CN115611717A - Preparation method of polyfluorobenzaldehyde - Google Patents

Preparation method of polyfluorobenzaldehyde Download PDF

Info

Publication number
CN115611717A
CN115611717A CN202211357870.5A CN202211357870A CN115611717A CN 115611717 A CN115611717 A CN 115611717A CN 202211357870 A CN202211357870 A CN 202211357870A CN 115611717 A CN115611717 A CN 115611717A
Authority
CN
China
Prior art keywords
dichlorofluorobenzene
substituted
formula
reaction
chloride
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
CN202211357870.5A
Other languages
Chinese (zh)
Other versions
CN115611717B (en
Inventor
杨建华
袁云龙
何立
顾竞
李晓亮
赵姗姗
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.)
Shanghai Wanshou Pharmaceutical Co ltd
Original Assignee
Shanghai Wanshou Pharmaceutical Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shanghai Wanshou Pharmaceutical Co ltd filed Critical Shanghai Wanshou Pharmaceutical Co ltd
Priority to CN202211357870.5A priority Critical patent/CN115611717B/en
Publication of CN115611717A publication Critical patent/CN115611717A/en
Application granted granted Critical
Publication of CN115611717B publication Critical patent/CN115611717B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/61Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
    • C07C45/63Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by introduction of halogen; by substitution of halogen atoms by other halogen atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/093Preparation of halogenated hydrocarbons by replacement by halogens
    • C07C17/10Preparation of halogenated hydrocarbons by replacement by halogens of hydrogen atoms
    • C07C17/14Preparation of halogenated hydrocarbons by replacement by halogens of hydrogen atoms in the side-chain of aromatic compounds
    • 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
    • C07C17/32Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton by introduction of halogenated alkyl groups into ring compounds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/42Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by hydrolysis
    • C07C45/43Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by hydrolysis of >CX2 groups, X being halogen
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C47/00Compounds having —CHO groups
    • C07C47/52Compounds having —CHO groups bound to carbon atoms of six—membered aromatic rings
    • C07C47/55Compounds having —CHO groups bound to carbon atoms of six—membered aromatic rings containing halogen

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention relates to the technical field of organic synthesis, in particular to a preparation method of polyfluorobenzaldehyde, which comprises the following steps: 1) Carrying out chloromethylation reaction on substituted dichlorofluorobenzene shown as a formula I to obtain chloromethyl substituted dichlorofluorobenzene shown as a formula II; 2) Carrying out chlorination reaction on the chloromethyl-substituted dichlorofluorobenzene provided by the step 1) shown in the formula II to obtain dichloromethyl-substituted dichlorofluorobenzene shown in the formula II'; 3) Carrying out hydrolysis reaction on dichloromethyl-substituted dichlorofluorobenzene shown in the formula II' provided by the step 2) to obtain formyl-substituted dichlorofluorobenzene shown in the formula III; 4) Carrying out fluorination reaction on the formyl group substituted dichlorofluorobenzene provided by the step 2) and shown in the formula III to obtain the polyfluorinated benzaldehyde shown in the formula IV. The method has the advantages of short reaction route, high conversion rate and universal applicability.

Description

Preparation method of polyfluorobenzaldehyde
Technical Field
The invention relates to the technical field of organic synthesis, in particular to a preparation method of polyfluorobenzaldehyde.
Background
Trifluorobenzaldehyde is an important fine chemical intermediate and can be used for synthesizing various medical liquid crystal materials. For example, 2,4,5-trifluorobenzaldehyde can be used for synthesizing hypotensor sitagliptin, 2,4,6-trifluorobenzaldehyde can be used for synthesizing medicines Bicteravir developed by Gilidide corporation for treating HIV, 2,3,4-trifluorobenzaldehyde can be used for synthesizing various 2,3,4-trifluorodiphenylacetylene liquid crystal compounds, and can also be used for synthesizing quinolone antibacterial medicines such as widely used sarcin antibiotics like ofloxacin, lomefloxacin, norfloxacin and the like. The prior art has the defects of long reaction route, low conversion rate and the like in the preparation of the trifluorobenzaldehyde.
Disclosure of Invention
In view of the above-mentioned disadvantages of the prior art, the present invention aims to provide a method for preparing polyfluorobenzaldehyde, which is used for solving the problems in the prior art.
In order to achieve the above objects and other related objects, one aspect of the present invention provides a method for preparing polyfluorobenzaldehyde represented by formula IV, comprising the steps of:
1) Performing chloromethylation reaction on the substituted dichlorofluorobenzene shown in the formula I to obtain chloromethyl substituted dichlorofluorobenzene shown in the formula II,
Figure BDA0003920906810000011
wherein R is 1 、R 2 、R 3 One of which is fluorine and the remainder hydrogen;
2) Carrying out chlorination reaction on the dichlorofluorobenzene substituted by chloromethyl shown in the formula II provided in the step 1) to obtain dichloromethyl-substituted dichlorofluorobenzene shown in a formula II';
Figure BDA0003920906810000021
3) Carrying out hydrolysis reaction on dichloromethyl-substituted dichlorofluorobenzene shown in the formula II' provided by the step 2) to obtain formyl-substituted dichlorofluorobenzene shown in a formula III;
Figure BDA0003920906810000022
4) Carrying out fluorination reaction on the dichloro fluorobenzene substituted by the formyl group shown in the formula III provided by the step 3) to obtain polyfluorinated benzaldehyde shown in the formula IV;
Figure BDA0003920906810000023
on the other hand, the invention provides polyfluorobenzaldehyde shown as a formula IV, which is prepared by the preparation method.
Compared with the prior art, the invention has the following beneficial effects:
the invention provides a brand-new preparation method of polyfluorobenzaldehyde, which adopts easily-purchased chemical raw materials, adopts a short reaction route, and has the advantages of good reaction positioning property, safe, simple and easy reaction, less three wastes, high conversion rate and universal applicability by a series of green, environment-friendly and safe reaction processes.
Detailed Description
The inventor of the invention provides a preparation method of polyfluorobenzaldehyde shown as a formula IV through a large amount of researches, and the polyfluorobenzaldehyde is prepared through chloromethylation reaction, hydrolysis reaction and fluorination reaction.
Figure BDA0003920906810000031
Wherein R is 1 、R 2 、R 3 One of which is fluorine and the remainder hydrogen.
The invention provides a preparation method of polyfluorobenzaldehyde shown as a formula IV in a first aspect, which comprises the following steps:
1) Performing chloromethylation reaction on the substituted dichlorofluorobenzene shown in the formula I to obtain chloromethyl substituted dichlorofluorobenzene shown in the formula II,
Figure BDA0003920906810000032
wherein R is 1 、R 2 、R 3 One of which is fluorine and the remainder hydrogen;
2) The dichlorofluorobenzene substituted by chloromethyl shown in the formula II provided in the step 1) is further subjected to chlorination reaction to obtain dichloromethyl substituted dichlorofluorobenzene shown in a formula II',
Figure BDA0003920906810000033
3) Carrying out hydrolysis reaction on dichloromethyl-substituted dichlorofluorobenzene provided by the step 2) to obtain formyl-substituted dichlorofluorobenzene shown in a formula III;
Figure BDA0003920906810000034
4) Carrying out fluorination reaction on the dichloro fluorobenzene substituted by the formyl group shown in the formula III provided by the step 3) to obtain polyfluorinated benzaldehyde shown in the formula IV;
Figure BDA0003920906810000041
in one embodiment of the present invention, when R 1 Is fluorine, R 2 、R 3 When hydrogen is present, the substituted dichlorofluorobenzene represented by the formula I is
Figure BDA0003920906810000042
2,6-dichlorofluorobenzene, the chloromethyl-substituted dichlorofluorobenzene shown in the formula II is
Figure BDA0003920906810000043
2,6-dichloro-3-chloromethylfluorobenzene (also named 2,4-dichloro-3-fluorobenzyl chloride), wherein the dichloromethyl-substituted dichlorofluorobenzene represented by the formula II' is
Figure BDA0003920906810000044
2,4-dichloro-3-fluorodichlorobenzyl (also known under the name 1,3-dichloro-4-dichloromethyl-2-fluorobenzene). The formyl-substituted dichlorofluorobenzene shown in the formula III is
Figure BDA0003920906810000045
2,6-dichloro-3-formylfluorobenzene (which may also be named 2,4-dichloro-3-fluorobenzaldehyde), wherein the polyfluorobenzaldehyde shown in the formula IV is
Figure BDA0003920906810000046
2,3,4-trifluorobenzaldehyde;
in another embodiment of the present invention, when R 2 Is fluorine, R1 2 、R 3 When hydrogen is present, the substituted dichlorofluorobenzene represented by the formula I is
Figure BDA0003920906810000047
2,4-dichlorofluorobenzene, the chloromethyl-substituted dichlorofluorobenzene shown in the formula II is
Figure BDA0003920906810000048
2,4-dichloro-5-chloromethylfluorobenzene (also named 2,4-dichloro-5-fluorobenzyl chloride), wherein the dichloromethyl-substituted dichlorofluorobenzene represented by the formula II' is
Figure BDA0003920906810000049
2,4-dichloro-5-fluorodichlorobenzyl. The formyl-substituted dichlorofluorobenzene shown in the formula III is
Figure BDA00039209068100000410
2,4-dichloro-5-formylfluorobenzene (which may also be named 2,4-dichloro-5-fluorobenzaldehyde), wherein the polyfluorobenzaldehyde shown in the formula IV is
Figure BDA0003920906810000051
2,4,5-trifluorobenzaldehyde.
In still another embodiment of the present invention, when R 3 Is fluorine, R 1 、R 2 When hydrogen is present, the substituted dichlorofluorobenzene represented by the formula I is
Figure BDA0003920906810000052
3,5-dichlorofluorobenzene, the chloromethyl-substituted dichlorofluorobenzene shown in the formula II is
Figure BDA0003920906810000053
3,5-dichloro-2-chloromethylfluorobenzene (also named 2,4-dichloro-6-fluorobenzyl chloride), wherein the dichloromethyl-substituted dichlorofluorobenzene represented by the formula II' is
Figure BDA0003920906810000054
2,4-dichloro-6-fluorodichlorobenzyl, the formyl-substituted dichlorofluorobenzene shown in the formula III is
Figure BDA0003920906810000055
3,5-dichloro-2-formylfluorobenzene (which may also be named 2,4-dichloro-6-fluorobenzaldehyde), wherein the polyfluorobenzaldehyde shown in the formula IV is
Figure BDA0003920906810000056
2,4,6-trifluorobenzaldehyde.
In the preparation method of the polyfluorobenzaldehyde shown as the formula IV, the step 1) is to perform chloromethylation reaction on substituted dichlorofluorobenzene shown as the formula I to obtain chloromethyl-substituted dichlorofluorobenzene shown as the formula II;
Figure BDA0003920906810000057
wherein R is 1 、R 2 、R 3 One of which is fluorine and the remainder hydrogen.
In step 1) of the present invention, the chloromethylation reaction is carried out in the presence of paraformaldehyde. The molecular formula of paraformaldehyde is HO- (CH) 2 O) n -H, n =10-100. In some embodiments, the molar ratio of the paraformaldehyde to the substituted dichlorofluorobenzene of formula I can be, for example, 1 to 5:1. 1-1.2: 1. 1.2-2:1. or 2 to 5:1, etc. Preferably, the molar ratio of the paraformaldehyde to the substituted dichlorofluorobenzene shown in the formula I is 1.2-2:1.
in step 1) of the present invention, the chloromethylation reaction is usually carried out at a certain temperature and for a certain time. For example, the chloromethylation reaction temperature may be, for example, 10 to 80 ℃, 10 to 20 ℃, 20 to 50 ℃, or 50 to 80 ℃. Preferably, the chloromethylation reaction temperature may be, for example, 20 to 50 ℃. The reaction time of the chloromethylation reaction is 2 to 10 hours.
In step 1) of the present invention, the chloromethylation reaction is carried out in the presence of a chlorinating agent selected from hydrogen chloride gas and/or chlorosulfonic acid, etc. In some embodiments, the molar ratio of the chlorinating agent to the substituted dichlorofluorobenzene represented by the formula I may be, for example, 0.9 to 4:1. 0.9-1.5: 1. 1.5-2.5: 1. or 2.5-4:1, etc. Further, when the chlorinating agent is selected from hydrogen chloride, the chloromethylation reaction is carried out in the presence of an acid selected from sulfuric acid.
In step 1) of the invention, the chloromethylation reaction is carried out under the condition of a catalyst, and the catalyst is selected from one or more of anhydrous zinc chloride, zinc chloride hexahydrate and tetramethylammonium chloride. The molar ratio of catalyst to substituted dichlorofluorobenzene represented by the formula I may be 0.01 to 0.1: 1. 0.01-0.02: 1. 0.02-0.05:1. or 0.05-0.1:1, etc. The molar ratio of catalyst to substituted dichlorofluorobenzene represented by the formula I is preferably 0.02 to 0.05:1.
in the preparation method of the polyfluorobenzaldehyde shown as the formula IV, the step 2) is to perform chlorination reaction on the dichlorofluorobenzene substituted by chloromethyl shown as the formula II provided by the step 1) to obtain dichloromethyl substituted dichlorofluorobenzene shown as the formula II',
Figure BDA0003920906810000061
in the step 2), the chlorination reaction is carried out in the presence of chlorine gas. The chlorination reaction can adopt a photoinitiation method, and the reaction temperature can be 30-60 ℃, 30-40 ℃, 40-50 ℃, or 50-60 ℃ and the like during the photoinitiation chlorination reaction. The chlorination reaction can also adopt a thermal initiation method, and the reaction temperature can be 70-100 ℃, 70-80 ℃, 80-90 ℃, or 90-100 ℃ and the like during the thermal initiation chlorination reaction. The chlorination reaction is carried out in the presence of a catalyst AIBN or BPO, and the dosage of the catalyst is 1 per thousand-1%, 1 per thousand-5 per thousand, 5 per thousand-1% and the like of the weight of the chloromethyl substituted dichlorofluorobenzene shown in the formula II. The chlorination reaction can be carried out in the presence of a solvent, and can be carried out in the absence of a solvent, and is selected from one or more of benzotrifluoride, p-chlorotrifluoromethane, nitrobenzene, 3,4-dichlorobenzotrifluoride, chlorobenzene, dichlorobenzene, trichlorobenzene, dichloroethane, and the like; the dosage of the solvent is 0.5 to 10 times, 0.5 to 1 time, 1 to 3 times, 3 to 5 times, 5 to 8 times, 8 to 10 times, and the like of the weight of the chloromethyl substituted dichlorofluorobenzene shown in the formula II. The content of dichloromethyl-substituted dichlorofluorobenzene shown in formula II 'is detected by GC in the chlorination reaction, and when the content of dichloromethyl-substituted dichlorofluorobenzene shown in formula II' is detected to be close to 50%, for example, the content is 45% -55%, or the content is 48% -52%, the reaction can be stopped, and the post-treatment can be carried out. The system can be cooled to room temperature, nitrogen is introduced to blow to remove the residual chlorine, then the system is distilled, and the separated chloromethyl substituted dichlorofluorobenzene shown as the formula II can be used for recycling and reusing; continuously separating and collecting dichloromethyl-substituted dichlorofluorobenzene shown in the formula II'; the residual kettle bottom materials are not used. When the content of dichloromethyl-substituted dichlorofluorobenzene shown as a formula II' is lower than 45% by GC detection in the chlorination reaction, the chlorination reaction is insufficient, and the conversion rate is low; when the content of dichloromethyl-substituted dichlorofluorobenzene shown in the formula II ' is higher than 55%, more than 3% of over-chlorinated compound II ' is generated in the reaction system, and the compound II ' causes difficulty in separation and purification of dichloromethyl-substituted dichlorofluorobenzene shown in the formula II ' and remains in the dichloromethyl-substituted dichlorofluorobenzene shown in the formula II ' to further influence the purity of subsequent products.
Figure BDA0003920906810000071
In the preparation method of the polyfluorobenzaldehyde shown as the formula IV, the step 3) is to perform hydrolysis reaction on dichloromethyl-substituted dichlorofluorobenzene shown as the formula II' provided by the step 2) to obtain formyl-substituted dichlorofluorobenzene shown as the formula III;
Figure BDA0003920906810000072
in step 3), the hydrolysis reaction is performed in the presence of a zinc reagent, wherein the zinc reagent is selected from one or more of zinc chloride, zinc acetate, and zinc acetate dihydrate. In the step 3), the molar ratio of the zinc reagent to the dichloromethyl-substituted dichlorofluorobenzene shown in the formula II' can be 0.02-1: 1. 0.02-0.03: 1. 0.03-0.08:1. 0.08-0.1: 1. 0.1-1:1, etc. Preferably, the molar ratio of the zinc reagent to the dichloromethyl-substituted dichlorofluorobenzene shown in the formula II' is 0.03-0.08:1.
in step 3), the hydrolysis is carried out in the presence of water, wherein the molar ratio of the water to dichloromethyl-substituted dichlorofluorobenzene shown as a formula II' is 0.9-2: 1. 0.9-1: 1. 1-1.5:1 or 1.5-2:1, etc. Preferably, the molar ratio of the water to the dichloromethyl-substituted dichlorofluorobenzene represented by the formula II' is 1 to 1.5:1.
in step 3), the hydrolysis reaction is carried out in the presence of formic acid, and the molar ratio of the formic acid to dichloromethyl-substituted dichlorofluorobenzene shown in II' is 3-10: 1. 3-4: 1. 4-6:1. or 6-10:1, etc. Preferably, the molar ratio of the formic acid to the dichloromethyl-substituted dichlorofluorobenzene shown in the formula II' is 4-6:1.
in step 3) of the present invention, it is usually necessary to carry out the hydrolysis reaction at a temperature of 100 to 150 ℃, 100 to 115 ℃, 115 to 135 ℃, 135 to 150 ℃ or the like. Preferably, the temperature of the hydrolysis reaction is 115-135 ℃. The reaction time may be, for example, 3 to 10 hours, 3 to 5 hours, 5 to 8 hours, 8 to 10 hours, or the like.
In step 3), the hydrolysis reaction may be performed in the presence of a phase transfer catalyst selected from one or more of tetrabutylammonium chloride, tetrabutylammonium iodide, tetrabutylammonium hydroxide, tetrabutylammonium hydrogen sulfate, tetramethylammonium chloride, tetrabutylammonium bromide, tetraethylammonium bromide, tetraphenylphosphonium bromide, 4-dimethylaminopyridine, polyethylene glycol, benzyltriethylammonium chloride, tetra-n-butylammonium fluoride, trioctylmethylammonium chloride, dodecyltrimethylammonium chloride, tetradecyltrimethylammonium chloride, and hexadecyltrimethylammonium bromide. In some embodiments, the phase transfer catalyst may be used in a molar ratio of the amount of the phase transfer catalyst to the dichloromethyl-substituted dichlorofluorobenzene represented by the formula II' of from 0.05 to 0.3:1. 0.05-0.1: 1. 0.1-0.15: 1. 0.15-0.2: 1. 0.2-0.25: 1. or 0.25 to 0.3:1, etc.
In step 3), the hydrolysis reaction is carried out under the protection of inert gas. The inert gas may be, for example, one or a combination of nitrogen, neon, argon, krypton, and the like.
In the preparation method of the polyfluorobenzaldehyde shown as the formula IV, the dichloro fluorobenzene substituted by the formyl group shown as the formula III in the step 4) is subjected to a fluorination reaction to obtain the polyfluorobenzaldehyde shown as the formula IV;
Figure BDA0003920906810000081
in the step 4), the fluorination reaction is carried out in an inert gas atmosphere; the inert gas may be, for example, one or a combination of nitrogen, neon, argon, krypton.
In the step 4), the fluorination reaction further comprises potassium fluoride; the molar ratio of the potassium fluoride to the formyl-substituted dichlorofluorobenzene represented by the formula III can be 2 to 5:1. 2-3: 1. 4-5: 1. or 4-5:1, etc.
In step 4) of the present invention, the fluorination reaction is usually carried out at a temperature of 100 to 180 ℃, 100 to 120 ℃, 120 to 150 ℃, or 150 to 180 ℃.
In step 4), the fluorination reaction further comprises a catalyst. The catalyst is selected from one or more of tetrabutylammonium chloride, tetrabutylammonium iodide, tetrabutylammonium hydroxide, tetrabutylammonium hydrogen sulfate, tetramethylammonium chloride, tetrabutylammonium bromide, tetraethylammonium bromide, tetraphenylphosphonium bromide, 4-dimethylaminopyridine, polyethylene glycol, benzyltriethylammonium chloride, tetra-n-butylammonium fluoride, trioctylmethylammonium chloride, dodecyltrimethylammonium chloride, tetradecyltrimethylammonium chloride, hexadecyltrimethylammonium bromide, crown ethers, and PEG. In some embodiments, the weight ratio of the catalyst to the formyl-substituted dichlorofluorobenzene represented by the formula III may be from 0.001 to 0.1: 1. 0.001-0.01: 1. 0.01-0.05: 1. or 0.05-0.1:1, etc.
In step 4), the invention further comprises a solvent selected from organic solvents, wherein the organic solvents are selected from one or more of 1,3-dimethyl imidazolidinone, 1,3-dimethyl-3,4,5,6-tetrahydro-2-pyrimidinone, DMAc, DMF, DMSO, NMP, sulfolane, MIBK, imidazolidinone and the like. In some embodiments, the solvent is 0.5 to 10 times, 0.5 to 3 times, 3 to 8 times, 8 to 10 times, 0.5 to 2 times, 2 to 5 times, 5 to 8 times, 8 to 10 times, or the like, the weight of the formyl-substituted dichlorofluorobenzene represented by the formula III.
The invention provides polyfluorobenzaldehyde shown in a formula IV, which is prepared by the preparation method of the polyfluorobenzaldehyde according to the first aspect of the invention.
In conclusion, the invention provides a brand-new preparation method of polyfluorobenzaldehyde, which adopts easily-purchased chemical raw materials, adopts a short reaction route, passes through a series of green, environment-friendly and safe reaction processes, and has the advantages of good reaction positioning property, safe, simple and easy reaction, less three wastes, high conversion rate and universal applicability.
The embodiments of the present invention are described below with reference to specific embodiments, and other advantages and effects of the present invention will be easily understood by those skilled in the art from the disclosure of the present specification. The invention is capable of other and different embodiments and of being practiced or of being carried out in various ways, and its several details are capable of modification in various respects, all without departing from the spirit and scope of the present invention.
It is to be understood that the processing equipment or apparatus not specifically identified in the following examples is conventional in the art.
Furthermore, it is to be understood that one or more method steps mentioned in the present invention does not exclude that other method steps may also be present before or after the combined steps or that other method steps may also be inserted between these explicitly mentioned steps, unless otherwise indicated; it is also to be understood that a combined connection between one or more devices/apparatus as referred to in the present application does not exclude that further devices/apparatus may be present before or after the combined device/apparatus or that further devices/apparatus may be interposed between two devices/apparatus explicitly referred to, unless otherwise indicated. Moreover, unless otherwise indicated, the numbering of the various method steps is merely a convenient tool for identifying the various method steps, and is not intended to limit the order in which the method steps are arranged or the scope of the invention in which the invention may be practiced, and changes or modifications in the relative relationship may be made without substantially changing the technical content.
Example 1
1) Chloromethylation reaction
Figure BDA0003920906810000091
Under nitrogen atmosphere at 20 + -3 deg.C, 10g paraformaldehyde, 100g 77% H 2 SO 4 And 5g of anhydrous ZnCl 2 Sequentially adding the mixture into a reaction bottle, stirring and adding 165g of 2, 6-dichlorofluorobenzene, and heating to 30-35 ℃. The hydrogen chloride gas was started. After 1h, the remaining 40g of paraformaldehyde and 400g 77% are added in portions 2 SO 4 . After the reaction is finished, stopping introducing hydrogen chloride gas, cooling to 20 +/-3 ℃, standing for liquid separation, washing an upper organic phase with brine, concentrating and rectifying to obtain 186.6g of GC99.92% and the yield of 87.4%.1H NMR (400MHZ, DMSO-d 6): δ 7.624-7.663= (m, 1h, ar-H), δ =7.520-7.545 (m, 1h, ar-H), δ =4.872 (s, 2h, ch) 2 )
2) Chlorination reaction
Figure BDA0003920906810000101
Mixing 2,4-dichloro-3-fluorobenzyl chloride 180g with dichloroethane 100g, adding catalyst AIBN 1g, heating and stirring to 70-80 deg.C; chlorine is slowly introduced into the saturated system, and after 16 hours of reaction, the content of 2,4-dichloro-3-fluorodichlorobenzyl is detected to be 49.6 percent. The temperature is reduced to room temperature, nitrogen purging is carried out for 30 minutes, and 105.1g of 2,4-dichloro-3-fluorodichlorobenzyl and 80g of raw material 2,4-dichloro-3-fluorobenzyl chloride are obtained by rectification. (yield in the chlorination reaction was 50.2%, and a reduced yield, that is, a yield after 80g of the starting material was recovered, was 90.5%)
1H NMR(400MHZ,DMSO-d6):δ7.765-7.782=(m,1H,Ar-H),δ=7.638-7.654(m,1H,Ar-H),δ=4.877(s,1H,CH)
Example 2
1) Chloromethylation reaction
Figure BDA0003920906810000102
12g of paraformaldehyde and 100g 77% of the total weight of the mixture at 20 + -3 ℃ under a nitrogen atmosphere 2 SO 4 And 9g of zinc chloride hexahydrate are sequentially added into a reaction bottle, 165g of 2, 4-dichlorofluorobenzene is added under stirring, and the temperature is increased to 30-35 ℃. The hydrogen chloride gas was started. Adding the remaining 48g of paraformaldehyde and 400g 77% in portions after the start of the reaction 2 SO 4 . After the reaction is finished, stopping introducing hydrogen chloride gas, cooling to 20 +/-3 ℃, standing for liquid separation, and separating an upper organic phaseAfter washing with brine, the product is concentrated and rectified to obtain 183.0g, GC98.89% and 85.7% yield.
1H NMR(400MHZ,DMSO-d6):δ=7.872-7.889(d,1H,Ar-H),δ=7.766-7.790(d,1H,Ar-H),δ=4.802(s,2H,CH 2 )。
2) Chlorination reaction
Figure BDA0003920906810000103
Adding 180g of 2,4-dichloro-5-fluorobenzyl chloride into 1g of AIBN catalyst, and heating and stirring to 40-50 ℃; ultraviolet fluorescence is started, chlorine is slowly introduced into the saturated system, and after 20 hours of reaction, the content of 2,4-dichloro-5-fluorodichlorobenzyl is detected to be 51.7 percent. Turning off the ultraviolet lamp, cooling to room temperature, purging with nitrogen for 30 minutes, and rectifying to obtain 2,4-dichloro-5-fluorodichlorobenzyl 108.9g and raw material 2,4-dichloro-5-fluorobenzyl chloride 74g. The starting material was recovered as above (yield 52.1% by chlorination reaction, 88.5% by reduced yield).
1H NMR(400MHZ,DMSO-d6):δ=7.885-7.901(d,1H,Ar-H),δ=7.787-7.808(d,1H,Ar-H),δ=4.822(s,1H,CH)
Example 3
1) Chloromethylation reaction
Figure BDA0003920906810000111
165g of 3, 5-dichlorofluorobenzene and 40g of paraformaldehyde (1.3 eq) are added into a reaction bottle, stirred and cooled to about 20 ℃, and 130g of chlorosulfonic acid (1.1 eq) is added dropwise, stirred and reacted for 2 hours at the temperature of 20-30 ℃. After the reaction is finished, the reaction solution is slowly poured into ice water under the condition of continuous stirring, the mixture is stirred and then stands for layering, the lower layer is a yellow organic phase, and distillation under reduced pressure is carried out to obtain 179.5g of distillate, the yield is 84.1%, and the GC detection content is 99.28%.
1 H NMR(DMSO-d 6 ,400MHz):δ7.509-7.613(m,2H,Ar-H),δ4.807(d,J=1.2Hz,2H,CH 2 )。
2) Chlorination reaction
Figure BDA0003920906810000112
Adding 180g of 2,4-dichloro-6-fluorobenzyl chloride into 1g of AIBN catalyst, and heating and stirring to 40-50 ℃; ultraviolet fluorescence is started, chlorine is slowly introduced into the saturated system, and after reacting for 18 hours, the content of 2,4-dichloro-6-fluorodichlorobenzyl is 51.2 percent through GC sampling detection. And (3) turning off the ultraviolet lamp, cooling to room temperature, purging with nitrogen for 30 minutes, and distilling to obtain 2,4-dichloro-6-fluorodichlorobenzyl 108.3g and raw material 2,4-dichloro-6-fluorobenzyl chloride 71g. (yield in chlorination reaction 51.8%, conversion yield 85.6%)
1H NMR(DMSO-d6,400MHz):δ7.527-7.621(m,2H,Ar-H),δ4.819(d,J=1.2Hz,1H,CH)
Example 4
And (3) hydrolysis reaction:
Figure BDA0003920906810000113
171g of 2, 4-dichloro-3-fluorodichlorobenzyl and 6g of zinc acetate are added at room temperature (20 +/-5 ℃), stirring is started, the mixture is heated to 120-130 ℃ in an oil bath, and water is slowly added dropwise while maintaining the temperature. After the reaction is finished, the temperature of the system is reduced to 25 +/-5 ℃, 30g of water is added for washing once, and the lower organic phase is washed by 10% sodium bicarbonate water solution until the pH value is about 7-8. Separating to obtain an organic phase, concentrating and purifying to obtain 120.4g of the product with the GC content of 99.96 percent and the yield of 90.4 percent.
Nuclear magnetism: 1H NMR (400MHZ, CDCl3): δ =10.392-10.395 (d, J =0.8hz,1h, cho), δ =7.685-7.709 (m, 1h, ar-H), δ =7.440-7.480 (m, 1h, ar-H).
Example 5
And (3) hydrolysis reaction:
Figure BDA0003920906810000121
171g of 2, 4-dichloro-3-fluorodichlorobenzyl and 7g of zinc acetate dihydrate are put into a four-neck flask, when the temperature is raised to be higher than 130 ℃, water is slowly dripped, the internal temperature of the four-neck flask is kept to be higher than 130 ℃, and the dripping is finished within about 30 min. After stirring for 1 hour, the temperature is reduced to 25 ℃, 100ml of dichloroethane and 100ml of water are added into the reaction solution, and the reaction solution is stirred and washed for half an hour. The organic phase of the lower layer was separated, distilled under reduced pressure, and the distillate was cooled to obtain 116.3g of a white solid, GC.
Example 6
And (3) hydrolysis reaction:
Figure BDA0003920906810000122
2,4-dichloro-5-fluoro-dichlorobenzyl (149g, 0.6mol, 1.00eq) and 3.4g anhydrous zinc chloride (0.041 eq) are put into a reaction bottle at room temperature, stirred under the protection of nitrogen, heated to 125 ℃, added with water dropwise, the temperature is controlled to 125-135 ℃, the reaction is very quick, and the reaction takes 2-3 hours to complete. The reaction can be stopped and the temperature can be reduced. A vacuum distillation device is built, and the product is distilled out, wherein the product is white crystal, the weight is 98.8g, the GC content is 99.94%, and the yield is 85.3%.
Nuclear magnetism: 1H NMR (DMSO-d 6, 400 MHz) δ 10.226-10.172 (m, 1H, CHO), δ 8.020-7.822 (m, 1H, ar-H), δ 7.794-7.651 (m, 1H, ar-H).
Example 7
And (3) hydrolysis reaction:
Figure BDA0003920906810000123
2,4-dichloro-5-fluoro-dichlorobenzyl (149g, 0.6mol, 1.00eq), 8g zinc acetate dihydrate and 100g formic acid are added, stirred, heated and reacted to 100 ℃, when the reaction temperature is less than or equal to 2 percent of raw materials, the heating is stopped, the mixture is naturally cooled to room temperature, dichloroethane is added for extraction, the dichloroethane phase is washed by water and then distilled, 101.6g of product is obtained, the GC detection shows that the yield is 99.28 percent, and the yield is 87.7 percent.
Example 8
And (3) hydrolysis reaction:
Figure BDA0003920906810000131
2,4-dichloro-6-fluoro-dichlorobenzyl (171g, 0.7mol, 1.00eq) and 3.9g anhydrous zinc chloride (0.041 eq) are put into a four-port reaction bottle, stirred and heated to 115-125 ℃ under the protection of nitrogen, the internal temperature is controlled to be more than or equal to 115 ℃, water is slowly dripped into the system, and the reaction is carried out for 5 hours. After the reaction, the temperature is reduced to room temperature, 60g of ethyl acetate is added and stirred, then the solvent and the water are distilled off, and the white crystals are obtained by continuous distillation, 112.9g of white crystals are obtained, and the yield is 83.6 percent by GC detection and 99.53 percent.
Example 9
And (3) hydrolysis reaction:
Figure BDA0003920906810000132
in a drying reaction vessel, 2,4-dichloro-6-fluoro-dichlorobenzyl (171g, 0.7mol, 1.00eq), 160g formic acid, 6g anhydrous zinc chloride and 1g tetrabutyl ammonium bromide are added under the protection of nitrogen, and the mixture is heated to 85 to 95 ℃ for reaction. After about 5 hours of reaction, the temperature is reduced to 20 to 30 ℃, dichloroethane is added for extraction at 150ml, the organic phase is separated, the organic phase is washed by water and NaHCO is used 3 The solution is washed until the pH value is neutral, an organic phase is separated, dichloroethane is removed, and the product 117.8g is obtained by distillation, the GC detection is 99.64 percent, and the yield is 87.2 percent.
1H NMR(DMSO-d 6 ,400MHz):δ10.247(s,1H,CHO),δ7.678~7.748(m,2H,Ar-H)。
Example 10
Fluorination reaction
Preparation of 2,3,4-trifluorobenzaldehyde
Figure BDA0003920906810000133
Under the protection of nitrogen, 80g of potassium fluoride, 3.5g of tetramethylammonium chloride and 500g of DMF500g are sequentially added into a reaction bottle, the stirring temperature is 150-155 ℃ for refluxing, 123g of 2,4-dichloro-3-fluorobenzaldehyde is added in batches, and the mixture is stirred, heated and refluxed for 2 hours. After the reaction is finished, the reaction product is cooled to room temperature, and after filtration, filtrate is directly distilled to obtain 2,4,5-trifluorobenzaldehyde, 91.9g of colorless transparent liquid, 99.01 percent of GC content and 90.1 percent of yield. 1 H NMR(400MHZ,CDCl3):δ=10.284(s,1H,CHO),δ=7.671-7.729(m,1H,Ar-H),δ=7.124-7.185(m,1H,Ar-H)
Example 11
Fluorination reaction
Preparation of 2,3,4-trifluorobenzaldehyde
Figure BDA0003920906810000141
Under the protection of nitrogen, 80g of potassium fluoride, 5.5g of tetrabutylammonium bromide and 600g of sulfolane are sequentially added into a reaction bottle, the temperature is raised to 150-155 ℃ by stirring, 2,4-dichloro-3-fluorobenzaldehyde 123g is added in batches, and the reaction is carried out at 150-155 ℃. After the reaction, the reaction mixture was cooled to room temperature (20 to 25 ℃), insoluble materials were removed by filtration, and the filtrate was distilled to give 2,4,5-trifluorobenzaldehyde as a colorless transparent liquid (92.3g, GC content 98.78%, yield 90.5%).
Example 12
Fluorination reaction
Preparation of 2,4,5-trifluorobenzaldehyde
Figure BDA0003920906810000142
Under the protection of nitrogen, 80g of potassium fluoride, 3g of tetramethylammonium chloride and 500g of DMF are sequentially added into a reaction bottle, stirred and heated to 150-155 ℃ for reflux, 123g of 2,4-dichloro-5-fluorobenzaldehyde is added in batches, and the mixture is stirred, heated and refluxed for 2 hours. After the reaction, the reaction mixture was cooled to room temperature, filtered, and the filtrate was distilled to obtain 2,4,5-trifluorobenzaldehyde as a colorless transparent liquid 91.6g, having a GC content of 98.90% and a yield of 89.8%.
1H NMR(DMSO-d6,400MHz):δ10.135(d,1H,CHO),δ7.912~7.845(m,1H,Ar-H),δ7.843~7.775(m,1H,Ar-H)
Example 13
Fluorination reaction
Preparation of 2,4,5-trifluorobenzaldehyde
Figure BDA0003920906810000143
Under the protection of nitrogen, 90g of potassium fluoride, 5g of tetrabutylammonium bromide and 550g of DMF are sequentially added into a reaction bottle, the stirring temperature is 150-155 ℃, reflux is carried out, 123g of 2,4-dichloro-5-fluorobenzaldehyde is added in batches, stirring and heating are carried out, and reflux is carried out for 2 hours. After the reaction is finished, the reaction product is cooled to room temperature, filtered, and the filtrate is subjected to steam distillation to obtain a mixed solution of 2,4,5-trifluorobenzaldehyde and water, 93.8g of colorless transparent liquid is obtained after layering, 92.5g of product is obtained after drying, the GC content is 99.17%, and the yield is 90.7%.
Example 14
Fluorination reaction
Preparation of 2,4,6-trifluorobenzaldehyde
Figure BDA0003920906810000151
Under the protection of nitrogen, 80g of potassium fluoride, 5.5g of tetrabutylammonium chloride and 550g of sulfolane are sequentially added into a reaction bottle, the temperature is raised to 150-155 ℃ by stirring, 123g of 2,4-dichloro-6-fluorobenzaldehyde is added in batches, the mixture is stirred and heated, and the reaction is carried out for 2 hours at the temperature of 150-155 ℃. After the reaction, the reaction mixture was cooled to room temperature, insoluble materials were removed by filtration, and the filtrate was subjected to steam distillation with water to give 2,4,6-trifluorobenzaldehyde, which was cooled to give 93.1g of a white solid with 98.73% GC content and 91.3% yield.
1H NMR(DMSO,400MHz):δ10.138(s,1H,CHO),δ7.439~7.368(m,2H,Ar-H)
Example 15
Fluorination reaction
Preparation of 2,4,6-trifluorobenzaldehyde
Figure BDA0003920906810000152
Under the protection of nitrogen, 85g of potassium fluoride, 3.5g of tetramethylammonium chloride and 600g of DMF are sequentially added into a reaction bottle, stirred and refluxed, 123g of 2,4-dichloro-6-fluorobenzaldehyde is added in batches, stirred and heated, and refluxed for 2 hours. After the reaction, the reaction mixture was cooled to room temperature (about 25 ℃), filtered, and the filtrate was subjected to steam distillation with water, and the distillate was cooled to give 2,4,6-trifluorobenzaldehyde 94.0g, having a GC content of 99.31% and a yield of 92.2%.
In conclusion, the present invention effectively overcomes various disadvantages of the prior art and has high industrial utilization value.
The foregoing embodiments are merely illustrative of the principles and utilities of the present invention and are not intended to limit the invention. Any person skilled in the art can modify or change the above-mentioned embodiments without departing from the spirit and scope of the present invention. Accordingly, it is intended that all equivalent modifications or changes which may be made by those skilled in the art without departing from the spirit and scope of the present invention as defined in the appended claims.

Claims (10)

1. A preparation method of polyfluorobenzaldehyde shown as a formula IV comprises the following steps:
1) Carrying out chloromethylation reaction on substituted dichlorofluorobenzene shown in a formula I to obtain chloromethyl substituted dichlorofluorobenzene shown in a formula II;
Figure FDA0003920906800000011
wherein R is 1 、R 2 、R 3 One of which is fluorine and the remainder hydrogen;
2) Carrying out chlorination reaction on the chloromethyl-substituted dichlorofluorobenzene provided by the step 1) shown in the formula II to obtain dichloromethyl-substituted dichlorofluorobenzene shown in the formula II';
Figure FDA0003920906800000012
3) Carrying out hydrolysis reaction on dichloromethyl-substituted dichlorofluorobenzene shown in the formula II' provided by the step 2) to obtain formyl-substituted dichlorofluorobenzene shown in the formula III;
Figure FDA0003920906800000013
4) Carrying out fluorination reaction on the dichloro fluorobenzene substituted by the formyl group shown in the formula III provided by the step 3) to obtain polyfluorinated benzaldehyde shown in the formula IV;
Figure FDA0003920906800000014
2. the method of claim 1, wherein in step 1), the chloromethylation reaction is carried out in the presence of paraformaldehyde in a molar ratio of 1 to 5 of substituted dichlorofluorobenzene of formula I: 1;
and/or, in the step 1), the temperature of the chloromethylation reaction is 10-80 ℃;
and/or, in step 1), the chloromethylation reaction is carried out in the presence of a chlorinating agent selected from hydrogen chloride gas and/or chlorosulfonic acid.
3. The method of claim 2, wherein in step 1), the molar ratio of paraformaldehyde to substituted dichlorofluorobenzene having a formula I is 1.2 to 2:1;
and/or, in the step 1), the temperature of the chloromethylation reaction is 20-50 ℃;
and/or, in the step 1), the molar ratio of the dosage of the chlorinating reagent to the substituted dichlorofluorobenzene shown in the formula I is 0.9-4:1.
4. the process of claim 3, wherein in step 1), when the chlorinating agent is selected from the group consisting of hydrogen chloride, the chloromethylation reaction is carried out in the presence of an acid selected from the group consisting of sulfuric acid;
and/or, in the step 1), the chloromethylation reaction is carried out under the condition of a catalyst, and the catalyst is selected from one or more of anhydrous zinc chloride, zinc chloride hexahydrate and tetramethylammonium chloride.
5. The method of claim 1, wherein in step 2), the chlorination reaction is carried out in the presence of chlorine gas;
and/or the chlorination reaction is a photo-initiated chlorination reaction and/or a thermal-initiated chlorination reaction; preferably, the temperature of the photoinitiated chlorination reaction is 30-60 ℃; the reaction temperature of the thermal initiation chlorination reaction is 70-100 ℃;
and/or, the chlorination reaction further comprises a catalyst selected from AIBN or BPO; preferably, the amount of the catalyst is 1 per mill-1% of the weight of the chloromethyl substituted dichlorofluorobenzene shown in the formula II;
and/or, the chlorination reaction is carried out under the condition of solvent or no solvent; when the chlorination reaction includes a solvent, the solvent is selected from one or more of trifluorotoluene, p-chlorotrifluoromethane, nitrobenzene, 3,4-dichlorotrifluorotoluene, chlorobenzene, dichlorobenzene, trichlorobenzene, dichloroethane; preferably, the amount of the solvent is 0.5-10 times of the weight of the chloromethyl substituted dichlorofluorobenzene shown in the formula II;
and/or stopping the reaction when the content of dichloromethyl-substituted dichlorofluorobenzene shown as the formula II' is detected to be 45-55% in the chlorination reaction.
6. The method of claim 1, wherein in step 3), the hydrolysis reaction is carried out in the presence of a zinc reagent selected from the group consisting of zinc chloride, zinc acetate, and a combination of one or more of zinc acetate dihydrate;
and/or, in step 3), the hydrolysis reaction is carried out in the presence of water;
and/or, in step 3), the hydrolysis reaction is carried out in the presence of formic acid.
7. The method according to claim 6, wherein in step 3), the molar ratio of the zinc reagent to the dichloromethyl-substituted dichlorofluorobenzene represented by the formula II' is 0.02 to 1:1;
and/or, in the step 3), the molar ratio of the water to the dichloromethyl-substituted dichlorofluorobenzene shown as the formula II' is 0.9-2:1;
and/or, in the step 3), the molar ratio of the formic acid to the dichloromethyl-substituted dichlorofluorobenzene shown in the II' is 3-10:1;
and/or, in the step 3), the temperature of the hydrolysis reaction is 100-150 ℃;
and/or, in step 3), the hydrolysis reaction may be carried out in the presence of a phase transfer catalyst selected from one or more of tetrabutylammonium chloride, tetrabutylammonium iodide, tetrabutylammonium hydroxide, tetrabutylammonium hydrogen sulfate, tetramethylammonium chloride, tetrabutylammonium bromide, tetraethylammonium bromide, tetraphenylphosphonium bromide, 4-dimethylaminopyridine, polyethylene glycol, benzyltriethylammonium chloride, tetra-n-butylammonium fluoride, trioctylmethylammonium chloride, dodecyltrimethylammonium chloride, tetradecyltrimethylammonium chloride, hexadecyltrimethylammonium bromide;
and/or, in the step 3), the hydrolysis reaction is carried out under the protection of inert gas.
8. The method according to claim 7, wherein in step 3), the molar ratio of the zinc reagent to the dichloromethyl-substituted dichlorofluorobenzene represented by II' is from 0.03 to 0.08:1;
and/or, in the step 3), the molar ratio of the water to the dichloromethyl-substituted dichlorofluorobenzene shown in the II' is 1-1.5:1;
and/or, in the step 3), the molar ratio of the formic acid to the dichloromethyl-substituted dichlorofluorobenzene shown in the II' is 4-6:1;
and/or, in the step 3), the temperature of the hydrolysis reaction is 115-135 ℃;
and/or, in the step 3), the molar ratio of the dosage of the phase transfer catalyst to the dichloromethyl-substituted dichlorofluorobenzene shown in the II' is 0.05-0.3:1.
9. the method of claim 1, wherein in step 4), the fluorination reaction is carried out under an inert gas atmosphere; preferably, the inert gas is selected from one or more of nitrogen, neon, argon and krypton;
and/or, in the step 4), potassium fluoride is also included in the fluorination reaction; the molar ratio of the potassium fluoride to the formyl-substituted dichlorofluorobenzene shown in the formula III is 2-5:1;
and/or, in the step 4), the temperature of the fluorination reaction is 100-180 ℃;
and/or, in the step 4), a catalyst is also included in the fluorination reaction; the catalyst is selected from one or more of tetrabutylammonium chloride, tetrabutylammonium iodide, tetrabutylammonium hydroxide, tetrabutylammonium hydrogen sulfate, tetramethylammonium chloride, tetrabutylammonium bromide, tetraethylammonium bromide, tetraphenylphosphonium bromide, 4-dimethylaminopyridine, polyethylene glycol, benzyltriethylammonium chloride, tetra-n-butylammonium fluoride, trioctylmethylammonium chloride, dodecyltrimethylammonium chloride, tetradecyltrimethylammonium chloride, hexadecyltrimethylammonium bromide, crown ethers, and PEG; preferably, the weight ratio of the catalyst to the formyl-substituted dichlorofluorobenzene shown in the formula III is 0.001 to 0.1:1;
and/or, in the step 4), a solvent is further included, wherein the solvent is selected from organic solvents, and the organic solvents are selected from one or more of 1,3-dimethyl imidazolidinone, 1,3-dimethyl-3,4,5,6-tetrahydro-2-pyrimidinone, DMAc, DMF, DMSO, NMP, sulfolane, MIBK and imidazolidinone; preferably, the solvent is 0.5 to 10 times of the weight of the formyl-substituted dichlorofluorobenzene shown in the formula III.
10. The method of any one of claims 1 to 9, wherein when R is 1 Is fluorine, R 2 、R 3 When the fluorine is hydrogen, the substituted dichlorofluorobenzene shown in the formula I is 2,6-dichlorofluorobenzene, the chloromethyl-substituted dichlorofluorobenzene shown in the formula II is 2,6-dichloro-3-chloromethyl fluorobenzene, the dichloromethyl-substituted dichlorofluorobenzene shown in the formula II' is 2,4-dichloro-3-fluorodichlorobenzyl, the formyl-substituted dichlorofluorobenzene shown in the formula III is 2,6-dichloro-3-formylfluorobenzene, and the polyfluorobenzaldehyde shown in the formula IV is 2,3,4-trifluorobenzaldehyde;
and/or when R 2 Is fluorine, R1 2 、R 3 When the fluorine is hydrogen, the substituted dichlorofluorobenzene shown in the formula I is 2,4-dichlorofluorobenzene, the chloromethyl-substituted dichlorofluorobenzene shown in the formula II is 2,4-dichloro-5-chloromethyl fluorobenzene, the dichloromethyl-substituted dichlorofluorobenzene shown in the formula II' is 2,4-dichloro-5-fluorodichlorobenzyl, the formyl-substituted dichlorofluorobenzene shown in the formula III is 2,4-dichloro-5-formylfluorobenzene, and the polyfluorobenzaldehyde shown in the formula IV is 2,4,5-trifluorobenzaldehyde;
and/or when R 3 Is fluorine, R 1 、R 2 When the fluorine is hydrogen, the substituted dichlorofluorobenzene shown as the formula I is 3,5-dichlorofluorobenzene, the chloromethyl substituted dichlorofluorobenzene shown as the formula II is 3,5-dichloro-2-chloromethyl fluorobenzene, and the formulaThe dichloromethyl-substituted dichlorofluorobenzene shown in II' is 2,4-dichloro-6-fluorodichlorobenzyl, the formyl-substituted dichlorofluorobenzene shown in the formula III is 3,5-dichloro-2-formylfluorobenzene, and the polyfluorobenzaldehyde shown in the formula IV is 2,4,6-trifluorobenzaldehyde.
CN202211357870.5A 2022-11-01 2022-11-01 Preparation method of polyfluorobenzaldehyde Active CN115611717B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202211357870.5A CN115611717B (en) 2022-11-01 2022-11-01 Preparation method of polyfluorobenzaldehyde

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202211357870.5A CN115611717B (en) 2022-11-01 2022-11-01 Preparation method of polyfluorobenzaldehyde

Publications (2)

Publication Number Publication Date
CN115611717A true CN115611717A (en) 2023-01-17
CN115611717B CN115611717B (en) 2024-06-28

Family

ID=84876708

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202211357870.5A Active CN115611717B (en) 2022-11-01 2022-11-01 Preparation method of polyfluorobenzaldehyde

Country Status (1)

Country Link
CN (1) CN115611717B (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85101737A (en) * 1984-06-04 1987-01-31 拜尔股份公司 Preparation 2,4,5-trihalogenated benzene and 2,3,4, the derivative method of 5-tetrahalogeno-benzene
CN1212674A (en) * 1996-03-07 1999-03-31 德国赫彻斯特研究技术两合公司 Process for producing fluorinated aromatics and fluorinated nitrogen-containing hetero-aromatics

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85101737A (en) * 1984-06-04 1987-01-31 拜尔股份公司 Preparation 2,4,5-trihalogenated benzene and 2,3,4, the derivative method of 5-tetrahalogeno-benzene
CN1212674A (en) * 1996-03-07 1999-03-31 德国赫彻斯特研究技术两合公司 Process for producing fluorinated aromatics and fluorinated nitrogen-containing hetero-aromatics

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
王军等: "苯甲醛的制备", 化学世界, no. 4, pages 201 - 203 *
王毅等: "氯化苄制备苯甲醛的研究", 精细化工中间体, vol. 35, no. 1, pages 45 - 49 *
陈宗化等: "2, 4- 二氯苯甲醛合成", 现代农药, vol. 4, no. 4, pages 12 - 19 *

Also Published As

Publication number Publication date
CN115611717B (en) 2024-06-28

Similar Documents

Publication Publication Date Title
ZA200505574B (en) Method for the production of benzophenones
CN115745766B (en) Preparation method of trifluorobenzaldehyde and trifluorobenzyl bromide
CN102898422B (en) Method for preparing difenoconazole
CN115611717A (en) Preparation method of polyfluorobenzaldehyde
CN112390748B (en) Preparation method of 2-cyano-3-fluoro-5-trifluoromethylpyridine
JPH09124558A (en) Preparation of dialkyl succinyl succinate
CN112939782B (en) Preparation method of fluorine-containing aryl compound
CN108689821B (en) Method for regenerating chloranil by oxidizing hydrogen peroxide
EP1246796B1 (en) Process for the preparation of diphenyl ether compounds
CN107417489B (en) Method for synthesizing bromo-fused ring aromatic compound
CN118359560B (en) Preparation method of methylene blue
CN1185191C (en) Process for preparing alicyclic ketones and alkyl-substituted alicyclic esters
CN111533701B (en) Synthetic method of pyridine quinazoline intermediate
CN110950809B (en) Synthetic post-treatment method of aryl triazolinone compound
JP4139448B2 (en) Method for producing α-bromo, ω-chloroalkane
CN117800808A (en) Preparation method of 2, 4-dichloro fluorobenzene
CN111646972B (en) Preparation method of selective estrogen receptor degradation agent and intermediate thereof
CN109265352B (en) Preparation method of aryl cyclopropyl ether and derivatives thereof
JP5000031B2 (en) Method for producing aromatic-o-dialdehyde compound
CN113968775A (en) Intermediate compound for preparing 4-chloro-2-trifluoromethyl-acetophenone, preparation method and application thereof
CN109721551B (en) Preparation method of 3, 4-dihydro-7-methoxy-4-oxoquinazolin-6-ol acetate
JPH08119939A (en) Production of highly pure ether type bismaleimide
US20090312584A1 (en) Process For Preparing High Purity TNT
JPH01160935A (en) Production of 4-biphenyl p-tolyl ether
CN117088797A (en) Synthesis method of 2-bromo-1- (4-methylsulfonyl) acetophenone

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