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CN102603531A - Method for preparing 2,3,4,5-tetrafluoro methyl benzoate in series reaction - Google Patents

Method for preparing 2,3,4,5-tetrafluoro methyl benzoate in series reaction Download PDF

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CN102603531A
CN102603531A CN2012100399351A CN201210039935A CN102603531A CN 102603531 A CN102603531 A CN 102603531A CN 2012100399351 A CN2012100399351 A CN 2012100399351A CN 201210039935 A CN201210039935 A CN 201210039935A CN 102603531 A CN102603531 A CN 102603531A
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tetrachloro
benzoic acid
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陈熙强
王勇
裴文
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XIANJU COUNTY OF DAYS CHEMICAL CO
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Abstract

The invention discloses a method for preparing 2,3,4,5-tetrafluoro methyl benzoate in series reaction, belonging to the technical field of fine chemical synthesis. The method comprises the following steps: carrying out fluorination reaction at 20-150 DEG C for 1-15 hours using ionic liquid, fluoride, a solid base catalyst and 2,3,4,5-tetrachlorophthalic anhydride, cooling the reaction solution to room temperature after the reaction is complete, adding methanol to perform esterification and decarboxylation reaction, and carrying out post treatment to obtain 2,3,4,5-tetrafluoro methyl benzoate. The preparation method provided by the invention uses ionic liquid and magnetic solid base catalyst, and performs series reaction between various components; the method is simple in operation, convenient in post treatment, good in technical performance, and low in environmental pollution; the yield of the obtained 2,3,4,5-tetrafluoro methyl benzoate is above 92%, and the content is >= 99.2%. The method is a green chemical synthesis technology and is suitable for industrialized production.

Description

A kind of series process prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters
Technical field
The invention belongs to technical field of fine chemical synthesis, be specifically related to a kind of method that heterogeneous catalysis cascade reaction technology prepares methyl 4-fluorobenzene of in ion liquid medium, using.
Background technology
2; 3; 4; The 5-methyl 4-fluorobenzene is a kind of important pharmaceutical intermediate, be mainly used in synthetic third generation QNS (lomefloxacin (lomefloxacin), Ofloxacine USP 23 (ofloxacin), the 4th generation QNS (RWJ 25213-097 (levofloxacin), sparfloxacin (sparfloxacin).Also be widely used in synthetic resins, electro-conductive material and liquid crystal material etc.The synthetic the earliest of methyl 4-fluorobenzene can be traced back to the twenties in last century, mainly is that raw material is respectively through imide route (comprise imidization, fluoridize, hydrolysis, decarboxylation and esterification five steps reaction) and through synthetic the making of chloride route (comprise hydrolysis, chloride, fluoridize, hydrolysis, decarboxylation and esterification) with the tetrachlorophthalic acid.But above-mentioned operational path is long, and cost is high, and environmental pollution is bigger.Along with the growth of fluoro-carbostyril class pharmaceutical requirements amount, at present State Planning Commission and national medical general bureau in " " eight or five " national levelization doctor series products tackle key problems guide ", clearly to adopt tetrafluorobenzoic aid and ester compound be that the new technology route of main raw material is the developing trend of national new drug.Therefore it is simple and direct to develop a reaction process, and flow process is short, pollutes little, with low cost methyl 4-fluorobenzene synthetic route, and making it as early as possible, large-scale industrial production has important social meaning and economic worth.
Summary of the invention
To the problems referred to above that exist in the prior art, the object of the present invention is to provide a kind of method that heterogeneous catalysis cascade reaction technology prepares methyl 4-fluorobenzene of in ion liquid medium, using.
Described a kind of series process prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that comprising the steps:
1) described 2,3,4,5 tetra fluoro benzoic acid methyl esters, 2,3,4,5-tetrachloro-phthalic acid acid anhydride and ionic liquid are respectively shown in formula I, formula II and formula III:
Figure 2012100399351100002DEST_PATH_IMAGE001
Figure 652247DEST_PATH_IMAGE002
?
Figure 788830DEST_PATH_IMAGE003
(Ⅰ) (Ⅱ) (Ⅲ)
2) in reaction flask, add successively ionic liquid shown in formula III, fluorizating agent, solid base catalyst and shown in formula II 2,3,4,5-tetrachloro-phthalic acid acid anhydride is 20 ℃-150 ℃ in temperature
Carried out fluoridation 1-15 hour, reaction is cooled to room temperature with reaction solution after finishing; Add methyl alcohol again and carry out esterification and decarboxylic reaction, after reaction finishes, through aftertreatment obtain title product shown in formula I 2; 3,4, the 5-methyl 4-fluorobenzene; Described fluorizating agent is an alkaline metal fluoride cpd, and described esterification and decarboxylic reaction temperature are 30 ℃-100 ℃; Reaction times is 1-15 hour.
Described a kind of series process preparation 2,3,4; The method of 5-methyl 4-fluorobenzene; It is characterized in that step 2) described alkaline metal fluoride cpd is any one in Potassium monofluoride, Sodium Fluoride or the cesium fluoride, 2,3; 4, the molar ratio of 5-tetrachloro-phthalic acid acid anhydride and alkaline metal fluoride cpd is 1:4-15.
Described a kind of series process prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that step 2) described ionic liquid is 3-Methylimidazole inorganic acid salt or 1-alkyl-3-Methylimidazole inorganic acid salt [Bmim] shown in formula III +L -, R is that H or carbon atom quantity are the alkyl of 1-18 in the formula, L is BF 4, PF 6, OA COr a kind of among the OH, its consumption is 2,3,4, the 1-20 of 5-tetrachloro-phthalic acid acid anhydride quality is doubly.
Described a kind of series process prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that step 2) described solid base catalyst is magnetic solid base catalyst, its consumption is 2,3,4, the 1-20% of 5-tetrachloro-phthalic acid acid anhydride mass percent.
Described a kind of series process prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that step 2) described post-treating method is for to use extracted in toluene with reaction solution, again through distill the 2,3,4,5 tetra fluoro benzoic acid methyl esters.
Described a kind of series process prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that step 2) described methyl alcohol and 2,3,4, the molar ratio 1-5:1 of 5-tetrachloro-phthalic acid acid anhydride.
Described a kind of series process prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that step 2) described alkaline metal fluoride cpd is Potassium monofluoride.
Described a kind of series process preparation 2; 3; 4, the method for 5-methyl 4-fluorobenzene is characterized in that step 2) described in ionic liquid be 1-alkyl-3-methyl imidazolium tetrafluoroborate; Wherein alkyl is that carbon atom quantity is the alkyl of 1-18, is preferably 1-butyl-3-methyl imidazolium tetrafluoroborate or 1-ethyl-3-methyl imidazolium tetrafluoroborate.
Described a kind of series process prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that step 2) consumption of described solid base catalyst is 2,3,4, the 5-15% of 5-tetrachloro-phthalic acid acid anhydride mass percent.
Described a kind of series process preparation 2; 3,4, the method for 5-methyl 4-fluorobenzene; The preparation method who it is characterized in that described magnetic solid base catalyst is following: the magnetic solid base that magnetic mg_al hydrotalcite makes; Be magnesium aluminum-hydrotalcite to be carried out magnetic modify, make it have magnetic and catalysis dual-use function, reach the purpose that improves catalytic activity.Particularly, the preparation method of described magnetic solid base catalyst is following: get a certain amount of magnetic colloidal sol and join in the reaction flask, add zero(ppm) water again; Stirring at room, magnesium nitrate and the aluminum nitrate getting the magnalium ratio and be 1: 2 are mixed with solution, and other joins the sodium hydroxide solution of pH=10-13; Two kinds of solution are added in the reaction flask; 110 ℃ of stirrings, washing and drying makes magnetic mg_al hydrotalcite, forms magnetic solid base 450~500 ℃ of high-temperature roastings then.Magnetic colloidal sol is to adopt chemical coprecipitation, with Fe 3+And Fe 2+Vitriol or muriate in excessive alkali, mix to stir in the ratio of 1:1 and make.Specifically can be with reference to the 29th volume the 3rd phase (in March, 2002) " preparation of magnetic mg_al hydrotalcite solid alkali and sign " of applicating technology.
Reaction equation of the present invention is following:
Figure DEST_PATH_IMAGE004
Compound method of the present invention is preparation according to the following steps specifically: with 1 mole 2,3,4, and 5-tetrachloro-benzoic acid acid anhydride, 4-15 mole metal fluorochemical; Quality is 2,3,4; 5-tetrachloro-phthalic acid acid anhydride 1-20 ionic liquid doubly, quality is 2,3 of 1-20%; 4, the magnetic solid base catalyst of 5-tetrachloro-phthalic acid acid anhydride quality adds in the reaction flask successively, carries out fluoridation 1-15 hour at 20 ℃-150 ℃ earlier; Then,, add the methyl alcohol of 1-5 mole again with reaction solution cooling, 30 ℃-100 ℃ reactions 1-15 hour, after reaction finishes, with reaction solution with extracted in toluene after, distill the 2,3,4,5 tetra fluoro benzoic acid methyl esters.
Through adopting above-mentioned technology, compared with prior art, beneficial effect of the present invention is following:
1) the present invention is through replacing the liquid alkali catalyst catalyse organic reaction not only can reduce pollution with solid base catalyst; Can also increase activity of such catalysts and selectivity; Simultaneously through reclaiming (regeneration) and reusing the work-ing life of improving catalyzer; Be to realize an eco-friendly important channel, solid acid alkali catalytic has become one of main contents of Green Chemistry research;
2) the present invention is through adopting many group cascade reactions; Cascade reaction is claimed the domino reaction again, is meant the process that under identical conditions, forms two keys or multikey, and next step reaction of this process is after last single step reaction; Therefore cascade reaction is the process of differentiating in a reaction times; The polycomponent cascade reaction has very big meliority with synthetic the comparing of changes traditional step, and it can reduce reactions step greatly, saves the loaded down with trivial details sepn process of a lot of complicacies;
3) the present invention as solvent, is the fluid cpds of being made up of ion fully with ionic liquid, compare with organic solvent have non-volatile; Nonflammable explosive, organism and inorganics there are good solubility, reaction can be carried out at homogeneous phase; Stable to water and air; Be convenient to operation and processing, be prone to reclaim, but also catalysis is quickened the process of chemical reaction and improved the selectivity of reaction;
4) the present invention has used ionic liquid and magnetic solid base catalyst in reaction process, and various ingredients is carried out cascade reaction, and is simple to operate; Convenient post-treatment, technological performance, environmental pollution is little, obtain 2; 3,4,5-methyl 4-fluorobenzene yield is up to more than 92%; Content >=99.2% is a kind of Green Chemistry synthetic technology, is suitable for suitability for industrialized production.
Embodiment
Below in conjunction with specific embodiment the present invention is described further, but protection scope of the present invention is not limited to this.
Embodiment 1: with 2,3,4, and 5-tetrachloro-benzoic acid acid anhydride 286 grams (1 mole), Potassium monofluoride 232 grams (4 moles); 1-butyl-3-methyl imidazolium tetrafluoroborate 858 grams, magnetic solid base catalyst 14.3 grams that embodiment 1 makes add in the reaction flask,, after 5 hours reaction solution are cooled off 80 ℃ of reactions; Add methyl alcohol 96 grams (2 moles), 60 ℃ of reactions 10 hours, after reaction finishes, with reaction solution with extracted in toluene after; After the distillation, get 2,3,4; 5-methyl 4-fluorobenzene 199 grams, yield 96%, boiling point 220-249 ℃, fusing point 126-128 ℃.Content >=99.5%.
The solid base catalyst that uses among the present invention is magnetic solid base catalyst, and its preparation method is with reference to the 29th volume the 3rd phase (in March, 2002) " preparation of magnetic mg_al hydrotalcite solid alkali and sign " of applicating technology.
In the present embodiment, it is 2,3 that metal fluoride uses mole number; 4; 5-tetrachloro-phthalic acid acid anhydride 4-15 Sodium Fluoride or cesium fluoride doubly replaces Potassium monofluoride, and it is 2,3 that ionic liquid uses consumption; 4, the 1-20 of 5-tetrachloro-phthalic acid acid anhydride quality 3-Methylimidazole inorganic acid salt or 1-alkyl-3-Methylimidazole inorganic acid salt [Bmim] doubly +L -, R is that H or carbon atom quantity are the alkyl of 1-18 in the formula, L is BF 4, PF 6, OA COr a kind of replacement 1-butyl-3-methyl imidazolium tetrafluoroborate among the OH, all can obtain same effect.
Embodiment 2: with 2,3,4, and 5-tetrachloro-benzoic acid acid anhydride 286 grams (1 mole), Sodium Fluoride 630 grams; 1-amyl group-3-Methylimidazole hexafluorophosphate 5720 grams, magnetic solid base catalyst 42.9 grams add in the reaction flask, after 15 hours, reaction solution are cooled to room temperature 20 ℃ of reactions; Add methyl alcohol 160 grams (5 moles), 30 ℃ of reactions 15 hours, after reaction finishes, with reaction solution with extracted in toluene after, after the distillation; Get 2,3,4,5 tetra fluoro benzoic acid methyl esters 194.8 grams; Yield 94%, boiling point 220-249 ℃, fusing point 126-128 ℃, content 99.3%.
Embodiment 3: with 2,3,4, and 5-tetrachloro-benzoic acid acid anhydride 286 grams (1 mole), cesium fluoride 608 grams (4 moles); 1-nonyl-3-N-Methylimidazoleacetic salt 5000 grams, magnetic solid base catalyst 2.86 grams add in the reaction flask,, after 2 hours reaction solution are cooled off 150 ℃ of reactions; Add methyl alcohol 32 grams (1 mole), 100 ℃ of reactions 1 hour, after reaction finishes, with reaction solution with extracted in toluene after, after the distillation; Get 2,3,4,5 tetra fluoro benzoic acid methyl esters 190.7 grams; Yield 92%, boiling point 220-249 ℃, fusing point 126-128 ℃, content 99.2%.
Embodiment 4: with 2,3,4, and 5-tetrachloro-benzoic acid acid anhydride 286 grams (1 mole), Potassium monofluoride 580 grams (10 moles); 1-nonyl-3-Methylimidazole subsalt 2860 grams, magnetic solid base catalyst 30 grams add in the reaction flask,, after 10 hours reaction solution are cooled off 90 ℃ of reactions; Add methyl alcohol 960 grams (3 moles), 70 ℃ of reactions 8 hours, after reaction finishes, with reaction solution with extracted in toluene after, after the distillation; Get 2,3,4,5 tetra fluoro benzoic acid methyl esters 203 grams; Yield 98%, boiling point 220-249 ℃, fusing point 126-128 ℃, content 99.7%.
Embodiment 5: with 2,3,4, and 5-tetrachloro-benzoic acid acid anhydride 286 grams (1 mole), cesium fluoride 630 grams (15 moles); 1-ethyl-3-methyl imidazolium tetrafluoroborate 45 grams, magnetic solid base catalyst 57.6 grams add in the reaction flask,, after 15 hours reaction solution are cooled off 60 ℃ of reactions; Add methyl alcohol 160 grams (5 moles), 60 ℃ of reactions 15 hours, after reaction finishes, with reaction solution with extracted in toluene after, after the distillation; Get 2,3,4,5 tetra fluoro benzoic acid methyl esters 197 grams; Yield 95%, boiling point 220-249 ℃, fusing point 126-128 ℃, content 99.6%.
Embodiment 6: with 2,3,4, and 5-tetrachloro-benzoic acid acid anhydride 286 grams (1 mole), Potassium monofluoride 378 grams (9 moles); 1-tridecyl-3-methyl imidazolium tetrafluoroborate 3432 grams, magnetic solid base catalyst 34.3 grams add in the reaction flask,, after 8 hours reaction solution are cooled off 90 ℃ of reactions; Add methyl alcohol 128 grams (4 moles), 70 ℃ of reactions 9 hours, after reaction finishes, with reaction solution with extracted in toluene after, after the distillation; Get 2,3,4,5 tetra fluoro benzoic acid methyl esters 201 grams; Yield 97%, boiling point 220-249 ℃, fusing point 126-128 ℃, content 99.7%.
Embodiment 7: with 2,3,4, and 5-tetrachloro-benzoic acid acid anhydride 286 grams (1 mole), Potassium monofluoride 378 grams (9 moles); 1-butyl-3-methyl imidazolium tetrafluoroborate 2860 grams, magnetic solid base catalyst 28.6 grams add in the reaction flask,, after 8 hours reaction solution are cooled off 90 ℃ of reactions; Add methyl alcohol 128 grams (4 moles), 70 ℃ of reactions 10 hours, after reaction finishes, with reaction solution with extracted in toluene after, after the distillation; Get 2,3,4,5 tetra fluoro benzoic acid methyl esters 201 grams; Yield 97%, boiling point 220-249 ℃, fusing point 126-128 ℃, content 99.6%.

Claims (9)

1. a series process prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that comprising the steps:
1) described 2,3,4,5 tetra fluoro benzoic acid methyl esters, 2,3,4,5-tetrachloro-phthalic acid acid anhydride and ionic liquid are respectively shown in formula I, formula II and formula III:
Figure 435981DEST_PATH_IMAGE002
(Ⅰ) (Ⅱ) (Ⅲ)
2) in reaction flask, add successively ionic liquid shown in formula III, fluorizating agent, solid base catalyst and shown in formula II 2,3,4,5-tetrachloro-phthalic acid acid anhydride is 20 ℃-150 ℃ in temperature
Carried out fluoridation 1-15 hour, reaction is cooled to room temperature with reaction solution after finishing; Add methyl alcohol again and carry out esterification and decarboxylic reaction, after reaction finishes, through aftertreatment obtain title product shown in formula I 2; 3,4, the 5-methyl 4-fluorobenzene; Described fluorizating agent is an alkaline metal fluoride cpd, and described esterification and decarboxylic reaction temperature are 30 ℃-100 ℃; Reaction times is 1-15 hour.
2. a kind of series process preparation 2,3,4 according to claim 1; The method of 5-methyl 4-fluorobenzene; It is characterized in that step 2) described alkaline metal fluoride cpd is any one in Potassium monofluoride, Sodium Fluoride or the cesium fluoride, 2,3; 4, the molar ratio of 5-tetrachloro-phthalic acid acid anhydride and alkaline metal fluoride cpd is 1:4-15.
3. a kind of series process preparation 2 according to claim 1; 3; 4, the method for 5-methyl 4-fluorobenzene is characterized in that step 2) described ionic liquid is 3-Methylimidazole inorganic acid salt or 1-alkyl-3-Methylimidazole inorganic acid salt [Bmim] shown in formula III +L -, R is that H or carbon atom quantity are the alkyl of 1-18 in the formula, L is BF 4, PF 6, OA COr a kind of among the OH, its consumption is 2,3,4, the 1-20 of 5-tetrachloro-phthalic acid acid anhydride quality is doubly.
4. a kind of series process preparation 2,3,4 according to claim 1; The method of 5-methyl 4-fluorobenzene is characterized in that step 2) described solid base catalyst is magnetic solid base catalyst, its consumption is 2; 3,4, the 1-20% of 5-tetrachloro-phthalic acid acid anhydride mass percent.
5. a kind of series process according to claim 1 prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that step 2) described post-treating method is for to use extracted in toluene with reaction solution, again through distill the 2,3,4,5 tetra fluoro benzoic acid methyl esters.
6. a kind of series process according to claim 1 prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that step 2) described methyl alcohol and 2,3,4, the molar ratio 1-5:1 of 5-tetrachloro-phthalic acid acid anhydride.
7. a kind of series process according to claim 2 prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that step 2) described alkaline metal fluoride cpd is Potassium monofluoride.
8. a kind of series process preparation 2 according to claim 3; 3; 4, the method for 5-methyl 4-fluorobenzene is characterized in that step 2) described in ionic liquid be 1-alkyl-3-methyl imidazolium tetrafluoroborate; Wherein alkyl is that carbon atom quantity is the alkyl of 1-18, is preferably 1-butyl-3-methyl imidazolium tetrafluoroborate or 1-ethyl-3-methyl imidazolium tetrafluoroborate.
9. a kind of series process according to claim 4 prepares the method for 2,3,4,5 tetra fluoro benzoic acid methyl esters, it is characterized in that step 2) consumption of described solid base catalyst is 2,3,4, the 5-15% of 5-tetrachloro-phthalic acid acid anhydride mass percent.
CN201210039935.1A 2012-02-22 2012-02-22 Method for preparing 2,3,4,5-tetrafluoro methyl benzoate in series reaction Expired - Fee Related CN102603531B (en)

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Cited By (1)

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CN106565421A (en) * 2016-11-08 2017-04-19 岳阳中科华昂精细化工科技有限公司 Preparation method of 2,3,5,6-tetrafluorohydrazine-1,4-benzene dimethanol

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CN1265644A (en) * 1997-08-01 2000-09-06 拜尔公司 Method for preparing 3-cyano-2,4-dihalogen-5-flour-benzoic acid
CN1335301A (en) * 1996-02-23 2002-02-13 拜尔公司 3-cyano-2, 4, 5-trifluorobenzoic acid and derivatives thereof and application thereof

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Publication number Priority date Publication date Assignee Title
CN1112105A (en) * 1993-09-18 1995-11-22 赫彻斯特股份公司 Method for preparation 3-hydroxy-2,4,5-trifluorbenzoealkyl formate and/or 3-alkoxy-2,4,5-trifluorbenzoealkyformate
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CN106565421A (en) * 2016-11-08 2017-04-19 岳阳中科华昂精细化工科技有限公司 Preparation method of 2,3,5,6-tetrafluorohydrazine-1,4-benzene dimethanol
CN106565421B (en) * 2016-11-08 2019-04-26 岳阳中科华昂精细化工科技有限公司 A kind of preparation method of 2,3,5,6-tetrafluoro-1,4-benzenedimethanol

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