Preparation method of p-aminophenylacetic acid

A technology of p-aminophenylacetic acid and p-nitrophenylacetic acid, applied in the field of preparation of p-aminophenylacetic acid, can solve problems such as higher requirements for reaction operating conditions, high preparation cost, and cost reduction, and achieves low cost and low production cost , the effect of good reaction selectivity

Active Publication Date: 2013-07-24
常熟紫金知识产权服务有限公司
View PDF4 Cites 5 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in this type of method, when Raney nickel is selected as the catalyst, higher temperature and pressure are required, and the requirements for the reaction operating conditions are higher; when Pd / C is selected as the catalyst, the preparation cost of the Pd / C catalyst is relatively high, which is not conducive to cut costs

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Preparation method of p-aminophenylacetic acid
  • Preparation method of p-aminophenylacetic acid
  • Preparation method of p-aminophenylacetic acid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] Example 1: Add 18g of p-nitrophenylacetic acid, 180g of ethanol (95%) and 0.36g of 3%Pd / attapulgite catalyst into the pressure reactor, replace the air in the reactor with nitrogen, and then pass in hydrogen to control 0.4MP and temperature 30-40 React at ℃ for 5 hours; let stand to cool to room temperature, open the pressure reactor, and evaporate 60% solvent ethanol; cool and crystallize, filter, and dry to obtain a crude product; recrystallize the crude product with 95% ethanol, decolorize with activated carbon, and obtain light white crystals 12.1g. The yield is 81%.

Embodiment 2

[0020] Example 2: Add 18g of p-nitrophenylacetic acid, 180g of ethanol (95%) and 0.54g of 4%Pd / attapulgite catalyst into the pressure reactor, replace the air in the reactor with nitrogen, and then pass in hydrogen to control 0.5MP and temperature 40-50 React at ℃ for 4 hours; let stand to cool to room temperature, open the pressure reactor, and evaporate 70% solvent ethanol; cool and crystallize, filter, and dry to obtain the crude product; recrystallize the crude product with 95% ethanol, decolorize with activated carbon, and obtain white crystal 12.4 g. The yield is 83%.

Embodiment 3

[0021] Example 3: Add 18g of p-nitrophenylacetic acid, 180g of ethanol (95%) and 0.72g of 5% Pd / attapulgite catalyst into the pressure reactor, replace the air in the reactor with nitrogen, and then pass in hydrogen, control 0.6MP, temperature 50-60 React at ℃ for 3 hours; let stand to cool to room temperature, open the pressure reactor, and evaporate 80% solvent ethanol; cool and crystallize, filter, and dry to obtain the crude product; recrystallize the crude product with 95% ethanol, decolorize with activated carbon, and obtain white crystal 14.2 g. The yield is 95%.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention discloses a preparation method of a p-aminophenylacetic acid, which comprises the following steps of: adding p-nitrophenylacetic acid, ethanol and a catalyst into a pressure reaction kettle in a certain proportion, replacing air in the reaction kettle with nitrogen, feeding hydrogen into the reaction kettle, and controlling a certain pressure and temperature; after the reaction is performed for a period of time, standing the reaction kettle, cooling the obtained product to room temperature, opening the pressure reaction kettle, and extracting 60-80% solvent ethanol through evaporating; carrying out cooling crystallization, filtration and drying on the solvent ethanol so as to obtain a coarse product, and carrying out recrystallization on the coarse product by using ethanol, and carrying out active carbon decoloration on the obtained product so as to obtain white crystalline p-aminophenylacetic acid, wherein the mass ratio of the p-nitrophenylacetic acid, the ethanol to the catalyst is 1:10: (0.02-0.05), the mass concentration of the ethanol is 95%, the mass concentration of the catalyst is 3-8% Pd / attapulgite clay, the reaction pressure is 0.4-0.6 MP, the reaction time is 3-5 hours, and the reaction temperature is 30-60 DEG C. According to the invention, the catalyst is low in cost, less in application amount and convenient for recycling; the method is mild in reaction conditions, energy-saving and environment-friendly; the method is good in reaction selectivity, less in side effects, easy to realize purification, and high in yield; and through taking hydrogen as a raw material, the method is less in pollution, simple in post-processing, and low in production cost.

Description

technical field [0001] The invention relates to a preparation method of p-aminophenylacetic acid. Background technique [0002] p-Aminophenylacetic acid is an important chemical intermediate, commonly used in the synthesis of 3,4-diaminophenylacetic acid, 4-sulfonamidophenylacetic acid, ethyl 4-isocyanatophenylacetic acid, and immunotherapy for the treatment of chronic rheumatoid arthritis Modulator atalide, β-adrenoceptor blocker atenolol, can also be used to prepare azo dyes. Various preparation methods of p-aminophenylacetic acid have been reported in the existing literature, which are summarized as follows: [0003] 1) Using nitrophenylacetic acid as raw material, obtain p-aminophenylacetic acid by reduction with Fe and hydrochloric acid: [0004] [0005] This reaction is a metal reduction method, which requires the use of Fe and hydrochloric acid, and will produce a large amount of waste residue containing iron sludge, which is harmful to the environment. [0006...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): C07C229/42C07C227/04
Inventor 支三军韦长梅孙小军李荣清刘炳华
Owner 常熟紫金知识产权服务有限公司
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products