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

Method for preparing DCB reduzate through continuous catalytic hydrogenation reduction

A catalytic hydrogenation and catalyst technology, which is applied in the preparation of hydrazine, chemical recovery, organic chemistry, etc., can solve the problems of unstable reaction control, toluene-containing waste gas emission, and large volume of the reactor, so as to achieve internal recycling and reduce by-products Fewer, more selective effects

Active Publication Date: 2020-05-08
ZHEJIANG QINYAN TECH CO LTD
View PDF3 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] 1. The volume of the reactor is large, resulting in high investment in equipment;
[0006] 2. A large amount of steam will be consumed in the reaction process, and the labor intensity is relatively high;
[0007] 3. Due to the unstable reaction control, the by-products in the reaction are relatively high;
[0008] 4. There will be a large amount of toluene-containing waste gas discharged into the air during the reaction, and there will be environmental pollution problems

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 preparing DCB reduzate through continuous catalytic hydrogenation reduction
  • Method for preparing DCB reduzate through continuous catalytic hydrogenation reduction
  • Method for preparing DCB reduzate through continuous catalytic hydrogenation reduction

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Add 600g of adjacent reactors to 3 2L continuous reactors connected in series (divided into the first-stage reactor / reactor, the second-stage reactor / reactor, and the third-stage reactor / reactor according to the order in series) Nitrochlorobenzene, 720g toluene, 250g 30% liquid caustic soda, 204g desalinated water and 6g 1% Pt / C catalyst, replace the air with nitrogen twice, and then replace the nitrogen with hydrogen twice, start stirring, and heat the reaction mass to 90 ℃, continuously feed hydrogen, control the hydrogen pressure at 1MPa, control the reaction temperature at 90-95 ℃, until all the three reactors react without absorbing hydrogen, the first stage of the intermittent reaction ends, and the substrate preparation for the continuous reaction is completed;

[0033] After the completion of the first step reaction, open the overflow feed valves of 3 kettle-type reactors, and pump o-nitrochlorobenzene, toluene, 30% liquid caustic soda and For desalted water, th...

Embodiment 2

[0038] 600g of o-nitrochlorobenzene, 720g of toluene, 250g of 30% liquid caustic soda, 204g of desalinated water and 4g of 1% Pt / C catalyst were added to three series-connected 2L kettle-type continuous reactors respectively, and the air was replaced with nitrogen for two times. After replacing the nitrogen with hydrogen twice, start stirring, heat the reaction mass to 90°C, continuously feed hydrogen, control the hydrogen pressure at 1.5MPa, and control the reaction temperature at 90-95°C until all the three reactors react without absorbing hydrogen. , the first stage of the batch reaction ends, and the substrate preparation of the continuous reaction is completed;

[0039]After the completion of the first step reaction, open the overflow feed valves of 3 kettle-type reactors, and pump o-nitrochlorobenzene, toluene, 30% liquid caustic soda and For desalted water, the feed rate of o-nitrochlorobenzene is 100g / h, the feed rate of toluene solvent is 120g / h, the feed rate of 30% ...

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 provides a method for preparing a DCB reduzate through continuous catalytic hydrogenation reduction. The method comprises the following steps: adding o-nitrochlorobenzene, toluene, caustic soda liquid with a concentration of 30%, desalted water and a Pt / C catalyst into three continuous tank reactors connected in series, and ending a first-stage intermittent reaction until all reactions do not absorb hydrogen; opening overflow discharge valves of the three tank reactors, and simultaneously pumping o-nitrochlorobenzene, methylbenzene, caustic soda liquid with the concentration of 30% and desalted water into the first tank reactor in proportion by using a metering pump; and continuously introducing hydrogen for catalytic hydrogenation to prepare the DCB reduzat, namely, 2,2-dichlorohydrazobenzene. According to the invention, the loss of the catalyst due to frequent filtering in a batch reaction process can be effectively reduced, internal recycling of the catalyst is achieved, and the service life of the catalyst is prolonged; meanwhile, the tank reactors are relatively small in size, reaction stability is good, product dechlorination is relatively low, selectivity is high and relatively few byproducts is produced; and in addition, exhaust emission in the continuous reaction is greatly reduced, so the environmental pollution is greatly reduced.

Description

technical field [0001] The invention relates to the field of organic chemical synthesis, in particular to a method for preparing a DCB reductant (2,2-dichlorohydroazobenzene) by continuous catalytic hydrogenation reduction. Background technique [0002] The chemical name of DCB is 3,3'-dichlorobenzidine, which is an important yellow organic pigment intermediate. Using DCB as the diazo component can synthesize C.I. Pigment Yellow 12, 13, 14, 17, 56, 63, 83 , 87, 106, 124, 127, 152, 170, 171, 172, 174, 176, 188 and orange 13, 14 and other pigment varieties. [0003] The preparation of DCB is generally based on o-nitrochlorobenzene as raw material, which is reduced under alkaline conditions. The reduction methods include catalytic hydrogenation, electrolytic reduction, chemical reduction, and chemical reduction can be divided into zinc powder method and formaldehyde method. , Sodium hydrosulfide method, hydrazine hydrate method, formic acid method, zinc powder method and hydra...

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): C07C241/02C07C243/22
CPCC07C241/02C07C243/22Y02P20/584
Inventor 王晓辉赵伟仇文仲赵磊苏天伟
Owner ZHEJIANG QINYAN TECH CO LTD
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