CN114685307A - Method for preparing 4-acetamido-3-nitrobenzoic acid by micro-reaction system - Google Patents

Method for preparing 4-acetamido-3-nitrobenzoic acid by micro-reaction system Download PDF

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CN114685307A
CN114685307A CN202210135063.2A CN202210135063A CN114685307A CN 114685307 A CN114685307 A CN 114685307A CN 202210135063 A CN202210135063 A CN 202210135063A CN 114685307 A CN114685307 A CN 114685307A
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acid
acetamido
sulfuric acid
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flow rate
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杨金会
周涛
李典军
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Ningxia University
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C231/00Preparation of carboxylic acid amides
    • C07C231/12Preparation of carboxylic acid amides by reactions not involving the formation of carboxamide groups
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0093Microreactors, e.g. miniaturised or microfabricated reactors

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Abstract

The invention discloses a method for preparing 4-acetamido-3-nitrobenzoic acid by a micro-reaction system, which comprises the following steps: s1, dissolving 4-acetamidobenzoic acid (25g,0.1523mol) in 98% sulfuric acid (125mL,2.3000mol), and dissolving 65% nitric acid (48mL,0.6923mol) in 98% sulfuric acid (39mL,0.7176 mol); s2, controlling the flow rate of the 4-acetamino-sulphuric acid solution to be 0.4mL/min and the flow rate of the nitric-sulfuric acid mixed solution to be 0.2mL/min, injecting materials into the microchannel reaction tube, controlling the reaction temperature to be 20 ℃, and ensuring the liquid holdup of the microchannel reaction tube to be 3.2 mL; and S3, quenching the reaction liquid by using an ice water solution, separating out, filtering, washing a filter cake by using water, and drying in vacuum to obtain a yellow solid, wherein the yellow solid is the 4-acetamido-3-nitrobenzoic acid. The invention has the advantages that: the liquid holdup can be obviously reduced, the temperature control is more accurate, the danger of production operation is reduced, and the continuous production is realized by using the microchannel reaction tube.

Description

Method for preparing 4-acetamido-3-nitrobenzoic acid by micro-reaction system
Technical Field
The invention relates to the technical field of chemical industry, in particular to a method for preparing 4-acetamido-3-nitrobenzoic acid by a micro-reaction system.
Background
4-acetamido-3-nitrobenzoic acid is an important nitro-containing compound, has important medicinal value and application prospect, is widely applied to the fields of chemistry, medicine, materials, agricultural science and the like, the synthesis of the compound increasingly arouses the interest of organic chemists, and various methods for synthesizing 4-acetamido-3-nitrobenzoic acid have been developed, and the synthesis reaction formula is shown in figure 1.
Through improvement, several improved synthesis methods of 4-acetamido-3-nitrobenzoic acid are developed, and the synthesis reaction formula is shown in figure 2.
These methods have great limitations, such as more reaction liquid and great danger; the reaction is sensitive to temperature, the temperature control is difficult, and the like, and a new method for synthesizing the 4-acetamido-3-nitrobenzoic acid needs to be developed.
Disclosure of Invention
In order to solve the problems, the application provides the method for preparing the 4-acetamido-3-nitrobenzoic acid by using the micro-reaction system which can obviously reduce liquid holdup, control temperature more accurately, reduce production operation danger and realize continuous production by using the micro-channel reaction tube.
In order to solve the technical problems, the technical scheme provided by the invention is as follows: a method for preparing 4-acetamido-3-nitrobenzoic acid by using a micro-reaction system comprises the following steps:
s1, dissolving 4-acetamidobenzoic acid (25g,0.1523mol) in 98% sulfuric acid (125mL,2.3000mol), and dissolving 65% nitric acid (48mL,0.6923mol) in 98% sulfuric acid (39mL,0.7176 mol);
s2, controlling the flow rate of the 4-acetamino-sulphuric acid solution to be 0.4mL/min and the flow rate of the nitric-sulfuric acid mixed solution to be 0.2mL/min, injecting materials into the microchannel reaction tube, controlling the reaction temperature to be 20 ℃, and ensuring the liquid holdup of the microchannel reaction tube to be 3.2 mL;
and S3, quenching the reaction liquid by using an ice water solution, separating out, filtering, washing a filter cake by using water, and drying in vacuum to obtain a yellow solid, wherein the yellow solid is the 4-acetamido-3-nitrobenzoic acid.
Compared with the prior art, the invention has the advantages that: 4-Acylaminobenzoic acid 1(25g,0.1523mol) was dissolved in 98% sulfuric acid (125mL,2.3000mol) in a total volume of 136 mL; 65% nitric acid (48mL,0.6923mol) was dissolved in 98% sulfuric acid (39mL,0.7176mol) in a total volume of 81 mL; controlling the flow rate of the injected material, the reaction temperature and the liquid holdup in the microchannel reaction tube; the liquid holdup can be obviously reduced, the temperature control is more accurate, and the danger of production operation is reduced.
Drawings
FIG. 1 is a diagram of a prior art synthesis of the present invention.
FIG. 2 is a diagram of the synthesis of reaction formula two according to the prior art.
FIG. 3 is a synthesis scheme of the present invention.
FIG. 4 is a product spectrum of the present invention.
Detailed Description
Examples
4-Acylaminobenzoic acid 1(25g,0.1523mol) was dissolved in 98% sulfuric acid (125mL,2.3000mol) in a total volume of 136 mL. 65% nitric acid (48mL,0.6923mol) was dissolved in 98% sulfuric acid (39mL,0.7176mol) in a total volume of 81 mL.
The flow rate of the raw material sulfuric acid solution is controlled to be 0.8mL/min, the reaction temperature is 0 ℃, and the flow rate of the mixed acid of nitric acid and sulfuric acid is changed.
Figure RE-GDA0003678658740000021
TABLE I shows the yield change at different flow rates of mixed nitric-sulfuric acid
The flow rate of the raw material sulfuric acid solution is controlled to be 0.8mL/min, the flow rate of the nitric-sulfuric mixed acid is controlled to be 0.4mL/min, and the reaction temperature is changed.
Figure RE-GDA0003678658740000022
TABLE II yield change at different temperatures
The reaction temperature was controlled at 0 ℃ and the time was varied by changing the flow rate of the two feed paths (ratio).
Figure RE-GDA0003678658740000023
Figure RE-GDA0003678658740000031
TABLE III is the change in yield at different reaction times
The method for preparing the 4-acetamido-3-nitrobenzoic acid by the micro-reaction system comprises the following steps:
s1, dissolving 4-acetamidobenzoic acid (25g,0.1523mol) in 98% sulfuric acid (125mL,2.3000mol), and dissolving 65% nitric acid (48mL,0.6923mol) in 98% sulfuric acid (39mL,0.7176 mol);
s2, controlling the flow rate of the 4-acetamino-sulphuric acid solution to be 0.4mL/min and the flow rate of the nitric-sulfuric acid mixed solution to be 0.2mL/min, injecting materials into the microchannel reaction tube, controlling the reaction temperature to be 20 ℃, and ensuring the liquid holdup of the microchannel reaction tube to be 3.2 mL;
and S3, quenching the reaction liquid by using an ice water solution, separating out, filtering, washing a filter cake by using water, and drying in vacuum to obtain a yellow solid, wherein the yellow solid is the 4-acetamido-3-nitrobenzoic acid.
It should be understood that the above examples are only for clarity of illustration and are not intended to limit the embodiments. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. And are neither required nor exhaustive of all embodiments. And obvious variations or modifications therefrom are within the scope of the invention.

Claims (1)

1. A method for preparing 4-acetamido-3-nitrobenzoic acid by using a micro-reaction system is characterized by comprising the following steps:
s1, dissolving 4-acetamidobenzoic acid (25g,0.1523mol) in 98% sulfuric acid (125mL,2.3000mol), and dissolving 65% nitric acid (48mL,0.6923mol) in 98% sulfuric acid (39mL,0.7176 mol);
s2, controlling the flow rate of the 4-acetamino-sulphuric acid solution to be 0.4mL/min and the flow rate of the nitric-sulfuric acid mixed solution to be 0.2mL/min, injecting materials into the microchannel reaction tube, controlling the reaction temperature to be 20 ℃, and ensuring the liquid holdup of the microchannel reaction tube to be 3.2 mL;
and S3, quenching the reaction liquid by using an ice water solution, separating out, filtering, washing a filter cake by using water, and drying in vacuum to obtain a yellow solid, wherein the yellow solid is the 4-acetamido-3-nitrobenzoic acid.
CN202210135063.2A 2022-02-14 2022-02-14 Method for preparing 4-acetamido-3-nitrobenzoic acid by micro-reaction system Pending CN114685307A (en)

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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3428673A (en) * 1964-06-03 1969-02-18 Du Pont Nitration of 4-acetamidobenzoic acid

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3428673A (en) * 1964-06-03 1969-02-18 Du Pont Nitration of 4-acetamidobenzoic acid

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李林吉等: ""微通道反应器在芳香化合物硝化反应中的应用进展"", 《化学与生物工程》, vol. 38, no. 2, pages 7 - 11 *

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Application publication date: 20220701