CN110128258A - The synthetic method of sitagliptin intermediate 2,4,5- trifluoro benzene acetic acid - Google Patents

The synthetic method of sitagliptin intermediate 2,4,5- trifluoro benzene acetic acid Download PDF

Info

Publication number
CN110128258A
CN110128258A CN201910331211.6A CN201910331211A CN110128258A CN 110128258 A CN110128258 A CN 110128258A CN 201910331211 A CN201910331211 A CN 201910331211A CN 110128258 A CN110128258 A CN 110128258A
Authority
CN
China
Prior art keywords
trifluoro
benzene
reaction
methylene chloride
acetic acid
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.)
Granted
Application number
CN201910331211.6A
Other languages
Chinese (zh)
Other versions
CN110128258B (en
Inventor
谭回
李维平
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.)
Shenzhen Second Peoples Hospital
Original Assignee
Shenzhen Second Peoples Hospital
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 Shenzhen Second Peoples Hospital filed Critical Shenzhen Second Peoples Hospital
Priority to CN201910331211.6A priority Critical patent/CN110128258B/en
Publication of CN110128258A publication Critical patent/CN110128258A/en
Application granted granted Critical
Publication of CN110128258B publication Critical patent/CN110128258B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/26Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton
    • C07C17/263Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton by condensation reactions
    • C07C17/269Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton by condensation reactions of only halogenated hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C253/00Preparation of carboxylic acid nitriles
    • C07C253/14Preparation of carboxylic acid nitriles by reaction of cyanides with halogen-containing compounds with replacement of halogen atoms by cyano groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/08Preparation of carboxylic acids or their salts, halides or anhydrides from nitriles

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a kind of synthetic method of 2,4,5- trifluoro benzene acetic acid of sitagliptin intermediate, 1,2,4- trifluoro-benzene is reacted to obtain 2,4,5- trifluoro benzene acetic acids with methylene chloride, cyanide under the effect of the catalyst.Operation of the present invention is simple, after the completion of chloromethylation, can directly carry out cyanalation reaction without post-processing;Reaction yield is higher, and cost is relatively low;By-product is less, and three waste discharge is less.

Description

The synthetic method of sitagliptin intermediate 2,4,5- trifluoro benzene acetic acid
Technical field
The invention belongs to pharmaceutical fields, and in particular to a kind of synthesis side of 2,4,5- trifluoro benzene acetic acid of sitagliptin intermediate Method.
Background technique
Sitagliptin is developed by United States Merck company, and in 2006 through Food and Drug Adminstration of the US (FDA) newly-developed hypoglycemic agent of the treatment type II diabetes of approval.Sitagliptin is as a kind of dipeptidyl peptidase-IV (DPP- IV) inhibitor, different from traditional hypoglycemic medicine, it is the effect by inhibiting DPP-IV degradation duodenin (Incretin) To generate hypoglycemic effect, new therapeutic strategy has been opened up for treatment type II diabetes.Sitagliptin energy concentration dependent The advantages that ground plays hypoglycemic effect and is provided simultaneously with good safety, validity and tolerance, and side effect is light.
The synthetic method of sitagliptin is mainly that starting material is synthesized with 2,4,5- trifluoro benzene acetic acids, technique road Line has several following:
Route 1
Route 2
Route 3
2,4,5- trifluoro benzene acetic acid is the important intermediate for synthesizing sitagliptin.Current 2,4,5- trifluoro-benzene reported in the literature The synthetic method of acetic acid mainly has four routes: 1. making using 1,2,4- trifluoro-benzene as raw material by chloromethylation, cyaniding, hydrolysis , more 2. 2,4, the 5- trifluorobromobenzenes of the route three wastes under alkaline condition, through transition metal-catalyzed, occur with diester malonate Coupling reaction, then hydrolysis obtains 2,4,5- trifluoro benzene acetic acids, and this method atom economy type is poor, and catalyst usage amount is more, It is unsuitable for industrialized production.After 3. Grignard Reagent is made in 2,4,5- trifluorobromobenzenes, coupling reaction is carried out with allyl bromide, bromoallylene, it is then double Key aoxidizes to obtain 2,4,5- trifluoro benzene acetic acids, and oxidant used in the method is that ruthenium and sodium metaperiodate composite oxidant, price are more expensive.④ 2,4,5- trifluoro benzyl chlorides are obtained by 1,2,4- trifluoro-benzene chloromethylation, it is anti-with carbon dioxide again then to form corresponding Grignard Reagent 2,4,5- trifluoro benzene acetic acids should be obtained, which still remains the more disadvantage of the chloromethylation three wastes.
Summary of the invention
To overcome disadvantages mentioned above, the present invention provides a kind of synthesis side of 2,4,5- trifluoro benzene acetic acid of sitagliptin intermediate Method, this method step is simple, and yield is high, and cost is relatively low, and three waste discharge is less.
To achieve the above object, the present invention adopts the following technical scheme:
The synthetic method of 2,4,5- trifluoro benzene acetic acid of sitagliptin intermediate, which is characterized in that 1,2,4- trifluoro-benzene exists React to obtain 2,4,5- trifluoro benzene acetic acids, the reaction process with methylene chloride, cyanide under the action of catalyst are as follows:
1) cyanide, alkali, activating agent A1 and deionized water are mixed, obtains mixture M 1;
2) in the case where protecting gas shielded, catalysts and solvents S is mixed, control reaction temperature is 100~120 DEG C, reaction pressure Power is 3~5 atmospheric pressure, after stirring 30~50min, starts 1,2,4- trifluoro-benzene of dropwise addition and methylene chloride, and drop finishes, control reaction Temperature is 130~150 DEG C, and reaction pressure is 4~8 atmospheric pressure, reacts 1~2h, obtains mixture M 2, and control reaction temperature is 50~70 DEG C, reaction pressure is 3~4 atmospheric pressure, and mixture M 1 is added dropwise, and drop finishes, and control reaction temperature is 70~80 DEG C, reaction Pressure is 5~7 atmospheric pressure, and the reaction was continued, and 3~5h terminates, and cools down and obtains mixture M 3 after being down to room temperature;
3) mixture M 3 is filtered to remove insoluble matter, be layered, after washing, desiccant dryness, concentration is evaporated off molten organic phase Agent obtains liquid L;
4) liquid L, activating agent A2 and acid-mixed is even, control reaction temperature is 80~110 DEG C, and reaction pressure is 3~5 Atmospheric pressure, 1~1.5h of reaction terminate, pour into trash ice after system is cooled down, and 2,4,5- trifluoro benzene acetic acid of white solid is precipitated.
The catalyst the preparation method comprises the following steps: by zeolite, zinc chloride be added aqueous hydrochloric acid solution in, impregnate 2~3h, then use Rotary Evaporators concentration is evaporated, and obtained solid activates 5~7h in 160~200 DEG C of bakings and obtains;The zeolite is HY-25, HY- 50 or HY-98 type;The mass ratio of the zinc chloride, zeolite and aqueous hydrochloric acid solution is 1:(3~5): (8~15);The hydrochloric acid The concentration of aqueous solution is mass fraction 5%.
The cyanide is Cymag or potassium cyanide;The alkali is sodium hydroxide or potassium hydroxide;The activating agent A1 is odium stearate;The activating agent A2 is tetrabutylammonium chloride;The protection gas is nitrogen or argon gas;The solvent S is Nitrobenzene;The acid is the hydrochloric acid of mass fraction concentration 20%;The desiccant is anhydrous sodium sulfate or anhydrous magnesium sulfate.
Described 1, the dropwise addition mode of 2,4- trifluoro-benzenes and methylene chloride are as follows: methylene chloride is first added dropwise, the drop to methylene chloride When dosage reaches itself 5%, start 1,2,4- trifluoro-benzene of dropwise addition;The 1,2,4- trifluoro-benzene and methylene chloride drop rate phase Deng.
The molar ratio of the 1,2,4- trifluoro-benzene and methylene chloride is 1:(1~1.05);Described is the 1,2,4- trifluoro The molar ratio of benzene and cyanide is 1:(1~1.08);The mass ratio of the 1,2,4- trifluoro-benzene and catalyst be 1:(0.15~ 0.22);The amount ratio of the 1,2,4- trifluoro-benzene and solvent S are 1g:(3~5.5) mL;The cyanide, alkali, activating agent A1 and The molar ratio of deionized water is 1:(0.12~0.2): (0.05~0.08): (10~15);The liquid L's and activating agent A2 Mass ratio is 1:(0.08~0.11);The mass ratio of the liquid L and acid is 1:(5~7).
Reaction principle of the present invention is shown below:
The present invention loads to zinc chloride on zeolite by processing, required catalyst is made, the catalyst is in the reaction Play the role of similar " Friedel-Crafts reaction " catalyst, chloromethylation is occurred into for 1,2,4- trifluoro-benzene and methylene chloride and obtains chlorine Methylate 1.Control the addition sequence and mode of two kinds of compounds of 1,2,4- trifluoro-benzene and methylene chloride, it is possible to reduce secondary anti- Answer: being first added methylene chloride, and during entire be added dropwise, the moment keeps methylene chloride slightly excessive, can to avoid because of 1,2, 4- trifluoro-benzene is excessive, and chloromethylation products 1 is caused to continue that the further pair for replacing chlorine atom occurs with 1,2,4- trifluoro-benzenes Reaction;Meanwhile control drop rate is equal, and it is anti-can to continue generation chloromethylation with methylene chloride to avoid chloromethylation products 1 Answer (although reaction odds in system is very low).
Mixture M 2 is obtained after completing chloromethylation, mixture M 1 is added, carries out cyanalation reaction: in alkali, activity Under the effects of agent, CN-Nucleophilic substitution occurs with the chlorine atom of chloromethylation products 1, generates cyanalation product 2.The present invention Corresponding reaction condition is taken, can quickly and efficiently be carried out cyanalation under the premise of being not required to chloromethylation products 1 to be separated Reaction.
Cyanalation product 2 is obtaining target product by hydrolysis: hydrolysis can be made more efficient using activating agent.
Compared with the existing technology, advantages of the present invention has:
1, operation is simple, after the completion of chloromethylation, can directly carry out cyanalation reaction without post-processing;
2, reaction yield is higher, and cost is relatively low;
3, by-product is less, and three waste discharge is less.
Specific embodiment
Combined with specific embodiments below, the present invention is further illustrated.
Embodiment 1
The synthetic method of 2,4,5- trifluoro benzene acetic acids, comprising the following steps:
1) Cymag, sodium hydroxide, odium stearate and deionized water are mixed, obtains mixture M 1, Cymag, hydroxide The molar ratio of sodium, odium stearate and deionized water is 1:0.16:0.07:13.
2) under protection of argon gas, catalyst and nitrobenzene are mixed, control reaction temperature is 115 DEG C, reaction pressure 4.5 A atmospheric pressure is first added dropwise methylene chloride, when the dripping quantity of methylene chloride reaches itself 5%, starts to drip after stirring 45min Add 1,2,4- trifluoro-benzenes, and keeps 1,2,4- trifluoro-benzenes and methylene chloride Drop volumes rate equal.
After completion of dropwise addition, control reaction temperature is 142 DEG C, and reaction pressure is 7 atmospheric pressure, reacts 1.5h, is mixed Object M2 is closed, control reaction temperature is 6 DEG C, and reaction pressure is 3~4 atmospheric pressure, and mixture M 1 is added dropwise, and drop finishes, control reaction temperature Degree is 76 DEG C, and reaction pressure is 6 atmospheric pressure, and the reaction was continued, and 4.5h terminates, and cools down and obtains mixture M 3 after being down to room temperature.
In the step, the molar ratio of 1,2,4- trifluoro-benzene and methylene chloride is 1:1.02,1,2,4- trifluoro-benzene and nitrobenzene Amount ratio be 1g:4.5mL, the molar ratio of 1,2,4- trifluoro-benzene and Cymag is 1:1.06,1,2,4- trifluoro-benzene and catalyst Mass ratio be 1:0.18.
The step used catalyst the preparation method comprises the following steps: by HY-98 type zeolite, zinc chloride be added mass fraction 5% salt In aqueous acid, 3h is impregnated, is then evaporated with Rotary Evaporators concentration, obtained solid is obtained in 200 DEG C of baking activation 7h, chlorination The mass ratio of zinc, zeolite and aqueous hydrochloric acid solution is 1:4:13.
3) mixture M 3 is filtered to remove insoluble matter, be layered, organic phase after washing, anhydrous sodium sulfate are dry, steam by concentration Except solvent obtains liquid L.
4) hydrochloric acid of liquid L, tetrabutylammonium chloride and mass fraction concentration 20% mix, and control reaction temperature is 108 DEG C, reaction pressure is 4 atmospheric pressure, and reaction 80min terminates, pours into trash ice after system is cooled down, white solid 2,4 is precipitated, 5- trifluoro benzene acetic acid.In the step, the mass ratio of liquid L and tetrabutylammonium chloride is 1:0.1;The mass ratio of liquid L and hydrochloric acid For 1:6.5.
Molar yield 99.2%, GC purity 98.7%.
Embodiment 2
The synthetic method of 2,4,5- trifluoro benzene acetic acids, comprising the following steps:
1) potassium cyanide, potassium hydroxide, odium stearate and deionized water are mixed, obtains mixture M 1, potassium cyanide, hydroxide The molar ratio of potassium, odium stearate and deionized water is 1:0.12:0.05:10.
2) under nitrogen protection, catalyst and nitrobenzene are mixed, control reaction temperature is 100 DEG C, and reaction pressure is 3 Atmospheric pressure is first added dropwise methylene chloride, when the dripping quantity of methylene chloride reaches itself 5%, starts to be added dropwise after stirring 30min 1,2,4- trifluoro-benzene, and keep 1,2,4- trifluoro-benzenes and methylene chloride Drop volumes rate equal.
After completion of dropwise addition, control reaction temperature is 130 DEG C, and reaction pressure is 4 atmospheric pressure, reacts 1h, obtains mixture M2, control reaction temperature are 50 DEG C, and reaction pressure is 3 atmospheric pressure, and mixture M 1 is added dropwise, and drop finishes, and control reaction temperature is 70 DEG C, reaction pressure is 5 atmospheric pressure, and the reaction was continued, and 3~5h terminates, and cools down and obtains mixture M 3 after being down to room temperature.
In the step, the molar ratio of 1,2,4- trifluoro-benzene and methylene chloride is 1:1, the use of 1,2,4- trifluoro-benzene and nitrobenzene For amount than being 1g:3mL, the molar ratio of 1,2,4- trifluoro-benzene and potassium cyanide is 1:1, and the mass ratio of 1,2,4- trifluoro-benzene and catalyst is 1:0.15。
The step used catalyst the preparation method comprises the following steps: by HY-25 type zeolite, zinc chloride be added mass fraction 5% salt In aqueous acid, 2h is impregnated, is then evaporated with Rotary Evaporators concentration, obtained solid is obtained in 160 DEG C of baking activation 5h, chlorination The mass ratio of zinc, zeolite and aqueous hydrochloric acid solution is 1:3:8.
3) mixture M 3 is filtered to remove insoluble matter, be layered, organic phase after washing, anhydrous magnesium sulfate are dry, steam by concentration Except solvent obtains liquid L.
4) hydrochloric acid of liquid L, tetrabutylammonium chloride and mass fraction concentration 20% mix, and control reaction temperature is 80 DEG C, Reaction pressure is 3 atmospheric pressure, and reaction 1h terminates, pours into trash ice after system is cooled down, and 2,4,5- trifluoro of white solid is precipitated Phenylacetic acid.In the step, the mass ratio of liquid L and activating agent A2 are 1:0.08;The mass ratio of liquid L and hydrochloric acid is 1:5.
Molar yield 98.2%, GC purity 98.1%.
Embodiment 3
The synthetic method of 2,4,5- trifluoro benzene acetic acids, comprising the following steps:
1) Cymag, sodium hydroxide, odium stearate and deionized water are mixed, obtains mixture M 1, Cymag, hydroxide The molar ratio of sodium, odium stearate and deionized water is 1:0.2:0.08:15.
2) under protection of argon gas, catalyst and nitrobenzene are mixed, control reaction temperature is 120 DEG C, and reaction pressure is 5 Atmospheric pressure is first added dropwise methylene chloride, when the dripping quantity of methylene chloride reaches itself 5%, starts to be added dropwise after stirring 50min 1,2,4- trifluoro-benzene, and keep 1,2,4- trifluoro-benzenes and methylene chloride Drop volumes rate equal.
After completion of dropwise addition, control reaction temperature is 150 DEG C, and reaction pressure is 8 atmospheric pressure, reacts 2h, obtains mixture M2, control reaction temperature are 70 DEG C, and reaction pressure is 4 atmospheric pressure, and mixture M 1 is added dropwise, and drop finishes, and control reaction temperature is 80 DEG C, reaction pressure is 7 atmospheric pressure, and the reaction was continued, and 5h terminates, and cools down and obtains mixture M 3 after being down to room temperature.
In the step, the molar ratio of 1,2,4- trifluoro-benzene and methylene chloride is 1:1.05,1,2,4- trifluoro-benzene and nitrobenzene Amount ratio be 1g:5.5mL, the molar ratio of 1,2,4- trifluoro-benzene and Cymag is 1:1.08,1,2,4- trifluoro-benzene and catalyst Mass ratio be 1:0.22.
The step used catalyst the preparation method comprises the following steps: by HY-50 type zeolite, zinc chloride be added mass fraction 5% salt In aqueous acid, 3h is impregnated, is then evaporated with Rotary Evaporators concentration, obtained solid is obtained in 180 DEG C of baking activation 6h, chlorination The mass ratio of zinc, zeolite and aqueous hydrochloric acid solution is 1:5:15.
3) mixture M 3 is filtered to remove insoluble matter, be layered, organic phase after washing, anhydrous sodium sulfate are dry, steam by concentration Except solvent obtains liquid L.
4) hydrochloric acid of liquid L, tetrabutylammonium chloride and mass fraction concentration 20% mix, and control reaction temperature is 110 DEG C, reaction pressure is 5 atmospheric pressure, and reaction 1.5h terminates, pours into trash ice after system is cooled down, and white solid 2,4,5- is precipitated Trifluoro benzene acetic acid.In the step, the mass ratio of liquid L and activating agent A2 are 1:0.11;The mass ratio of liquid L and hydrochloric acid is 1:7.
Molar yield 98.7%, GC purity 98.5%.
Embodiment 4
System is added in 1,2,4- trifluoro-benzene in advance, then is starting that other reaction conditions of methylene chloride and material use are added dropwise Than same embodiment 1, molar yield 35.3%, GC purity 55.2%.
Embodiment 5
Tetrabutylammonium chloride is not added, other reaction conditions and material are with than same embodiment 1, and molar yield 75.5%, GC is pure Degree 80.3%.
Embodiment 6
Catalyst is not added, target product is not detected with than same embodiment 1 in other reaction conditions and material.
Embodiment 7
Reaction pressure before starting 1,2,4- trifluoro-benzene of dropwise addition is set as 2 atmospheric pressure, and reaction temperature is set as 80 DEG C, other Reaction condition and material are with than same embodiment 1, molar yield 55.2%, GC purity 72.2%.
Embodiment 8
Reaction pressure before starting 1,2,4- trifluoro-benzene of dropwise addition is set as 7 atmospheric pressure, and reaction temperature is set as 150 DEG C, His reaction condition and material are with than same embodiment 1, molar yield 61.3%, GC purity 69.2%.
Embodiment 9
Reaction pressure after 1,2,4- trifluoro-benzenes and methylene chloride will be added dropwise is set as 2 atmospheric pressure, and reaction temperature is set as 110 DEG C, other reaction conditions and material are with than same embodiment 1, molar yield 65.3%, GC purity 77.1%.
Embodiment 10
Reaction pressure after 1,2,4- trifluoro-benzenes and methylene chloride will be added dropwise is set as 12 atmospheric pressure, and reaction temperature is set as 180 DEG C, other reaction conditions and material are with than same embodiment 1, molar yield 72.1%, GC purity 82.1%.
The identification of 11 product structure of embodiment
By taking 1 product of embodiment as an example, structural analysis data are as follows.
1) fusing point
123~124 DEG C, 121~125 DEG C of literature value
2) mass spectrum
Molecular ion peak 190.
3) nucleus magnetic hydrogen spectrum is analyzed
1H-NMR (DMSO): δ 11.5 (1H), δ 6.82 (1H), δ 6.58 (1H), δ 3.72 (1H).Various hydrogen are in product structure On ownership such as following formula:
Nmr analysis, product structure meet object, i.e., 2,4,5- trifluoro benzene acetic acids.

Claims (5)

1. the synthetic method of 2,4,5- trifluoro benzene acetic acid of sitagliptin intermediate, which is characterized in that urging 1,2,4- trifluoro-benzene React to obtain 2,4,5- trifluoro benzene acetic acids, the reaction process with methylene chloride, cyanide under the action of agent are as follows:
1) cyanide, alkali, activating agent A1 and deionized water are mixed, obtains mixture M 1;
2) in the case where protecting gas shielded, catalysts and solvents S is mixed, control reaction temperature is 100~120 DEG C, reaction pressure 3 ~5 atmospheric pressure after stirring 30~50min, start 1,2,4- trifluoro-benzene of dropwise addition and methylene chloride, and drop finishes, and controls reaction temperature It is 130~150 DEG C, reaction pressure is 4~8 atmospheric pressure, reacts 1~2h, obtains mixture M 2, control reaction temperature is 50~ 70 DEG C, reaction pressure is 3~4 atmospheric pressure, and mixture M 1 is added dropwise, and drop finishes, and control reaction temperature is 70~80 DEG C, reaction pressure For 5~7 atmospheric pressure, the reaction was continued, and 3~5h terminates, and cools down and obtains mixture M 3 after being down to room temperature;
3) mixture M 3 is filtered to remove insoluble matter, be layered, after washing, desiccant dryness, concentration is evaporated off solvent and obtains organic phase Liquid L;
4) liquid L, activating agent A2 and acid-mixed is even, control reaction temperature is 80~110 DEG C, and reaction pressure is 3~5 atmosphere Pressure, 1~1.5h of reaction terminate, pour into trash ice after system is cooled down, and 2,4,5- trifluoro benzene acetic acid of white solid is precipitated.
2. the synthetic method of 2,4,5- trifluoro benzene acetic acid of sitagliptin intermediate as described in claim 1, which is characterized in that institute State catalyst the preparation method comprises the following steps: zeolite, zinc chloride are added in aqueous hydrochloric acid solution, are impregnated 2~3h, are then used Rotary Evaporators Concentration is evaporated, and obtained solid activates 5~7h in 160~200 DEG C of bakings and obtains;The zeolite is HY-25, HY-50 or HY-98 Type;The mass ratio of the zinc chloride, zeolite and aqueous hydrochloric acid solution is 1:(3~5): (8~15);The concentration of the aqueous hydrochloric acid solution For mass fraction 5%.
3. the synthetic method of 2,4,5- trifluoro benzene acetic acid of sitagliptin intermediate as described in claim 1, which is characterized in that institute Stating cyanide is Cymag or potassium cyanide;The alkali is sodium hydroxide or potassium hydroxide;The activating agent A1 is stearic acid Sodium;The activating agent A2 is tetrabutylammonium chloride;The protection gas is nitrogen or argon gas;The solvent S is nitrobenzene;It is described Acid is the hydrochloric acid of mass fraction concentration 20%;The desiccant is anhydrous sodium sulfate or anhydrous magnesium sulfate.
4. the synthetic method of 2,4,5- trifluoro benzene acetic acid of sitagliptin intermediate as described in claim 1, which is characterized in that institute State the dropwise addition mode of 1,2,4- trifluoro-benzenes and methylene chloride are as follows: methylene chloride is first added dropwise, the dripping quantity to methylene chloride reaches certainly Body 5% when, start 1,2,4- trifluoro-benzene of dropwise addition;The 1,2,4- trifluoro-benzene and methylene chloride drop rate are equal.
5. the synthetic method of 2,4,5- trifluoro benzene acetic acid of sitagliptin intermediate as described in claim 1, which is characterized in that institute The molar ratio for stating 1,2,4- trifluoro-benzene and methylene chloride is 1:(1~1.05);Described is the 1,2,4- trifluoro-benzene and cyanide Molar ratio be 1:(1~1.08);The mass ratio of the 1,2,4- trifluoro-benzene and catalyst is 1:(0.15~0.22);Described 1, The amount ratio of 2,4- trifluoro-benzene and solvent S are 1g:(3~5.5) mL;The cyanide, alkali, activating agent A1 and deionized water are rubbed You are than being 1:(0.12~0.2): (0.05~0.08): (10~15);The mass ratio of the liquid L and activating agent A2 is 1: (0.08~0.11);The mass ratio of the liquid L and acid is 1:(5~7).
CN201910331211.6A 2019-04-24 2019-04-24 Synthetic method of sitagliptin intermediate 2,4, 5-trifluorophenylacetic acid Expired - Fee Related CN110128258B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910331211.6A CN110128258B (en) 2019-04-24 2019-04-24 Synthetic method of sitagliptin intermediate 2,4, 5-trifluorophenylacetic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910331211.6A CN110128258B (en) 2019-04-24 2019-04-24 Synthetic method of sitagliptin intermediate 2,4, 5-trifluorophenylacetic acid

Publications (2)

Publication Number Publication Date
CN110128258A true CN110128258A (en) 2019-08-16
CN110128258B CN110128258B (en) 2022-04-01

Family

ID=67571132

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910331211.6A Expired - Fee Related CN110128258B (en) 2019-04-24 2019-04-24 Synthetic method of sitagliptin intermediate 2,4, 5-trifluorophenylacetic acid

Country Status (1)

Country Link
CN (1) CN110128258B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111393282A (en) * 2020-05-21 2020-07-10 湖南复瑞生物医药技术有限责任公司 Preparation method of 2,4, 5-trifluorophenylacetic acid
WO2022099439A1 (en) * 2020-11-10 2022-05-19 杭州臻挚生物科技有限公司 Preparation method for 2,4,5-trifluorophenylacetic acid

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040077901A1 (en) * 2002-10-08 2004-04-22 Norihiro Ikemoto Process for the synthesis of trifluorophenylacetic acids
CN1749232A (en) * 2005-09-29 2006-03-22 上海康鹏化学有限公司 Process for preparing 2,4,5-triflorophenylacetic acid
CN101092345A (en) * 2007-04-04 2007-12-26 浙江永太化学有限公司 Method for preparing 2,4,5 trifluorobenzene acetic acid
CN101659611A (en) * 2009-09-28 2010-03-03 浙江永太科技股份有限公司 Method for preparing 2, 4, 5-trifluoro-phenylacetic-acid
CN102690166A (en) * 2012-06-12 2012-09-26 南通施美康药物化学有限公司 Preparation methods of 2, 4, 5-trifluoro-benzyl chloride and 2, 4, 5-trifluoro-phenylacetic acid
CN106748716A (en) * 2016-11-14 2017-05-31 江苏汉阔生物有限公司 A kind of new method for preparing 2,4,5 trifluoro benzene acetic acids

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040077901A1 (en) * 2002-10-08 2004-04-22 Norihiro Ikemoto Process for the synthesis of trifluorophenylacetic acids
CN1749232A (en) * 2005-09-29 2006-03-22 上海康鹏化学有限公司 Process for preparing 2,4,5-triflorophenylacetic acid
CN101092345A (en) * 2007-04-04 2007-12-26 浙江永太化学有限公司 Method for preparing 2,4,5 trifluorobenzene acetic acid
CN101659611A (en) * 2009-09-28 2010-03-03 浙江永太科技股份有限公司 Method for preparing 2, 4, 5-trifluoro-phenylacetic-acid
CN102690166A (en) * 2012-06-12 2012-09-26 南通施美康药物化学有限公司 Preparation methods of 2, 4, 5-trifluoro-benzyl chloride and 2, 4, 5-trifluoro-phenylacetic acid
CN106748716A (en) * 2016-11-14 2017-05-31 江苏汉阔生物有限公司 A kind of new method for preparing 2,4,5 trifluoro benzene acetic acids

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111393282A (en) * 2020-05-21 2020-07-10 湖南复瑞生物医药技术有限责任公司 Preparation method of 2,4, 5-trifluorophenylacetic acid
WO2022099439A1 (en) * 2020-11-10 2022-05-19 杭州臻挚生物科技有限公司 Preparation method for 2,4,5-trifluorophenylacetic acid

Also Published As

Publication number Publication date
CN110128258B (en) 2022-04-01

Similar Documents

Publication Publication Date Title
CN105669398B (en) Produce the device and method of benzaldehyde
CN110128258A (en) The synthetic method of sitagliptin intermediate 2,4,5- trifluoro benzene acetic acid
CN102516122B (en) Environment friendly method for preparing DMF (Dimethyl Formamide) solution of 2-hydroxy-benzonitril
CN101891621A (en) Compounding method for 3- ethyoxyl-4-ethoxycarbonyl phenylacetic acid
CN108358760B (en) Application of metalate/palladium compound catalytic reduction system in debenzylation reaction and deuteration reaction
CN106892808A (en) A kind of preparation method of 2,4 dichlorphenoxyacetic acids
CN101659611B (en) Method for preparing 2, 4, 5-trifluoro-phenylacetic-acid
CN103396318B (en) Synthetic process for 2,4-dinitroanisole
CN109970580B (en) Extraction and preparation method of R-3-aminobutanol
CN1942422B (en) Method for producing hydrate of fluoroalkyl ketone
CN105130869B (en) A kind of synthetic method of the ketone of Entresto intermediates (S) 5 (carbonyl of biphenyl 4) pyrrolidines 2
CN102417486B (en) Method for synthesizing valsartan
CN107827742A (en) A kind of CO2The method that direct carboxylation method prepares aromatic acid
CN114835605B (en) Synthesis method of diphenyl ketone hydrazone
CN101575348A (en) Method for synthesizing beta-sodium glycero-phosphate
CN101941905B (en) Method for producing ester of 2, 4-dichlorphenoxyacetic acid
CN105237340B (en) Novel synthesis method for 4,4,4-trifluorobutanol
CN101362752A (en) Synthesis method of lamivudine intermediate
CN112174798B (en) Synthesis method of Sakuba/valsartan sodium LCZ696
CN102924362A (en) Preparation method of hexahydro-2-cyclopentyl-pyrryl amine hydrochloride
CN102838482B (en) Preparation method of 3,6-dichlorosalicylic acid
CN106966940B (en) A kind of preparation method of Sitagliptin phosphate intermediate N arylmethyl -2S- cyano methyl acridine
CN106588584A (en) Dehydration method for ether solvent
CN104557512B (en) A kind of 3-(bromo phenyl)-2, the preparation method of 2 '-difluoro propionic acid
CN103772151A (en) Preparation method of 2-methyl-3-phenyl benzyl alcohol

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20220401

CF01 Termination of patent right due to non-payment of annual fee