1g, purity 99.0%, yield 89.6%.
Embodiment 2:
In three mouthfuls of reactors of a 3L, add 300g water successively, 1000g Glacial acetic acid, 200g sodium perchlorate, slowly drip the vitriol oil then to 100g, keeping dripping the process system temperature is 15 ℃, dropwises, and is stirring 15 minutes below 15 ℃, add 308g biphenyl then, finish, system is cooled to below 20 ℃, slowly drips bromine until 330g, keep dripping bromine process system temperature at 20 ℃, after bromine dropwised, system can be warming up to 35 ℃, and stirred 2 hours under this temperature, be warming up to 90 ℃ of degree reactions 4 hours then, reaction finishes postcooling, filters solid phase prod, and washes solid with water to neutral, again with the drip washing of equivalent methyl alcohol, dry at last finished product 534.1g, purity 98.6%, yield 85.6%.
Embodiment 3:
In three mouthfuls of reactors of a 3L, add 300g water successively, 1000g Glacial acetic acid, 250g sodium perchlorate, slowly drip the vitriol oil then to 100g, keeping dripping the process system temperature is 15 ℃, dropwises, and is stirring 15 minutes below 15 ℃, add 308g biphenyl then, finish, system is cooled to below 20 ℃, slowly drips bromine to 330g, keep dripping bromine process system temperature at 20 ℃, after bromine dropwised, system can be warming up to 35 ℃, and stirred 2 hours under this temperature, be warming up to 90 ℃ of degree reactions 4 hours then, reaction finishes postcooling, filters solid phase prod, and washes solid with water to neutral, again with the drip washing of equivalent methyl alcohol, dry at last finished product 575.3g, purity 99.8%, yield 92.2%.
Embodiment 4:
In three mouthfuls of reactors of a 3L, add 300g water successively, 1000g Glacial acetic acid, 250g sodium perchlorate, slowly drip the vitriol oil then to 150g, keeping dripping the process system temperature is 15 ℃, dropwises, and is stirring 15 minutes below 15 ℃, add 308g biphenyl then, finish, system is cooled to below 20 ℃, slowly drips bromine to 330g, keep dripping bromine process system temperature at 20 ℃, after bromine dropwised, system can be warming up to 35 ℃, and stirred 2 hours under this temperature, be warming up to 90 ℃ of degree reactions 4 hours then, reaction finishes postcooling, filters solid phase prod, and washes solid with water to neutral, again with the drip washing of equivalent methyl alcohol, dry at last finished product 574.0g, purity 99.6%, yield 92.0%.
Embodiment 5:
In three mouthfuls of reactors of a 3L, add 300g water successively, 1000g Glacial acetic acid, 300g sodium perchlorate, slowly drip the vitriol oil then to 100g, keeping dripping the process system temperature is 15 ℃, dropwises, and is stirring 15 minutes below 15 ℃, add 308g biphenyl then, finish, system is cooled to below 20 ℃, slowly drips bromine to 330g, keep dripping bromine process system temperature at 20 ℃, after bromine dropwised, system can be warming up to 35 ℃, and stirred 2 hours under this temperature, be warming up to 90 ℃ of degree reactions 4 hours then, reaction finishes postcooling, filters solid phase prod, and washes solid with water to neutral, again with the drip washing of equivalent methyl alcohol, dry at last finished product 572.2g, purity 99.7%, yield 91.7%.
Embodiment 6:
In three mouthfuls of reactors of a 3L, add 150g water successively, 500g Glacial acetic acid, 190g ammonium persulphate, slowly drip the vitriol oil then to 100g, keeping dripping the process system temperature is 15 ℃, dropwises, and is stirring 15 minutes below 15 ℃, add 154g biphenyl then, finish, system is cooled to below 20 ℃, slowly drips bromine to 190g, keep dripping bromine process system temperature at 20 ℃, after bromine dropwised, system can be warming up to 35 ℃, and stirred 2 hours under this temperature, be warming up to 90 ℃ of degree reactions 4 hours then, reaction finishes postcooling, filters solid phase prod, and washes solid with water to neutral, again with the drip washing of equivalent methyl alcohol, dry at last finished product 265.1g, purity 99.4%, yield 84.9%.
Embodiment 7:
In three mouthfuls of reactors of a 3L, add 150g water successively, 500g Glacial acetic acid, 262g Sodium Persulfate, slowly drip the vitriol oil then to 100g, keep dripping 15 ℃ of process system temperature, dropwise, stirring 15 minutes below 15 ℃, add 154g biphenyl then, finish, system is cooled to below 20 ℃, slowly drips bromine to 180g, keep dripping bromine process system temperature at 20 ℃, after bromine dropwised, system can be warming up to 35 ℃, and stirred 2 hours under this temperature, be warming up to 90 ℃ of degree reactions 4 hours then, reaction finishes postcooling, filters solid phase prod, and washes solid with water to neutral, again with the drip washing of equivalent methyl alcohol, dry at last finished product 269.8g, purity 99.2%, yield 85.6%.
Embodiment 8:
In three mouthfuls of reactors of a 3L, add 150g water successively, 500g Glacial acetic acid, 324g Potassium Persulphate, slowly drip the vitriol oil then to 100g, keeping dripping the process system temperature is 15 ℃, dropwises, and is stirring 15 minutes below 15 ℃, add 154g biphenyl then, finish, system is cooled to below 20 ℃, slowly drips bromine to 180g, keep dripping bromine process system temperature at 20 ℃, after bromine dropwised, system can be warming up to 35 ℃, and stirred 2 hours under this temperature, be warming up to 90 ℃ of degree reactions 4 hours then, reaction finishes postcooling, filters solid phase prod, and washes solid with water to neutral, again with the drip washing of equivalent methyl alcohol, dry at last finished product 270.2g, purity 99.5%, yield 86.5%.
The foregoing description just is to allow the one of ordinary skilled in the art can understand content of the present invention and enforcement according to this for technical conceive of the present invention and characteristics being described, its objective is, can not limit protection scope of the present invention with this.The variation or the modification of every equivalence that the essence of content has been done according to the present invention all should be encompassed in protection scope of the present invention.

Claims (7)

1. one kind 4, the preparation method of 4 '-'-dibromobiphenyl is characterized in that, comprises the steps:
1) add solvent and oxygenant successively in reaction system, wherein, described solvent is mixed and made into by water and Glacial acetic acid;
2) temperature of reaction system is remained on 0-20 ℃ scope, in reaction system, slowly drip pro-oxidant then, after dropwising, stirred 15 minutes;
3) temperature of reaction system is remained on 0-20 ℃ scope, in reaction system, add biphenyl then;
4) temperature of reaction system is remained on 15-25 ℃ scope, in reaction system, slowly drip bromine then;
5) temperature of reaction system is warming up to 30-40 ℃ scope, stirred 2 hours, reaction system is warming up to 90 ℃ then, react and obtain containing 4 after 4 hours, the mixture of 4 '-'-dibromobiphenyl, its reaction equation is as follows:
Figure FSA00000125147300011
6) with reaction system cooling, filter solid crude product;
7) wash described solid crude product with water until neutrality, again with methyl alcohol drip washing;
8) dry finished product.
2. according to claim 14, the preparation method of 4 '-'-dibromobiphenyl is characterized in that, the mass ratio of described water and Glacial acetic acid is 1: 3-3.5.
3. according to claim 14, the preparation method of 4 '-'-dibromobiphenyl is characterized in that, described oxygenant can be sodium perchlorate, ammonium persulphate, Sodium Persulfate or Potassium Persulphate.
4. according to claim 14, the preparation method of 4 '-'-dibromobiphenyl is characterized in that, described pro-oxidant is the vitriol oil.
5. according to claim 1 or 3 or 4 described 4, the preparation method of 4 '-'-dibromobiphenyl is characterized in that, the mass ratio of described oxygenant and described pro-oxidant is 1.5-5: 1.
6. according to claim 1 or 3 or 4 described 4, the preparation method of 4 '-'-dibromobiphenyl is characterized in that, the mass ratio of described oxygenant and described pro-oxidant is 2.5: 1.
7. according to claim 14, the preparation method of 4 '-'-dibromobiphenyl is characterized in that, the mass ratio of described solid crude product and described methyl alcohol is 1: 1.
CN201010179508A 2010-05-24 2010-05-24 Preparation method of 4,4'-dibromobiphenyl Pending CN101851148A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201010179508A CN101851148A (en) 2010-05-24 2010-05-24 Preparation method of 4,4'-dibromobiphenyl

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201010179508A CN101851148A (en) 2010-05-24 2010-05-24 Preparation method of 4,4'-dibromobiphenyl

Publications (1)

Publication Number Publication Date
CN101851148A true CN101851148A (en) 2010-10-06

Family

ID=42802863

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201010179508A Pending CN101851148A (en) 2010-05-24 2010-05-24 Preparation method of 4,4'-dibromobiphenyl

Country Status (1)

Country Link
CN (1) CN101851148A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4950817A (en) * 1988-03-19 1990-08-21 Bayer Aktiengesellschaft Process for the preparation of 4,4'-dihalobiphenyls
US4983781A (en) * 1988-03-02 1991-01-08 Rhone-Poulenc Chimie Process for the preparation of 4,4'-dibromobiphenyl in a solvent medium and with a catalyst

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4983781A (en) * 1988-03-02 1991-01-08 Rhone-Poulenc Chimie Process for the preparation of 4,4'-dibromobiphenyl in a solvent medium and with a catalyst
US4950817A (en) * 1988-03-19 1990-08-21 Bayer Aktiengesellschaft Process for the preparation of 4,4'-dihalobiphenyls

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
ALICE M. CLARK ET AL.: "Preparation of biphenyl-2,2",3,3",5,5",6m6"-2Hg", 《JOURNAL OF LABELLED COMPOUNDS AND RADIOPHARMACEUTICALS》 *
杨果等: "p,p,p,p"-四氯联苯二膦的合成", 《化学研究与应用》 *

Similar Documents

Publication Publication Date Title
CN112876509B (en) Bio-based flame-retardant magnolol epoxy monomer, preparation method and application in flame-retardant epoxy resin
CN101284805A (en) Production method for 2-acryloylamino-2-methylpropane sulfonic acid
CN114195621B (en) Preparation method of methyl octabromoether
CN107325284A (en) A kind of hyperbranched poly phenyl triazole formic acid esters and preparation method and application
CN101381601A (en) Oligomer blue light electroluminescence material and synthetic method thereof
CN105111049A (en) Preparation method of 2, 2'-dihydroxybiphenyl
CN101851148A (en) Preparation method of 4,4'-dibromobiphenyl
CN113912478B (en) Synthesis method of 4,4' -biphenol
CN102515121B (en) Preparation method of linear polyhalophosphazene with high relative molecular mass
CN107162870B (en) Method for synthesizing dichloro-p-xylene ring dimer
CN108276439B (en) Brominated phosphate flame retardant and preparation method thereof
CN113307809B (en) Graphene imide and unilateral perylene imide based on cyclooctatetraene and synthesis and application thereof
CN102585225A (en) Preparation method of diaza-naphthalenone-biphenyl-polybenzoxazole, monomer and polymer
CN111087623B (en) Polysiloxane side chain liquid crystal polymer with smectic phase and application thereof
CN103980131A (en) 1,3,5-tri(3-amino-2,4,6-trinitro styryl) benzene compound and preparation method and application thereof
CN101234990B (en) Method for preparing 4,4'-di(2,4-dinitrophenoxy)diphenylmethane
CN115322070A (en) Preparation method of p-alkyl phenyl o-fluorobenzene
CN101234986B (en) Method for preparing 1,4-di(2,4-dinitrophenoxy)naphthalene
CN101234984B (en) Method for preparing 2,5-di(2,4-dinitrophenoxy)toluene
CN101234979B (en) Method for preparing 3,5-di(2,4-dinitrophenoxy)toluene
CN101284788B (en) Preparation method of 2,3-di(2,4-dinitro phenoxy)naphthalin
CN101245015B (en) Process for producing 1,3-bis(2,4-dinitrophenoxy)naphthalin
CN101279922B (en) Preparation of 1,4-bis(2,4- dinitrophenoxy)-2,3,5- trimethylbenzene
CN101234989A (en) Method for preparing 4,4'-di(2,4-dinitrophenoxy)benzophenone
CN101230005B (en) Method for preparing 1,3,5-tri(2,4-dinitrophenoxy) benzene

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20101006