Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Method for continuously preparing nitrile from amide

A technology of amide and amide, which is applied in the field of continuous preparation of nitriles from amides, can solve the problems of continuous production, corrosion of equipment, environmental protection pressure, and ineffective reaction, etc., to achieve wide substrate applicability, reduce three wastes discharge, The effect of low thermal stability requirement

Active Publication Date: 2020-12-04
QUZHOU RES INST OF ZHEJIANG UNIV +1
View PDF4 Cites 4 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The traditional method for the dehydration of amides to prepare nitriles is to use stoichiometric acidic reagents (such as P 4 o 10 , POCl 3 , SOCl 2 、TiCl 4 etc.) and alkaline reagents (such as NaBH 4 ) as a dehydrating agent to promote the dehydration of amides. These methods will produce a large amount of acidic or alkaline by-products, which will corrode equipment and cause high environmental pressure; on this basis, scholars have developed a series of new catalysts, including hydrosilane dehydration systems, high-temperature catalytic system, palladium catalyzed dehydration nitrilation system, etc., in which various transition metals or nitrites catalyze the activation of Si-H bonds of hydrosilicides to form electrophilic silicon hydrogen species. These reaction intermediates can promote the dehydration of primary amides to form nitriles, However, during the reaction process, hydrogen and silyl ether are produced, which increases the difficulty of separation; in the absence of a dehydrating agent, the dehydration of amide to generate nitrile requires a higher reaction temperature (>160 ° C), Campbell et al. (Campbell J, McdougaldG , Mcnab H, et al.Synthesis, 2007, 20:3179-3184) reported the dehydration performance of amides and oximes catalyzed by dehydrating agent 3A molecular sieve and tungsten trioxide under fast vacuum pyrolysis conditions, and the reaction did not produce other by-products , but the reaction temperature is high (above 300°C), only suitable for thermally stable amides
Sueoka et al. (Sueoka S, Mitsudome T, Mizugaki T, et al. Chem Commun, 2010, 46:8243-8245) reported that a material supporting monomeric vanadium oxide on hydrotalcite can be used for heterogeneous amide dehydration Catalyst, under the catalysis of 20mol% load, amide is refluxed in mesitylene and dehydrated into nitrile, which is difficult to achieve continuous production
[0005] If the above-mentioned amide dehydration reaction in the absence of a dehydrating agent is assumed to be carried out at room temperature, the reaction will not be able to proceed effectively

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
  • Method for continuously preparing nitrile from amide
  • Method for continuously preparing nitrile from amide
  • Method for continuously preparing nitrile from amide

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] Example 1. A method for the efficient dehydration of benzamide and continuous preparation of benzonitrile catalyzed by a molecular sieve-supported lead catalyst

[0034] (1) immerse 100g molecular sieve in the aqueous solution 100ml that contains 10g lead diacetate, until this solution is completely absorbed by molecular sieve;

[0035] The obtained impregnated molecular sieve was dried in a drying oven at 80° C. for 2 hours, at 120° C. for 2 hours, and then calcined in a muffle furnace at 400° C. for 2 hours to obtain a catalyst.

[0036] In this catalyst, the atomic loading of lead is 6.4 wt% of the molecular sieve.

[0037] (2) Fill the above-mentioned catalyst in a fixed-bed reactor.

[0038] The height of the fixed bed reactor is L=1500mm, the inner diameter D=100mm; 5000g of catalyst is installed inside.

[0039] The top of the fixed-bed reactor is equipped with a pre-heater, the set temperature of the pre-heater is 150°C, and the reaction temperature (bed tempe...

Embodiment 2~8

[0055] Examples 2-8, changing the load of lead diacetate, other operations are the same as in Example 1, to obtain Examples 2-8, see Table 1 for process parameters and reaction results.

[0056] Table 1

[0057] Example Loading amount of lead diacetate (wt%) Raw material conversion rate (%) Reaction selectivity (%) Product yield (%) 2 2 91.3 100 88.7 3 5 94.6 100 92.2 4 8 95.9 100 93.5 5 12 97.5 100 95.5 6 15 97.7 100 95.7 7 18 97.9 100 95.8 8 20 98.0 100 95.8

Embodiment 9~13

[0058] Examples 9-13, changing the type of lead salt, the atomic loading of lead remains unchanged, which is still 6.4wt% of the molecular sieve. Other operations were the same as in Example 1 to obtain Examples 9-13. See Table 2 for process parameters and reaction results.

[0059] Table 2

[0060] Example lead salt Raw material conversion rate (%) Reaction selectivity (%) Product yield (%) 9 Lead metaborate 97.0 100 94.8 10 lead chloride 93.7 100 91.2 11 lead bromide 94.1 100 92.0 12 lead phosphate 96.5 100 94.3 13 lead nitrate 95.2 100 92.8

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 method for continuously preparing nitrile from amide, which comprises the following steps: preparing a molecular sieve-loaded lead catalyst from a lead salt and a molecular sieve by an impregnation method, and filling a fixed bed reactor with the molecular sieve-loaded lead catalyst; feeding an amide or an amide solution into the fixed bed reactor from the top of the fixed bed for catalytic dehydration, and leading out an obtained reaction product from the bottom of the fixed bed; and separating the reaction product to obtain a crude nitrile product corresponding to amide. A fixed bed continuous production process is adopted, the reaction process is simple, the production efficiency is high, product aftertreatment is simple, and industrial production is easy to achieve.

Description

technical field [0001] The invention belongs to the field of chemical industry, in particular to a method for continuously preparing nitriles from amides. Background technique [0002] Nitrile is an important chemical raw material and synthetic intermediate, widely used in the manufacture of medicines, synthetic fibers and plastics. For example, adiponitrile is the raw material for the preparation of nylon 66. Acrylonitrile is the monomer used to produce polyacrylonitrile. It is copolymerized with other monomers and can be used to produce synthetic rubber and engineering plastics. Benzonitrile is mainly used as an intermediate for advanced coatings such as benzomelamine, and is also an intermediate for the synthesis of pesticides, aliphatic amines, and benzoic acid, and can be used as a solvent for nitrile rubber, resins, polymers, and coatings. Phenylacetonitrile is used to produce phenylacetic acid, phenylethylamine, diphenylacetonitrile, β-phenylethanol, phenylacetaldehy...

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
Patent Type & Authority Applications(China)
IPC IPC(8): C07B43/08C07C253/20C07C255/50C07C255/57C07C255/54C07C255/58C07C255/51C07C255/52C07C255/33C07C255/03C07C255/46C07C255/04C07C319/12C07C323/62C07D307/68C07D213/84C07D215/48C07D333/38B01J29/70B01J29/08
CPCC07B43/08C07C253/20C07C319/12C07D307/68C07D213/84C07D215/48C07D333/38B01J29/7053B01J29/087C07C2601/14B01J2229/18C07C255/50C07C255/57C07C255/54C07C255/58C07C255/51C07C255/53C07C255/52C07C255/33C07C255/03C07C255/46C07C255/04C07C323/62Y02P20/584
Inventor 陈新志阮诗想阮建成周少东钱超
Owner QUZHOU RES INST OF ZHEJIANG UNIV
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products