CN117623897A - Preparation method of o-trifluoromethyl benzoic acid - Google Patents

Preparation method of o-trifluoromethyl benzoic acid Download PDF

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CN117623897A
CN117623897A CN202311505931.2A CN202311505931A CN117623897A CN 117623897 A CN117623897 A CN 117623897A CN 202311505931 A CN202311505931 A CN 202311505931A CN 117623897 A CN117623897 A CN 117623897A
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compound
formula
sulfuric acid
preparation
concentration
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Inventor
谢四维
牛文耀
李俊奇
潘强彪
虞佳凯
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Wei Zhejiang Huaxin Materials Ltd By Share Ltd
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Wei Zhejiang Huaxin Materials Ltd By Share Ltd
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Abstract

The invention discloses a preparation method of o-trifluoromethyl benzoic acid. The invention provides a preparation method of a compound shown in a formula I, which comprises the following steps: (1) Hydrolyzing a compound of formula III in the presence of sulfuric acid in the absence of an organic solvent; (2) And (3) reacting the reaction liquid obtained in the step (1) with sodium nitrite to obtain the compound shown in the formula I. The preparation method provided by the invention provides a novel method for synthesizing o-trifluoromethyl benzoic acid, and has high yield and purity and convenient operation; meanwhile, no organic solvent is needed, and the method is more in line with green chemistry.

Description

Preparation method of o-trifluoromethyl benzoic acid
Technical Field
The invention belongs to the field of organic synthesis, and provides a novel method for preparing o-trifluoromethyl benzoic acid.
Background
O-trifluoromethyl benzoic acid is an important intermediate or raw material in the field of fine chemical engineering, and as the raw material, o-trifluoromethyl benzoic acid is used as a key intermediate for synthesizing broad-spectrum bactericides fluopyram and cyflumetofen, and along with the wide use of the bactericides, the demand of the o-trifluoromethyl benzoic acid is also increasing. In the patents CN114436810a and CN103274929a, a preparation method of o-trifluoro benzoic acid is mentioned, and a common preparation method is that o-trifluoro methyl toluene is used as a raw material, and is subjected to substitution reaction with chlorine gas, then hydrolyzed into o-trifluoro methyl benzaldehyde, and then oxidized into o-trifluoro methyl benzoic acid. Two routes for oxidizing o-trifluoromethyl benzaldehyde into o-trifluoro-benzoic acid have industrial value; in addition, o-fluorobenzotrifluoride is also widely applied to the fields of medicine, pesticide, chemical industry and the like.
Route one: oxidizing o-trifluoromethyl benzaldehyde into o-trifluoromethyl benzoic acid by hydrogen peroxide
Route two: the raw material is o-trifluoromethyl benzaldehyde as the same as the first route, and TEMPO is used as an oxidant
Route three: o-trifluoromethyl dichlorobenzyl is taken as a raw material, and is hydrolyzed in nitric acid solution to obtain o-trifluoromethyl benzaldehyde, and then in-situ oxidation is carried out to obtain o-trifluoromethyl benzoic acid
O-trifluoromethyl benzoic acid with molecular formula of C 8 H 5 F 3 O 2 The relative molecular weight is 190.1, the melting point is 110-112 ℃, the boiling point is 248 ℃, and the powder is white solid.
Disclosure of Invention
In the prior art, o-trifluoromethyl benzonitrile is not used for synthesizing o-trifluoromethyl benzoamide and o-trifluoromethyl benzoic acid. Because of the effect of trifluoromethyl, the two raw materials are difficult to directly hydrolyze to synthesize the target product o-trifluoromethyl benzoic acid. The preparation method provided by the invention provides a novel method for synthesizing o-trifluoromethyl benzoic acid, and has high yield and purity and convenient operation; meanwhile, no organic solvent is needed, and the method is more in line with green chemistry.
The invention provides a preparation method of a compound shown in a formula I, which comprises the following steps:
(1) Hydrolyzing a compound of formula III in the presence of sulfuric acid in the absence of an organic solvent;
(2) The reaction liquid obtained in the step (1) reacts in the presence of sodium nitrite to obtain the compound shown in the formula I,
the concentration of the sulfuric acid is 75-90%;
the reaction temperature in the step (1) is 100-150 ℃;
the reaction temperature in the step (2) is 80-140 ℃.
In one embodiment, the concentration of sulfuric acid is 80 to 85%, preferably 80%.
In one embodiment, the sodium nitrite is an aqueous solution of sodium nitrite having a concentration of 5 to 45%, preferably 20 to 30%, for example 20%.
In one embodiment, the molar ratio of the compound of formula III to sodium sulfite is 1 (1-2), preferably 1 (1.1-1.6), e.g., 1:1.1, 1:1.2, 1:1.3, 1:1.4, 1:1.5 or 1:1.6.
In one embodiment, the sulfuric acid is added in an amount of 2 to 10ml/kg, preferably 4 to 6ml/kg, for example 5ml/kg, relative to the compound of formula III.
In one embodiment, the reaction time in step (1) is 1 to 8 hours, preferably 3 hours.
In one embodiment, the reaction time in step (2) is 2 to 10 hours, preferably 5 to 6 hours.
In one embodiment, the reaction temperature in step (1) is 140 to 150 ℃, preferably 140 ℃.
In one embodiment, the reaction temperature in step (2) is 120 to 140 ℃, preferably 120 ℃.
In one embodiment, the preparation method comprises the following steps:
(1) In the absence of an organic solvent, hydrolyzing the compound of formula III in the presence of 80% sulfuric acid at 140 ℃;
(2) The reaction liquid obtained in the step (1) reacts with 20% sodium nitrite to obtain the compound shown in the formula I, and the reaction temperature is 120 ℃.
In one embodiment, the preparation method further comprises the following steps: stirring, cooling, and suction filtering to obtain the compound of formula I.
The invention also provides a preparation method of the compound shown in the formula II, which comprises the following steps: hydrolyzing the compound of the formula III in the presence of sulfuric acid under the condition of no organic solvent to obtain the compound of the formula II,
the concentration of the sulfuric acid is 75-90%;
the temperature of the hydrolysis is 100-150 ℃.
In one embodiment, the concentration of sulfuric acid is 80 to 85%, preferably 80%.
In one embodiment, the molar ratio of the compound of formula III to sodium sulfite is 1 (1-2), preferably 1 (1.1-1.6), e.g., 1:1.1, 1:1.2, 1:1.3, 1:1.4, 1:1.5 or 1:1.6.
In one embodiment, the amount of sulfuric acid added is 2-10ml/kg, preferably 4-6ml/kg, for example 5ml/kg, relative to the compound of formula III.
In one embodiment, the hydrolysis time is 1 to 8 hours, preferably 3 hours.
In one embodiment, the hydrolysis temperature is 140 to 150 ℃, preferably 140 ℃.
In one embodiment, the preparation method comprises the following steps: in the absence of organic solvents, the compounds of formula III are hydrolysed in the presence of 80% sulfuric acid at a temperature of 140 ℃.
The invention also provides a preparation method of the compound shown in the formula I, which comprises the following steps: (1) Hydrolyzing the compound of the formula III in the presence of sulfuric acid in the absence of an organic solvent to obtain a compound of the formula II,
the concentration of the sulfuric acid is 75-90%;
the temperature of the hydrolysis is 100-150 ℃;
(2) Hydrolyzing the compound of the formula II in the presence of acid and sodium nitrite to obtain a compound of the formula I,
the acid is sulfuric acid or hydrochloric acid;
the concentration of sulfuric acid is 20-80% when the acid is sulfuric acid;
when the acid is hydrochloric acid, the concentration of the hydrochloric acid is 30-35%.
In one embodiment, in step (2), the acid is sulfuric acid or hydrochloric acid; when the acid is sulfuric acid, the concentration of the acid is 20-80%; the concentration of the acid is 30-35% when the acid is hydrochloric acid.
In one embodiment, in step (2), the acid is sulfuric acid, preferably 20 to 80% sulfuric acid, more preferably 30 to 50% sulfuric acid, for example 40% sulfuric acid.
In a certain scheme, in the step (2), the sodium nitrite is an aqueous solution of sodium nitrite, and the concentration of the aqueous solution of sodium nitrite is 5-45%, preferably 20-30%.
In one embodiment, in step (2), the molar ratio of the compound of formula II to sodium sulfite is 1 (1-2), preferably 1 (1.1-1.6), e.g. 1:1.1, 1:1.2, 1:1.3, 1:1.4, 1:1.5 or 1:1.6.
In one embodiment, in step (2), the acid is added in an amount of 2 to 10ml/kg, preferably 2 to 5ml/kg, more preferably 3 to 4ml/kg, relative to the compound of formula II.
In one embodiment, in step (2), the hydrolysis is carried out at a temperature of 80 to 140 ℃, preferably 100 to 130 ℃, for example 120 ℃.
In one embodiment, in the step (2), the time for the hydrolysis is 2 to 10 hours, preferably 5 to 6 hours.
In a certain scheme, in the step (2), the preparation method further comprises the following steps: stirring, cooling, and suction filtering to obtain the compound of formula I.
In a certain scheme, in the step (2), the preparation method comprises the following steps: the compound of formula II is hydrolyzed in the presence of 40% sulfuric acid and 20% aqueous sodium nitrite to give the compound of formula I at a temperature of 120 ℃.
In one embodiment, in the step (1), the concentration of the sulfuric acid is 80 to 85%, preferably 80%.
In one embodiment, in step (1), the molar ratio of the compound of formula III to sodium sulfite is 1 (1-2), preferably 1 (1.1-1.6), e.g. 1:1.1, 1:1.2, 1:1.3, 1:1.4, 1:1.5 or 1:1.6.
In one embodiment, in step (1), the amount of sulfuric acid added is 2 to 10ml/kg, preferably 4 to 6ml/kg, for example 5ml/kg, relative to the compound of formula III.
In one embodiment, in step (1), the hydrolysis time is 1 to 8 hours, preferably 3 hours.
In one embodiment, in step (1), the hydrolysis temperature is 140 to 150 ℃, preferably 140 ℃.
In one embodiment, in step (1), the preparation method comprises the following steps: in the absence of organic solvents, the compounds of formula III are hydrolysed in the presence of 80% sulfuric acid at a temperature of 140 ℃.
The above preferred conditions can be arbitrarily combined on the basis of not deviating from the common knowledge in the art, and thus, each preferred embodiment of the present invention can be obtained.
The reagents and materials used in the present invention are commercially available.
The invention has the positive progress effects that: the preparation method provided by the invention provides a novel method for synthesizing o-trifluoromethyl benzoic acid, and has high yield and purity and convenient operation; meanwhile, no organic solvent is needed, and the method is more in line with green chemistry.
Detailed Description
The invention is further illustrated by means of the following examples, which are not intended to limit the scope of the invention. The experimental methods, in which specific conditions are not noted in the following examples, were selected according to conventional methods and conditions, or according to the commercial specifications.
Purity (content) analysis method:
GC analysis parameters:
example 1
The reaction equation is:
experimental feed table:
experimental operation:
preparing an experiment, namely preparing an 80% sulfuric acid solution, placing the solution into a flask, adding raw materials according to a feeding ratio, heating to 140 ℃, reacting for 3 hours, performing central control, wherein after the raw materials react, the content of an intermediate o-trifluoromethyl benzamide is 97%, preparing a 20% sodium nitrite aqueous solution, cooling to room temperature, dropwise adding the sodium nitrite solution, after the dropwise adding, performing heat preservation, performing central control (120-140 ℃ for heat preservation) for 5 hours, and performing stirring, cooling and suction filtration to obtain 92g of a product with the purity: 99% (GC), yield 82%.
1 H NMR(400MHz,DMSO-d6)8.19(d,J=7.8Hz,1H),8.13(s,1H),7.96(d,J=7.7Hz,1H),7.72(t,J=7.8Hz,1H)
Example 2
The reaction equation is:
experimental feed table:
experimental operation:
preparing an experiment, namely preparing an 80% sulfuric acid solution, placing the solution into a flask, adding raw materials according to a feeding ratio, heating to 140 ℃, reacting for 3 hours, performing central control, wherein after the raw materials are reacted, the content of an intermediate o-trifluoromethyl benzamide is 96.4%, preparing a 20% sodium nitrite aqueous solution, cooling to 120 ℃, dropwise adding the sodium nitrite solution, performing heat preservation, performing central control to 5 hours, stirring, cooling and suction filtering to obtain a product with the purity of 90 g: 96.4% (GC), yield 81%.
Example 3
The reaction equation is:
experimental feed table:
experimental operation:
preparing an experiment, preparing 80% sulfuric acid solution, placing the solution into a flask, adding raw materials according to a feeding ratio, heating to 140 ℃, reacting for 3 hours, performing central control, after the raw materials react, preparing 20% sodium nitrite aqueous solution with the content of the intermediate o-trifluoromethyl benzamide of 97.3%, cooling to 120 ℃, dropwise adding sodium nitrite solution, after dropwise adding, performing heat preservation, performing central control to 5 hours, performing product content of 98.2%, stirring, cooling, and performing suction filtration to obtain 84g of a product with the purity: 97.3% (GC) yield 75%.
Example 4
The reaction equation is:
experimental feed table:
experimental operation:
preparing an experiment, preparing an 80% sulfuric acid solution, placing the solution into a flask, adding raw materials according to a feeding ratio, heating to 140 ℃, reacting for 3 hours, performing central control, and performing post treatment after the raw materials are reacted to obtain the intermediate o-trifluoromethyl benzamide with the content of 97.2%.105.2g, purity: 97.2% (GC) yield 95.1%.
1H NMR(600MHz,DMSO-d6)δ7.92(s,1H),7.73(d,J=7.8Hz,1H),7.67(t,J=7.5Hz,1H),7.59(dd,J=13.9,5.9Hz,2H),7.51(d,J=7.6Hz,1H).
Example 5
The reaction equation is:
experimental feed table:
experimental operation:
preparing an experiment, preparing a 40% sulfuric acid solution, placing the solution into a flask, adding the raw materials prepared in the example 4 according to a feeding ratio, heating to 120 ℃, preparing a 20% sodium nitrite aqueous solution, dropwise adding the sodium nitrite solution, after the dropwise adding, keeping the temperature for controlling to 6 hours, stirring and cooling the solution until the product content is 98%, and performing suction filtration to obtain 132g of a product with the purity: 98% (GC), yield 87%.
Example 6
The reaction equation is:
experimental feed table:
experimental operation:
preparing an experiment, preparing a 40% sulfuric acid solution, placing the solution into a flask, adding the raw materials prepared in the example 4 at room temperature according to a feeding ratio, preparing a 20% sodium nitrite aqueous solution, dropwise adding the sodium nitrite solution at room temperature, heating to 120 ℃ after the dropwise adding is finished, performing heat preservation, controlling the temperature to 6h, stirring, cooling and suction filtering to obtain 129g of a product with the purity: 98% (GC) yield 84.8%.
The above-described embodiments are merely preferred embodiments of the present invention, and are not intended to limit the present invention in any way. While the invention has been described with reference to preferred embodiments, it is not intended to be limiting. Therefore, any simple modification, equivalent variation and modification of the above embodiments according to the technical substance of the present invention shall fall within the scope of the technical solution of the present invention.

Claims (10)

1. A process for the preparation of a compound of formula I comprising the steps of:
(1) Hydrolyzing a compound of formula III in the presence of sulfuric acid in the absence of an organic solvent;
(2) The reaction liquid obtained in the step (1) reacts in the presence of sodium nitrite to obtain the compound shown in the formula I,
the concentration of the sulfuric acid is 75-90%;
the reaction temperature in the step (1) is 100-150 ℃;
the reaction temperature in the step (2) is 80-140 ℃.
2. A process for the preparation of a compound of formula I according to claim 1, wherein the process meets one or more of the following conditions:
(1) The concentration of the sulfuric acid is 80-85%;
(2) The sodium nitrite is sodium nitrite aqueous solution, and the concentration of the sodium nitrite aqueous solution is preferably 5-45%;
(3) The mol ratio of the compound of the formula III to sodium sulfite is 1 (1-2);
(4) The feeding amount of the sulfuric acid relative to the compound of the formula III is 2-10 ml/kg;
(5) The reaction time in the step (1) is 1 to 8 hours;
(6) The reaction time in the step (2) is 2-10 hours;
(7) The reaction temperature in the step (1) is 140-150 ℃; and
(8) The reaction temperature in the step (2) is 120-140 ℃.
3. A process for the preparation of a compound of formula I according to claim 2, wherein the process meets one or more of the following conditions:
(1) The concentration of sulfuric acid is 80%;
(2) The concentration of the sodium nitrite aqueous solution is 20-30%;
(3) The mol ratio of the compound of the formula III to sodium sulfite is 1 (1.1-1.6);
(4) The addition amount of the sulfuric acid relative to the compound of the formula III is 4-6ml/kg;
(5) The reaction time in step (1) was 3 hours;
(6) The reaction time in the step (2) is 5-6 hours;
(7) The reaction temperature in the step (1) is 140 ℃; and
(8) The reaction temperature in step (2) was 120 ℃.
4. A process for the preparation of a compound of formula I according to claim 2, wherein the process meets one or more of the following conditions:
(1) The concentration of the sodium nitrite aqueous solution is 20%;
(2) The molar ratio of the compound of formula III to sodium sulfite is 1:1.1, 1:1.2, 1:1.3, 1:1.4, 1:1.5 or 1:1.6; and
(3) The amount of sulfuric acid added was 5ml/kg relative to the compound of formula III.
5. A process for the preparation of a compound of formula I according to any one of claims 1 to 4, comprising the steps of:
(1) In the absence of an organic solvent, hydrolyzing the compound of formula III in the presence of 80% sulfuric acid at 140 ℃;
(2) The reaction liquid obtained in the step (1) reacts with 20% sodium nitrite to obtain the compound shown in the formula I, and the reaction temperature is 120 ℃.
6. A process for the preparation of a compound of formula II comprising the steps of: hydrolyzing the compound of the formula III in the presence of sulfuric acid under the condition of no organic solvent to obtain the compound of the formula II,
the concentration of the sulfuric acid is 75-90%;
the temperature of the hydrolysis is 100-150 ℃.
7. A process for the preparation of a compound of formula II according to claim 6, wherein the process meets one or more of the following conditions:
(1) The concentration of the sulfuric acid is 80-85%, preferably 80%;
(2) The molar ratio of the compound of formula III to sodium sulfite is 1 (1-2), preferably 1 (1.1-1.6), for example 1:1.1, 1:1.2, 1:1.3, 1:1.4, 1:1.5 or 1:1.6;
(3) The sulfuric acid is added in an amount of 2 to 10ml/kg, preferably 4 to 6ml/kg, for example 5ml/kg, relative to the compound of formula III;
(4) The hydrolysis time is 1 to 8 hours, preferably 3 hours; and
(5) The temperature of the hydrolysis is 140 to 150 ℃, preferably 140 ℃.
8. A process for the preparation of a compound of formula I, comprising the steps of:
(1) Hydrolyzing the compound of the formula III in the presence of sulfuric acid in the absence of an organic solvent to obtain a compound of the formula II,
the concentration of the sulfuric acid is 75-90%;
the temperature of the hydrolysis is 100-150 ℃;
(2) Hydrolyzing the compound of the formula II in the presence of acid and sodium nitrite to obtain a compound of the formula I,
the acid is sulfuric acid or hydrochloric acid;
the concentration of sulfuric acid is 20-80% when the acid is sulfuric acid;
when the acid is hydrochloric acid, the concentration of the hydrochloric acid is 30-35%.
9. The process for the preparation of a compound of formula I according to claim 8, wherein step (2) fulfils one or more of the following conditions:
(1) In step (2), the acid is 30 to 50% sulfuric acid, for example 40% sulfuric acid;
(2) In the step (2), the sodium nitrite is sodium nitrite aqueous solution, and the concentration of the sodium nitrite aqueous solution is preferably 5-45%, and more preferably 20-30%;
(3) In step (2), the molar ratio of the compound of formula II to sodium sulfite is 1 (1-2), preferably 1 (1.1-1.6), for example 1:1.1, 1:1.2, 1:1.3, 1:1.4, 1:1.5 or 1:1.6;
(4) In step (2), the acid is added in an amount of 2 to 10ml/kg, preferably 2 to 5ml/kg, more preferably 3 to 4ml/kg, relative to the compound of formula II;
(5) In step (2), the temperature of the hydrolysis is 80 to 140 ℃, preferably 100 to 130 ℃, for example 120 ℃; and
(6) In the step (2), the hydrolysis time is 2 to 10 hours, preferably 5 to 6 hours;
and/or, the step (1) satisfies one or more of the following conditions:
(1) In the step (1), the concentration of the sulfuric acid is 80-85%, preferably 80%;
(2) In step (1), the molar ratio of the compound of formula III to sodium sulfite is 1 (1-2), preferably 1 (1.1-1.6), for example 1:1.1, 1:1.2, 1:1.3, 1:1.4, 1:1.5 or 1:1.6;
(3) In step (1), the sulfuric acid is fed in an amount of 2 to 10ml/kg, preferably 4 to 6ml/kg, for example 5ml/kg, relative to the compound of formula III;
(4) In the step (1), the time of the hydrolysis is 1 to 8 hours, preferably 3 hours; and
(5) In step (1), the hydrolysis temperature is 140 to 150 ℃, preferably 140 ℃.
10. A process for the preparation of a compound of formula I according to claim 8 or 9, wherein in step (2) the preparation comprises the steps of: the compound of formula II is hydrolyzed in the presence of 40% sulfuric acid and 20% aqueous sodium nitrite to give the compound of formula I at a temperature of 120 ℃.
CN202311505931.2A 2023-11-13 2023-11-13 Preparation method of o-trifluoromethyl benzoic acid Pending CN117623897A (en)

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