CN101863791A - Method for synthesizing 2-Ethylhexyl p-dimethylaminobenzoate (EHA) - Google Patents

Method for synthesizing 2-Ethylhexyl p-dimethylaminobenzoate (EHA) Download PDF

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CN101863791A
CN101863791A CN201010209076A CN201010209076A CN101863791A CN 101863791 A CN101863791 A CN 101863791A CN 201010209076 A CN201010209076 A CN 201010209076A CN 201010209076 A CN201010209076 A CN 201010209076A CN 101863791 A CN101863791 A CN 101863791A
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benzoic acid
dimethylamino
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eha
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CN101863791B (en
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李永芳
陈文�
王先文
陈立柱
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HUBEI HUIDA TECHNOLOGY DEVELOPMENT CO LTD
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Abstract

The invention relates to a method for synthesizing 2-Ethylhexyl p-dimethylaminobenzoate (EHA) and production technology research thereof. The method comprises the steps of: reacting halogeno benzene benzoic acid as raw materials with dimethylamine and isooctanol, removing a solvent and isooctanol via reduced pressure distillation to obtain the 2-Ethylhexyl p-dimethylaminobenzoate (EHA), wherein the product has the purity being greater than 98% and the overall yield being 85%. The process has the characteristics of mild reaction condition, simple operation, environmental protection and easy recycling of the solvent, and is suitable for industrial production.

Description

The synthetic method of the different monooctyl ester of p-(dimethylamino)-benzoic acid (EHA)
Invention field
The present invention relates to the synthetic method and the production technique of a kind of important different monooctyl ester of ultraviolet initiator p-(dimethylamino)-benzoic acid of chemical industry.Method of the present invention is to be raw material to halogenated benzoic acid, through reacting with dimethylamine, reacts with isooctyl alcohol in the presence of catalyzer again, remove through underpressure distillation then and desolvate and isooctyl alcohol, obtain the different monooctyl ester of p-(dimethylamino)-benzoic acid (EHA), product purity is greater than 99%, and total recovery is more than 85%.Synthetic method of the present invention has from basic chemical raw materials, and no severe condition are simple to operate, environmentally friendly, solvent easy to recovery of applied etc. characteristics, be fit to be applied to industrial production.
Background of invention
The p-(dimethylamino)-benzoic acid ester series compound is a class amine promoter efficiently, same free radical (II) type light trigger uses together, the varnish colour system that is mainly used in paper, timber, metal and frosting is carried out ultra-violet curing, also can be used for single or multiple monomeric ultraviolet radiation polyreaction, or the sensitizing agent of excellent property, normal and thioxanthone photoinitiator, acetophenones light trigger are united use, photoinitiation can be promoted, the interference effect of oxygen can be effectively eliminated again light initiation polymerization.
The p-(dimethylamino)-benzoic acid ester series compound, can do good uvioresistant additive, be widely used in the water-fast sun care preparations, comprising p-(dimethylamino)-benzoic acid isopentyl ester (IADB) and the different monooctyl ester (EHA of p-(dimethylamino)-benzoic acid, commodity by name 507), the latter is a kind of UV light absorber of good UVB district, as sun-screening agent, used in large quantities in the world, U.S. FDA is classified it as sun-screening agent that the first kind is recommended use.The p-(dimethylamino)-benzoic acid ester not only is applied to cosmetic field, and also can be used as sanitas and use, as: p-(dimethylamino)-benzoic acid methyl esters, p-(dimethylamino)-benzoic acid propyl ester, the positive butyl ester of p-(dimethylamino)-benzoic acid and solution thereof all have preservative activity.
The processing method of existing synthetic p-(dimethylamino)-benzoic acid ester, usually all be substrate with the p-(dimethylamino)-benzoic acid, therefore seek the synthetic method of a suitable p-(dimethylamino)-benzoic acid suitability for industrialized production, crucial meaning is arranged for exploitation p-(dimethylamino)-benzoic acid derivatives class series product.
The main method of at present synthetic p-(dimethylamino)-benzoic acid has: (1) is to carboxylated (Journal of Organic Chemistry, 55 (6), the 1768-71 of dimethylamino halogeno-benzene; 1990); (2) carboxylated to the haloform of dimethylamino methyl phenyl ketone; (3) nitrogen of the para-amino benzoic acid (GB2233975 that methylates; Huaxue Shiji, 25 (4), 245-246; 2003; Journal of Organic Chemistry, 70 (7), 2476-2485; 2005); (4) direct oxidation of paradimethy laminobenzaldehyde (Organic Letters, 9 (18), 3515-3518; 2007; Huaihai Gongxueyuan Xuebao, ziran Kexueban, 14 (2), 53-55; 2005).Method (1), (2) and (3) are not suitable for large-scale industrial production owing to raw materials cost height, toxicity are big, the uneasy congruent factor of operation, and wherein method (3) also can produce the by product of a large amount of monomethylations, brings difficulty for product separation and purifying; Method (4) is the classical way that aromatic aldehyde is oxidized to aromatic carboxylic acid, but the cost of aromatic aldehyde is higher, and oxidation step often need use the active Textone of expensive Silver Nitrate and character, is not suitable for big industrial production.
Diformazan aminobenzoic acid ester preparation method there be (I) to the direct esterification of diformazan aminobenzoic acid (Journal of Organic Chemistry, 70 (7), 2476-2485; 2005; ); (I I) vitamin Bx ester methylates through formaldehyde catalysis nitrogen, and (GB 2233975; CN1289764).Shortcomings such as method (I) exists the p-(dimethylamino)-benzoic acid cost more expensive, and esterification yield is low, and the acid waste water amount is big.It is fully very difficult that method (II) exists nitrogen to methylate, and used methylating reagent methyl-sulfate toxicity is big, the acid waste water amount is many; With methyl chloride, methyl iodide cost height, both exist simultaneously, and ester has partial hydrolysis in the process of methylating, and influences the productive rate shortcoming.
Summary of the invention
The objective of the invention is to overcome the existing existing shortcoming of synthetic method, provide that a kind of operational path is short, raw material is easy to get, condition is gentle, easy and simple to handle relatively, the three wastes are few, the synthetic method of the different monooctyl ester of the p-(dimethylamino)-benzoic acid of high yield (EHA).This method adopt domestic be easy to get halogenated benzoic acid and dimethylamine agueous solution are done raw material, catalyzer exist down ammonia separate, again through catalytic esterification, the different monooctyl ester of the p-(dimethylamino)-benzoic acid of the synthetic high level of high yield (EHA).All steps do not have severe condition, and are simple to operate, environmentally friendly, meet requirements of green environmental protection, have remarkable social benefit and economic benefit, are fit to suitability for industrialized production.
The structural formula of the different monooctyl ester of p-(dimethylamino)-benzoic acid (EHA) is as follows:
Figure BSA00000167480300021
For achieving the above object, the step that comprises of synthetic method provided by the invention: its synthesis step is:
X=Cl,Br
The concrete operations step is as follows:
Step 1: be under 10~150 ℃ the condition in temperature, in to the mixed system of halogenated benzoic acid and dimethylamine agueous solution, add catalyzer Cat-1, and 50~200 ℃ of heated and stirred 5~20 hours, be cooled to room temperature, behind the reacting liquid filtering, filtrate is regulated pH ≈ 4 with dilute hydrochloric acid, filters the solid crude product that obtains p-(dimethylamino)-benzoic acid, can be directly used in the next step after drying.
In the step 1 of the present invention, the catalyzer Cat-1 of adding is a tetrabutylammonium chloride, Tetrabutyl amonium bromide, trimethyl benzyl ammonia chloride, polyoxyethylene glycol 800~1200, phase-transfer catalysts such as glycerine; Catalyzer Cat-2 is CuCl 2, Cu 2O, Cu powder, CoCl 2This two classes catalyzer makes reaction conditions more gentle when accelerating speed of reaction; Excessive dimethylamine is beneficial to promotion reaction conversion as the acid binding agent of reaction, but and multistep recycled.
Step 2: be under 20~80 ℃ the condition in temperature, in the mixed system of p-(dimethylamino)-benzoic acid, isooctyl alcohol and solvent orange 2 A, add catalyzer Cat-3, be heated to reaction system boiling and through minute fluidization tower extraction solvent and water, treat to keep 1~2 hour again to no longer including the water generation after the material clarification, sampling analysis to feed stock conversion greater than 99%, about 3~15 hours of this process.Reaction system is cooled to room temperature, is neutralized to neutrality, leaves standstill to tell organic layer, and vacuum distillation recovered solvent and remaining isooctyl alcohol continue underpressure distillation again and obtain product.
In the step 2 of the present invention, reaction solvent A can be benzene,toluene,xylene, chlorobenzene and dichlorobenzene, preferred dimethylbenzene; Catalyzer Cat-3 is a tosic acid, sulfuric acid, phosphoric acid, boric acid and tetra-sodium, preferential phosphoric acid; The post processing mode that adopts is: reaction solution is neutralized to neutrality, leaves standstill to tell organic layer, sloughs solvent and residual raw materials, gets the different monooctyl ester of p-(dimethylamino)-benzoic acid (EHA), and product purity is greater than 99%; Two step total recoverys are greater than 85%.
The invention relates to the synthetic method of the different monooctyl ester of p-(dimethylamino)-benzoic acid (EHA), synthetic route is totally two steps, and is shorter than the additive method step, more help big industrial production, this route does not have obvious by product, the acid binding agent of the dimethylamine double as reaction of one of substrate, but multistep recycled.The present invention can provide the total recovery more than 85%, and product purity is greater than 99%, institute do not have in steps severe condition, simple to operate, environmentally friendly, solvent is easy to recovery of applied, is fit to be applied to industrial production.
Embodiment
In order to be illustrated more clearly in the present invention, hereinafter adopt indefiniteness embodiment to be described further.
Embodiment one
(1) step 1: the preparation of p-(dimethylamino)-benzoic acid
Add 78.0g (0.5mol) Chlorodracylic acid in the autoclave of 2L successively, 1364g (10mol) dimethylamine agueous solution (wt 33%) adds 7.8g CuCl again 22H 2O and 7.8g tetrabutylammonium chloride, temperature of reaction are 150 ℃, heating 15h, monitor to feedstock conversion fully through HPLC, reaction finishes, and dimethylamine is reclaimed in distillation, be cooled to room temperature then, with dilute hydrochloric acid regulation system pH ≈ 4, separate out a large amount of yellow crystals behind the reacting liquid filtering, in ice bath behind the cooling 10min, suction filtration, solid drying gets product 74.7g, single step yield 90.6%, structure warp 1H-NMR, MS conclusive evidence.
(2) step 2: the preparation of the different monooctyl ester of p-(dimethylamino)-benzoic acid (EHA)
In the four-hole bottle that installs agitator, thermometer, reflux condensation mode and water trap, add 156.0g (1mol) p-(dimethylamino)-benzoic acid, 143.0g (1.1mol) isooctyl alcohol, 420ml chlorobenzene and 18g phosphoric acid.Heated and stirred is warming up to boiling, the about 8h of reflux water-dividing, treat vial material clarification after, keep the 1~2h that refluxes again, generate to no longer including water, the sampling analysis material content is less than 1.0%, reaction finishes.Be cooled to room temperature, be neutralized to neutrality, leave standstill and tell organic layer, underpressure distillation removes removal xylene and isooctyl alcohol, continue to distill product 264.5g, HPLC purity: 99.3%, single step yield 95.5%, structure warp 1H-NMR, MS conclusive evidence.
Two step total recoverys 86.5%.
Embodiment two
(1) step 1: the preparation of p-(dimethylamino)-benzoic acid
Add 100.0g (0.5mol) parabromobenzoic acid in the autoclave of 2L successively, 1364g (10mol) dimethylamine agueous solution (wt 33%) adds 8.8g CuCl again 22H 2O and 7.8g tetrabutylammonium chloride, temperature of reaction are 150 ℃, heating 15h, monitor to feedstock conversion fully through HPLC, reaction finishes, and dimethylamine is reclaimed in distillation, be cooled to room temperature then, with dilute hydrochloric acid regulation system pH ≈ 4, separate out a large amount of yellow crystals behind the reacting liquid filtering, in ice bath behind the cooling 10min, suction filtration, solid drying gets product 78.8g, single step yield 95.6%, structure warp 1H-NMR, MS conclusive evidence.
(2) step 2: the preparation of the different monooctyl ester of p-(dimethylamino)-benzoic acid (EHA)
In the reactor that installs agitator, thermometer, reflux condensation mode and water trap (four-hole bottle), add 165.0g (1mol) p-(dimethylamino)-benzoic acid, 143.0g (1.1mol) isooctyl alcohol, 420ml dimethylbenzene and 5g sulfuric acid (wt 98% content).Heated and stirred is warming up to boiling, the about 8h of reflux water-dividing, treat vial material clarification after, keep the 1~2h that refluxes again, generate to no longer including water, the sampling analysis material content is less than 1.0%, reaction finishes.Be cooled to room temperature, be neutralized to neutrality, leave standstill and tell organic layer, underpressure distillation removes removal xylene and isooctyl alcohol, continue to distill product 270g, HPLC purity: 99.3%, single step yield 95.5%, structure warp 1H-NMR, MS conclusive evidence.
Two step total recoverys 91.3%.

Claims (4)

1. the synthetic method of the different monooctyl ester of p-(dimethylamino)-benzoic acid (EHA), described method comprises following two steps:
Step 1: be under 10~150 ℃ the condition in temperature, in to the mixed system of halogenated benzoic acid and dimethylamine agueous solution, add catalyzer Cat-1, and 50~200 ℃ of heated and stirred 5~20 hours, be cooled to room temperature, behind the reacting liquid filtering, filtrate is regulated pH ≈ 4 with dilute hydrochloric acid, filters the solid crude product that obtains p-(dimethylamino)-benzoic acid, can be directly used in the next step after drying.
Step 2: be under 20~80 ℃ the condition in temperature, in the mixed system of p-(dimethylamino)-benzoic acid, isooctyl alcohol and solvent orange 2 A, add catalyzer Cat-3, be heated to reaction system boiling and through minute fluidization tower extraction solvent and water, treat to keep 1~2 hour again to no longer including the water generation after the material clarification, sampling analysis to feed stock conversion greater than 99%, about 3~15 hours of this process.Reaction system is cooled to room temperature, is neutralized to neutrality, leaves standstill to tell organic layer, and vacuum distillation recovered solvent and remaining isooctyl alcohol continue underpressure distillation again and obtain product.
2. according to the method for claim 1, it is characterized in that in the described step 1 that inventing a kind of is the method for feedstock production to mesitylenic acid with facile halogenated benzoic acid.
3. according to the method for claim 1, it is characterized in that in the described step 1 that having introduced catalysts Cat-1 is tetrabutylammonium chloride, Tetrabutyl amonium bromide, trimethyl benzyl ammonia chloride, polyoxyethylene glycol 800~1200, phase-transfer catalysts such as glycerine; Catalyzer Cat-2 is CuCl 2, Cu 2O, Cu powder, CoCl 2This two classes catalyzer makes reaction conditions more gentle when accelerating speed of reaction; Excessive dimethylamine is beneficial to promotion reaction conversion as the acid binding agent of reaction, but and multistep recycled.
4. according to the method for claim 1, it is characterized in that in the described step 2, solvent orange 2 A is benzene,toluene,xylene, chlorobenzene and dichlorobenzene, is preferably dimethylbenzene; Reaction is preferably at 80~150 ℃; Catalyzer Ca t-3 is a tosic acid, sulfuric acid, phosphoric acid, boric acid and tetra-sodium, preferential phosphoric acid; The post processing mode that adopts is: reaction solution is neutralized to neutrality, leaves standstill to tell organic layer, sloughs solvent and residual raw materials, gets the different monooctyl ester of p-(dimethylamino)-benzoic acid (EHA).
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CN102746172A (en) * 2012-06-25 2012-10-24 湖北远成药业有限公司 Preparation method of dimethylaminocinnamaldehyde
CN107935817A (en) * 2017-12-12 2018-04-20 浙江优创材料科技股份有限公司 Isooctyl p-dimethylaminobenzoate crude product recycles the devices and methods therefor of isooctanol
CN108546232A (en) * 2018-05-22 2018-09-18 湖北汇达科技发展有限公司 A kind of monosubstituted or disubstituted benzene formic ether compounds preparation methods

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102746172A (en) * 2012-06-25 2012-10-24 湖北远成药业有限公司 Preparation method of dimethylaminocinnamaldehyde
CN102746172B (en) * 2012-06-25 2014-07-30 湖北远成赛创科技有限公司 Preparation method of dimethylaminocinnamaldehyde
CN107935817A (en) * 2017-12-12 2018-04-20 浙江优创材料科技股份有限公司 Isooctyl p-dimethylaminobenzoate crude product recycles the devices and methods therefor of isooctanol
CN107935817B (en) * 2017-12-12 2023-08-29 浙江优创材料科技股份有限公司 Device and method for recovering isooctyl alcohol from isooctyl p-dimethylaminobenzoate crude product
CN108546232A (en) * 2018-05-22 2018-09-18 湖北汇达科技发展有限公司 A kind of monosubstituted or disubstituted benzene formic ether compounds preparation methods
CN108546232B (en) * 2018-05-22 2020-10-16 湖北汇达科技发展有限公司 Preparation method of mono-substituted or di-substituted benzoate compound

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