CN104829455B - A kind of method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate - Google Patents

A kind of method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate Download PDF

Info

Publication number
CN104829455B
CN104829455B CN201510209805.1A CN201510209805A CN104829455B CN 104829455 B CN104829455 B CN 104829455B CN 201510209805 A CN201510209805 A CN 201510209805A CN 104829455 B CN104829455 B CN 104829455B
Authority
CN
China
Prior art keywords
trifluoroacetic
ethyl acetate
mixed
metal salt
synthesizing
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.)
Active
Application number
CN201510209805.1A
Other languages
Chinese (zh)
Other versions
CN104829455A (en
Inventor
王玉林
吕亮
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.)
Quzhou University
Original Assignee
Quzhou University
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 Quzhou University filed Critical Quzhou University
Priority to CN201510209805.1A priority Critical patent/CN104829455B/en
Publication of CN104829455A publication Critical patent/CN104829455A/en
Application granted granted Critical
Publication of CN104829455B publication Critical patent/CN104829455B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/30Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
    • C07C67/333Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton
    • C07C67/343Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/24Nitrogen compounds
    • B01J27/25Nitrates

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

The invention discloses a kind of method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate, comprises the following steps:A divalence and trivalent metal salt mixed aqueous solution are mixed by () with NaOH and sodium carbonate mixed aqueous solution, make solution ph for after 8.5~10.5, aging, filter, dry, grind to obtain catalyst precarsor;B catalyst precarsor roasting that step (a) is obtained by (), cooling, are then added in the KF aqueous solution, stir, filter, wash and be vacuum dried, roasting is obtained catalyst;C catalyst that step (b) is obtained by () is 0.001~0.05 with ethyl acetate, Trifluoroacetic Acid Ethyl Ester in mass ratio:2~5:1,5~10h is reacted at 40~60 DEG C, rectifying, cooling obtain condensation product, add the mixed solution of formic acid and ethyl acetate again in the condensation product for obtaining, 0.5~3h, cooling is reacted at 30~55 DEG C, filter, filtrate decompression rectifying obtains trifluoroacetic ethyl acetoacetate.The present invention has the advantages that process is simple, high income, safety and environmental protection.

Description

A kind of method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate
Technical field
The present invention relates to the synthetic method of trifluoroacetic ethyl acetoacetate, more particularly to one kind catalyze and synthesize trifluoroacetyl acetic acid The method of ethyl ester.
Background technology
Trifluoroacetic ethyl acetoacetate is the important intermediate of the fluorochemicals such as synthetic pesticide, medicine, with trifluoroacetyl second Acetoacetic ester is raw material or as key intermediate, can produce all kinds of containing heterocyclic drug, efficient pesticides and highy potent herbicide, or It is the important intermediate for obtaining synthesizing these products.The product variety that has developed at present has pyridines, miazines, pyroles, sulphur Ureide derivative compound and fluorine-containing organic acid and its salt etc..In view of the important use of trifluoroacetic ethyl acetoacetate, study further, Optimize its synthetic technology, accelerate its production industrially and application has great importance.
At present, the synthesis of trifluoroacetic ethyl acetoacetate mainly take in atent solvent and highly basic effect under, to trifluoro second Acetoacetic ester and ethyl acetate carry out Claisen condensation.
If Edward Micinski is with hexamethylene (or dodecane) as solvent, in highly basic (metallic sodium, caustic alcohol or hydrogenation Sodium) effect under Trifluoroacetic Acid Ethyl Ester and ethyl acetate are carried out Claisen condensation, unreacted reagent and life are removed by rectifying The ethanol for becoming obtains condensation product;3- alkoxyl -3- is obtained afterwards with inorganic acid (hydrochloric acid, sulfuric acid or phosphoric acid) neutralization condensation product Hydroxyl -4,4,4- trifluoroacetic acid ethyl ester;Again with the acetylation reagent such as carboxylic acid halides (or acetic anhydride) by its acetylation, separated after obtain Trifluoroacetic ethyl acetoacetate (Edward Micinski.Preparation of Alkyl Trifluoroacetoacetate [p].US:4647689,1987-3-3.).
And for example Louis Amiet and Bernard Langlois be with hexamethylene as solvent, by trifluoro under caustic alcohol effect Ethyl acetate and ethyl acetate carry out Claisen condensation, and the ethanol for removing unreacted reagent and generation by rectifying is condensed Product;Afterwards with Bronsted acid (formic acid) neutralize condensation product, then separated after obtain trifluoroacetic ethyl acetoacetate (Louis Amiet, Bernard Langlois.Process for The Preparation of Ethyl Trifluoroacetoacetate [p].US:4883904,1989-11-28.).
For another example Cheong Kuoc Va etc. is condensed with Trifluoroacetic Acid Ethyl Ester under caustic alcohol effect with excessive ethyl acetate, rectifying Neutralize condensation product with the concentrated sulfuric acid after separating, then be rectifying to obtain trifluoroacetic ethyl acetoacetate (Cheong Kuoc Va, Zheng Chunzhi. trifluoro The synthesis [J] of ethyl acetoacetate. agricultural chemicals, 2007,46 (12):833-834.).
From the point of view of the result of study of existing report, it is synthesis three that Trifluoroacetic Acid Ethyl Ester and ethyl acetate carry out Claisen condensation The committed step of acetyl fluoride ethyl acetate.Claisen condensation adopts strong alkali as a catalyst, predominantly metallic sodium, caustic alcohol or hydrogenation Sodium etc., directly adopts metallic sodium, then react acutely and have hydrogen to generate, dangerous big;Sodium hydride activity is high, in the reaction A large amount of hydrogen can be produced, thus dangerous high;According to caustic alcohol, in addition to it need to consume a large amount of caustic alcohols, also a large amount of ethanol are generated, The separation of impact condensation product, in addition also has substantial amounts of sodium salt to generate during the course of the reaction, needs separation and recovery, high cost, environmental protection Pressure is big.
Content of the invention
The present invention is for the catalysis conjunction in place of the deficiencies in the prior art, providing a kind of process is simple, high income, safety and environmental protection The method for becoming trifluoroacetic ethyl acetoacetate.
In order to solve above-mentioned technical problem, the technical solution used in the present invention is:One kind catalyzes and synthesizes trifluoroacetyl acetic acid The method of ethyl ester, comprises the following steps:
A divalence and trivalent metal salt mixed aqueous solution are mixed by () with NaOH and sodium carbonate mixed aqueous solution, adjustment After solution ph is 8.5~10.5, in 50~75 DEG C of aging 15~25h, filter cake is filtrated to get, by Washing of Filter Cake to neutrality, then 10~15h is dry at 70~90 DEG C, grind to obtain catalyst precarsor;
B catalyst precarsor that step (a) is obtained by () is cooled down, is then added to KF water in 400~550 DEG C of 2~5h of roasting In solution, under room temperature, 20~48h is stirred, after filtering, wash and being vacuum dried, 3~8h of roasting at 400~550 DEG C, cooling, Prepared catalyst;
C catalyst that step (b) is obtained by () is 0.001~0.05 with ethyl acetate, Trifluoroacetic Acid Ethyl Ester in mass ratio: 2~5:1,5~10h is reacted at 40~60 DEG C, rectifying, cooling obtain condensation product, then add in the condensation product for obtaining Formic acid and the mixed solution of ethyl acetate, react 0.5~3h at 30~55 DEG C, cool down, and filter, filtrate decompression rectifying is obtained To trifluoroacetic ethyl acetoacetate.
The total mole number of the total mole number of described divalent metal salt and trivalent metal salt and NaOH and sodium carbonate it Than being preferably 0.4~0.5:.1.
Bivalent metal ion and trivalent metal ion mole in described divalent metal salt and trivalent metal mixed salt solution Than being preferably 2~4:1.
In described NaOH and sodium carbonate mixture, NaOH is preferably 4~10 with the mass ratio of sodium carbonate: 1.
Described divalent metal salt is preferably Mg (NO3)2·6H2O、Co(NO3)2·6H2O、Cu(NO3)2·3H2O、Mn (NO3)2·4H2The mixture of one or more in O.
Described trivalent metal salt is preferably Al (NO3)3·9H2O or Fe (NO3)3·9H2The mixture of O or both.
Described KF is preferably 1 with the ratio of the total mole number of divalent metal salt and trivalent metal salt:10~25.
The mixed solution of described formic acid and ethyl acetate is preferably 0.5~1.5 with the mass ratio of Trifluoroacetic Acid Ethyl Ester:1.
In the mixed solution of described formic acid and ethyl acetate, formic acid is preferably 1 with the mass ratio of ethyl acetate:0.3~3.
The catalyst that the present invention is prepared is stratified material, is a kind of polynary houghite, and its chemical composition is [M2+ 1- xM3+ x(OH)2]x+(An- x/n)·mH2O, M2+And M3+Divalence and trivalent metal ion, A are represented respectivelyn-Anion is represented, x is M3+/ (M2++M3+) mol ratio, M2+It is Ca2+、Mg2+、Co2+、Ni2+、Mn2+、Cu2+、Fe2+In one or more, M3+It is Fe3+、Al3 +、Cr3+、Sc3+In one or more, An-It is CO3 2-、OH-、NO3 -、Cl-、SO4 2-、PO4 3-In one or two.
The catalyst of the present invention can be recycled, further reduce three waste discharge, reduce into through simple regeneration This.Catalyst recovery process is:By the catalyst being recovered by filtration, after fully being washed with organic solvent, go in Muffle kiln roasting Except organic matter, sintering temperature are 300 DEG C~600 DEG C, preferably 400 DEG C~500 DEG C, room temperature is naturally cooled to.
Compared with prior art, the present invention has advantages below:
1st, process is simple, gently steadily, product is easily separated, catalyst reusable edible, it is easy to industrial metaplasia for course of reaction Produce;
2nd, safety and environmental protection, in preparation process, the inflammable gas such as no hydrogen is generated, and catalyst can be circulated through simple regeneration Utilize, three waste discharge is further reduced, reduces cost;
3rd, high income, good product quality, yield reach as high as 89.5% more than 87.5%;Product purity for More than 99.2%, reach as high as 99.9%.
Specific embodiment
The present invention is described in further detail with reference to specific embodiment, but protection scope of the present invention is not limited in This.
Embodiment 1
(1) in four-hole bottle, by Mg (NO3)2·6H2O 48.08g(0.1875mol)、Al(NO3)3·9H2O 23.45g (0.0625mol) I 70ml of mixed aqueous solution being configured to, with NaOH 20g (0.5mol) and sodium carbonate 3.31g (0.03125mol) II 70ml of mixed aqueous solution for preparing is mixed to get mixed solution, and the pH value for adjusting mixed solution is 8.5, stirs 30min is mixed, in 65 DEG C of aging 18h, filter cake is filtrated to get, by Washing of Filter Cake to neutrality, at 80 DEG C, 12h is dry, grind and must be catalyzed Agent precursor;
(2) roasting 3h at the catalyst precarsor for obtaining step (1) is put in Muffle furnace in 450 DEG C, nitrogen protection are lower certainly Room temperature is so cooled to.Solid after roasting is added in the 100ml 0.1mol/L KF aqueous solution, under room temperature, stirs 48h, mistake Filter, wash and be vacuum dried after, at 450 DEG C, roasting 8h, then naturally cools to room temperature under nitrogen protection, be obtained catalysis Agent;
(3) in four-hole boiling flask, it is separately added into ethyl acetate 40g, Trifluoroacetic Acid Ethyl Ester 20g and step (2) is obtained urges Agent 0.02g, reacts 6h at 40 DEG C, and rectifying removes unreacted ethyl acetate and the ethanol of generation obtains condensation product, cold But, (formic acid is 1 with ethyl acetate mass ratio then to add formic acid and ethyl acetate in the condensation product for obtaining:1) mixing is molten Liquid 10g, reacts 1h at 40 DEG C, cools down, and filters, filtrate decompression rectifying obtains trifluoroacetic ethyl acetoacetate, divides through GC/MS Analysis, purity are 99.9%, and yield is 87.9%.
Embodiment 2
(1) in four-hole bottle, by Mg (NO3)2·6H2O 51.28g(0.2mol)、Al(NO3)3·9H2O 15.01g (0.04mol)、Fe(NO3)3·9H2I 70ml of mixed aqueous solution that O 4.04g (0.01mol) is configured to, with NaOH II 70ml of mixed aqueous solution that 20.00g (0.5mol) and sodium carbonate 2.65g (0.025mol) are prepared is mixed to get mixed solution, The pH value of adjustment mixed solution is 9, stirs 30min, in 60 DEG C of aging 15h, is filtrated to get filter cake, by Washing of Filter Cake to neutrality, 15h is dry at 80 DEG C, grind to obtain catalyst precarsor;
(2) roasting 4h at the catalyst precarsor for obtaining step (1) is put in Muffle furnace in 400 DEG C, nitrogen protection are lower certainly Room temperature is so cooled to.Solid after roasting is added in the 100ml 0.15mol/L KF aqueous solution, under room temperature, stirs 40h, mistake Filter, wash and be vacuum dried after, at 400 DEG C, roasting 10h, naturally cools to room temperature under nitrogen protection, be obtained catalyst;
(3) in four-hole boiling flask, it is separately added into ethyl acetate 60g, Trifluoroacetic Acid Ethyl Ester 20g and step (2) is obtained urges Agent 0.06g, reacts 7h at 45 DEG C, and rectifying removes unreacted ethyl acetate and the ethanol of generation obtains condensation product, cold But, (formic acid is 1 with ethyl acetate mass ratio then to add formic acid and ethyl acetate in the condensation product for obtaining:2) mixing is molten Liquid 12g, reacts 2h at 35 DEG C, cools down, and filters, filtrate decompression rectifying obtains trifluoroacetic ethyl acetoacetate, divides through GC/MS Analysis, purity are 99.7%, and yield is 88.5%.
Embodiment 3
(1) in four-hole bottle, by Co (NO3)2·6H2O 17.46g(0.06mol)、Cu(NO3)2·3H2O 4.84g (0.02mol)、Mn(NO3)2·4H2O 2.45g(0.01mol)、Al(NO3)3·9H2O 7.50g(0.02mol)、Fe(NO3)3· 9H2I 50ml of mixed aqueous solution that O 4.04g (0.01mol) is configured to, with NaOH 10g (0.25mol) and sodium carbonate 1.7g (0.016mol) II 50ml of mixed aqueous solution for preparing is mixed to get mixed solution, and the pH value for adjusting mixed solution is 9.5, stirring 30min, in 55 DEG C of aging 20h, is filtrated to get filter cake, by Washing of Filter Cake to neutrality, dries 10h at 70 DEG C, grinds to obtain catalyst Precursor;
(2) roasting 5h at the catalyst precarsor for obtaining step (1) is put in Muffle furnace in 500 DEG C, adds after cooling In the 60ml0.15mol/L KF aqueous solution, under room temperature, 35h is stirred, after filtering, wash and being vacuum dried, roasting 4h at 500 DEG C, Naturally cool to room temperature under nitrogen protection, catalyst is obtained;
(3) in four-hole boiling flask, it is separately added into ethyl acetate 80g, Trifluoroacetic Acid Ethyl Ester 20g and step (2) is obtained urges Agent 0.1g, reacts 9h at 55 DEG C, and rectifying removes unreacted ethyl acetate and the ethanol of generation obtains condensation product, cold But, (formic acid is 1 with ethyl acetate mass ratio then to add formic acid and ethyl acetate in the condensation product for obtaining:2.5) mixing Solution 14g, reacts 3h at 45 DEG C, cools down, and filters, filtrate decompression rectifying obtains trifluoroacetic ethyl acetoacetate, through GC/MS Analysis, purity are 99.5%, and yield is 88.8%.
Embodiment 4
(1) in four-hole bottle, by Co (NO3)2·6H2O 17.46g(0.06mol)、Cu(NO3)2·3H2O 7.25g (0.03mol)、Al(NO3)3·9H2O 7.50g(0.02mol)、Fe(NO3)3·9H2It is mixed that O 4.04g (0.01mol) is configured to I 50ml of Heshui solution, the mixed aqueous solution II for preparing with NaOH 10g (0.25mol) and sodium carbonate 1.7g (0.016mol) 50ml is mixed to get mixed solution, and the pH value for adjusting mixed solution is 10, stirs 30min, in 75 DEG C of aging 20h, is filtrated to get Filter cake, by Washing of Filter Cake to neutrality, dries 14h at 85 DEG C, grinds to obtain catalyst precarsor;
(2) roasting 6h at the catalyst precarsor for obtaining step (1) is put in Muffle furnace in 500 DEG C, adds after cooling In the 80ml0.15mol/L KF aqueous solution, under room temperature, 30h is stirred, after filtering, wash and being vacuum dried, roasting 4h at 500 DEG C, Naturally cool to room temperature under nitrogen protection, catalyst is obtained;
(3) in four-hole boiling flask, it is separately added into ethyl acetate 100g, Trifluoroacetic Acid Ethyl Ester 20g and step (2) is obtained urges Agent 0.2g, reacts 5h at 45 DEG C, and rectifying removes unreacted ethyl acetate and the ethanol of generation obtains condensation product, cold But, (formic acid is 1 with ethyl acetate mass ratio then to add formic acid and ethyl acetate in the condensation product for obtaining:3) mixing is molten Liquid 16g, reacts 0.5h at 50 DEG C, cools down, and filters, filtrate decompression rectifying obtains trifluoroacetic ethyl acetoacetate, through GC/MS Analysis, purity are 99.2%, and yield is 87.5%.
Embodiment 5
(1) in four-hole bottle, by Co (NO3)2·6H2O 29.11g(0.1mol)、Cu(NO3)2·3H2O 15.70g (0.0650mol)、Al(NO3)3·9H2O 30.95g (0.0825mol), I 80ml of mixed aqueous solution being configured to, with hydroxide II 80ml of mixed aqueous solution that sodium 20g (0.5mol) and sodium carbonate 4.37g (0.04125mol) are prepared is mixed to get mixed solution, Adjustment mixed solution pH value be 10.5, stir 30min, in 70 DEG C of aging 20h, be filtrated to get filter cake, by Washing of Filter Cake in Property, 13h is dry at 75 DEG C, grinds to obtain catalyst precarsor;
(2) roasting 7h at the catalyst precarsor for obtaining step (1) is put in Muffle furnace in 500 DEG C, adds after cooling In the 120ml0.1mol/L KF aqueous solution, under room temperature, 25h is stirred, after filtering, wash and being vacuum dried, roasting 4h at 500 DEG C, Naturally cool to room temperature under nitrogen protection, catalyst is obtained;
(3) in four-hole boiling flask, it is separately added into ethyl acetate 50g, Trifluoroacetic Acid Ethyl Ester 20g and step (2) is obtained urges Agent 0.5g, reacts 8h at 50 DEG C, and rectifying removes unreacted ethyl acetate and the ethanol of generation obtains condensation product, cold But, (formic acid is 2 with ethyl acetate mass ratio then to add formic acid and ethyl acetate in the condensation product for obtaining:1) mixing is molten Liquid 20g, reacts 2.5h at 55 DEG C, cools down, and filters, filtrate decompression rectifying obtains trifluoroacetic ethyl acetoacetate, through GC/MS Analysis, purity are 99.3%, and yield is 88.5%.
Embodiment 6
(1) in four-hole bottle, by Co (NO3)2·6H2O 17.46g(0.06mol)、Mn(NO3)2·4H2O 7.50g (0.03mol)、Al(NO3)3·9H2O 7.50g(0.02mol)、Fe(NO3)3·9H2It is mixed that O 4.04g (0.01mol) is configured to I 50ml of Heshui solution, the mixed aqueous solution II for preparing with NaOH 10g (0.25mol) and sodium carbonate 1.7g (0.016mol) 50ml is mixed to get mixed solution, and the pH value for adjusting mixed solution is 9, stirs 30min, in 50 DEG C of aging 25h, is filtrated to get filter Cake, by Washing of Filter Cake to neutrality, dries 10h at 90 DEG C, grinds to obtain catalyst precarsor;
(2) roasting 8h at the catalyst precarsor for obtaining step (1) is put in Muffle furnace in 550 DEG C, adds after cooling In the 60ml0.1mol/L KF aqueous solution, under room temperature, 20h is stirred, after filtering, wash and being vacuum dried, roasting 4h at 500 DEG C, Naturally cool to room temperature under nitrogen protection, catalyst is obtained;
(3) in four-hole boiling flask, it is separately added into ethyl acetate 100g, Trifluoroacetic Acid Ethyl Ester 20g and step (2) is obtained urges Agent 1g, reacts 10h at 60 DEG C, and rectifying removes unreacted ethyl acetate and the ethanol of generation obtains condensation product, cooling, (formic acid is 3 with ethyl acetate mass ratio to add formic acid and ethyl acetate again in the condensation product for obtaining:1) mixed solution 30g, reacts 1.5h at 30 DEG C, cools down, and filters, filtrate decompression rectifying obtains trifluoroacetic ethyl acetoacetate, divides through GC/MS Analysis, purity are 99.5%, and yield is 89.5%.

Claims (6)

1. a kind of method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate, it is characterised in that comprise the following steps:
A divalent metal salt and trivalent metal salt mixed aqueous solution are mixed by () with NaOH and sodium carbonate mixed aqueous solution, institute In the divalent metal salt that states and trivalent metal mixed salt solution, bivalent metal ion and trivalent metal ion mol ratio are 2~4:1, Described divalent metal salt is Mg (NO3)2·6H2O、Co(NO3)2·6H2O、Cu(NO3)2·3H2O、Mn(NO3)2·4H2In O One or more of mixture, described trivalent metal salt are Al (NO3)3·9H2O or Fe (NO3)3·9H2The mixing of O or both Thing, after adjustment solution ph is 8.5~10.5, in 50~75 DEG C of aging 15~25h, is filtrated to get filter cake, by Washing of Filter Cake extremely Neutrality, then 10~15h is dry at 70~90 DEG C, grind to obtain catalyst precarsor;
B catalyst precarsor that step (a) is obtained by () is cooled down, is then added to the KF aqueous solution in 400~550 DEG C of 2~5h of roasting In, 20~48h is stirred under room temperature, after filtering, wash and being vacuum dried, 3~8h of roasting at 400~550 DEG C, cooling, it is obtained Catalyst;
C catalyst that step (b) is obtained by () is 0.001~0.05 with ethyl acetate, Trifluoroacetic Acid Ethyl Ester in mass ratio:2~ 5:1,5~10h is reacted at 40~60 DEG C, rectifying, cooling obtain condensation product, then add formic acid in the condensation product for obtaining With the mixed solution of ethyl acetate, at 30~55 DEG C, 0.5~3h is reacted, cool down, filter, filtrate decompression rectifying obtains three Acetyl fluoride ethyl acetate.
2. the method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate according to claim 1, it is characterised in that described divalence The total mole number of slaine and trivalent metal salt is 0.4~0.5 with the ratio of the total mole number of NaOH and sodium carbonate:.1.
3. the method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate according to claim 1, it is characterised in that described hydrogen-oxygen It is 4~10 with the mass ratio of sodium carbonate to change NaOH in sodium and sodium carbonate mixture:1.
4. the method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate according to claim 1, it is characterised in that described KF with The ratio of the total mole number of divalent metal salt and trivalent metal salt is 1:10~25.
5. the method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate according to claim 1, it is characterised in that described formic acid It is 0.5~1.5 with the mixed solution of ethyl acetate and the mass ratio of Trifluoroacetic Acid Ethyl Ester:1.
6. the method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate according to claim 1, it is characterised in that described formic acid Mass ratio with formic acid in the mixed solution of ethyl acetate and ethyl acetate is 1:0.3~3.
CN201510209805.1A 2015-04-29 2015-04-29 A kind of method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate Active CN104829455B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510209805.1A CN104829455B (en) 2015-04-29 2015-04-29 A kind of method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510209805.1A CN104829455B (en) 2015-04-29 2015-04-29 A kind of method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate

Publications (2)

Publication Number Publication Date
CN104829455A CN104829455A (en) 2015-08-12
CN104829455B true CN104829455B (en) 2017-03-08

Family

ID=53807703

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510209805.1A Active CN104829455B (en) 2015-04-29 2015-04-29 A kind of method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate

Country Status (1)

Country Link
CN (1) CN104829455B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105727923B (en) * 2015-12-30 2018-07-10 衢州学院 A kind of catalyst for synthesizing HFC-125 and preparation method thereof
CN116284139B (en) * 2023-02-28 2023-11-07 江苏福基新材料研究院有限公司 Method for synthesizing pentaerythritol diphosphite dioctadecyl ester

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2583415B1 (en) * 1985-06-14 1987-08-14 Rhone Poulenc Spec Chim PROCESS FOR THE PREPARATION OF ETHYL TRIFLUOROACETOACETATE.
US20120283493A1 (en) * 2009-06-05 2012-11-08 Olson Edwin S Multiproduct biorefinery for synthesis of fuel components and chemicals from lignocellulosics via levulinate condensations
CN102633644A (en) * 2012-04-06 2012-08-15 华远医药研究院有限公司 Synthesis process of trifluoroacetyl ethyl acetate

Also Published As

Publication number Publication date
CN104829455A (en) 2015-08-12

Similar Documents

Publication Publication Date Title
EP2697192B1 (en) Method for preparation of alkoxy-amine hydrochloride
CN104447312B (en) A kind of method of Synthesis of dimethyl carbonate
CN113800485B (en) Preparation method of lithium bis (fluorosulfonyl) imide
CN104829455B (en) A kind of method for catalyzing and synthesizing trifluoroacetic ethyl acetoacetate
CN105001085A (en) Method for synthesizing ethyl 4,4-difluoroacetoacetate in catalyzed mode through layered materials
CN109400497A (en) A kind of process for cleanly preparing of methyl hydrazine
CN105503544A (en) Method for catalytically synthesizing propylene glycol methyl ether by adopting solid base catalyst KF/ZrO2-SiO2
CN103130657A (en) Synthetic method of 2-chloro-4-aminophenol
CN103396318B (en) Synthetic process for 2,4-dinitroanisole
CN103012074A (en) Method for preparing aromatic methyl ether compound
CN104058936B (en) A kind of method of separating-purifying paracresol
CN106588657B (en) Method for synthesizing dimethyl carbonate
CN103497157B (en) 2-imidazolidone synthesis method
CN108976108A (en) A method of synthesis pseudo ionone
CN101265236B (en) Synthesis technique for toltrazuril
CN109748800A (en) A kind of preparation method of pair of nitrobenzyl alcohol
CN103483577A (en) Preparation method of glycidyl terminated allyl alcohol polyoxyethylene ether
CN103709039B (en) Method for synthesizing methyl (ethyl) gallate through catalysis of Cu-mordenite
CN107001250B (en) A method of Ao Dangka is prepared for intermediate
CN101671296A (en) New method for obtaining 2-chloro-3-methylpyridine from mixture of 2-chloro-5-methylpyridine and 2-chloro-3-methylpyridine
CN114369044A (en) Preparation method of p-aminophenyl-beta-hydroxyethyl sulfone and p-aminophenyl-beta-hydroxyethyl sulfone sulfate
CN106187691B (en) A method of recycling hexafluoroisopropanol from the gaseous mixture containing hexafluoroisopropanol and hydrogen
CN104262160B (en) A kind of preparation method of 2-nitro-2-methyl isophthalic acid-propyl alcohol
CN106957235B (en) A kind of preparation method of tamoxifen
CN106831493A (en) The synthetic method of tetrabutyl urea

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
EXSB Decision made by sipo to initiate substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant