Clean production method of vanillin

A clean production and vanillin technology, applied in chemical instruments and methods, preparation of organic compounds, preparation of carbon-based compounds, etc., can solve the problems of high added value, small production scale, troublesome processing process, and difficult separation of silver powder. Achieve the effects of avoiding decomposition or polymerization side reactions, safety and environmental protection in the production process, and shortening the oxidation reaction time

Active Publication Date: 2015-08-19
TIANJIN VOCATIONAL INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For example, the air catalytic oxidation method is adopted in the industrial production of vanillin, the oxidation reaction yield is 86%-90%, and the oxidation reaction time is 12-24 hours. The acid is not stable enough, and there is a relatively serious decomposition or polymerization phenomenon in the long-term oxidation process at a higher temperature
[0007] The study found that if copper oxide is used for chemical oxidation, the oxidation reaction yield is as high as 98%, and the oxidation reaction time is only 1.5-2.5 hours. The problem is that the formed cuprous oxide exists in the form of colloid, which is difficult to separate from the reaction solution and To achieve recycling, it is necessary to select an oxidant that is easy to separate after the oxidation reaction is completed
[0012] The deficiencies in the preparation of reducing agents from fine silver powder include: (1) The reducing agents hydrazine hydrate, formaldehyde and hydroquinone are poisonous, highly irritating, and have serious environmental and safety problems; (2) The cost of reducing agents sodium borohydride and hydroquinone is too high , affecting the production efficiency of silver powder; (3) The reducing agent ascorbic acid is sensitive to changes in the acidity, concentration and temperature of the reducing system, and the production conditions are not easy to control; (4) Most reducing agents need to be used in conjunction with a large number of dispersants, resulting in the subsequent separation of silver powder Difficult; (5) The feed ratio of commonly used reducing agents is too large, and there is a lack of safe and stable new reducing agents
[0013] In the above ultra-fine silver powder production process, the reducing agent is oxidized to generate a large amount of useless waste. The treatment process of these pollutants is troublesome. At present, only because of the high added value of product production and small production scale, the problem of environmental pollution has not been fully addressed. Pay attention to

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] A 1000mL four-neck reaction flask equipped with a stirrer, a condenser and a constant pressure dropping funnel was installed on a constant temperature water bath, and 59.5g of guaiacol (0.48 mol) and 100mL of 4.8mol / L sodium hydroxide were added thereto (0.48 mol), generate sodium guaiacol solution, add 74.1g40% glyoxylic acid (0.4mol) and sodium hydroxide (0.48 mol) of 100mL4.8mol / L respectively through two constant pressure dropping funnels, control The temperature is 20-40°C and the pH is 11-13, and the feed is fed for 1-2 hours. After the feed is completed, the reaction is continued for 4-6 hours to complete the condensation reaction. Use about 200mL of sulfuric acid with a mass percentage concentration of 10% to neutralize the condensation reaction solution to pH 5-6, and use 100mL toluene to separate the unconverted guaiacol in two extractions to obtain the vanillin synthesis intermediate 3-methanol Oxygen-4-hydroxymandelic acid condensation reaction solution,...

Embodiment 2

[0040] Obtain the vanillin synthesis intermediate 3-methoxyl-4-hydroxymandelic acid condensation reaction solution in the same manner as in the examples, and determine the content of MHMA in it to be 0.66mol / L (0.32mol).

[0041] Add silver nitrate solution 237 mL3 mol / L (0.71mol), sodium hydroxide solution 150 mL4.8 mol / L (0.66mol) and the above 3-methoxy-4-hydroxy Mandelic acid solution, react to generate 3-methoxyl-4-hydroxyacetophenone sodium solution and ultra-fine silver powder, the feeding speed is controlled to keep the precipitate generated in the reaction solution as off-white, and the temperature of the reaction solution is maintained at 20-40°C and React at pH 11-13 for 0.5-1 hour, raise the temperature to 50-60°C after feeding is completed, continue to stir and react for 0.5-1 hour to make MHMA completely react, then add 12.0g 20% ​​formic acid solution (0.05mol) to make excess silver nitrate reduction.

[0042] The resulting silver powder was separated by fil...

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Abstract

The invention discloses a clean production method of oxidizing 3-methoxy-4-hydroxy mandelic acid for joint production of vanillin and superfine silver powder under an alkaline condition by adopting silver nitrate. The clean production method comprises the following steps: adding a silver nitrate solution, a 3-methoxy-4-hydroxy mandelic acid solution and a sodium hydroxide solution in a parallel flow manner into a reactor, reacting to generate a 3-methoxy-4-hydroxy acetophenone sodium solution and superfine silver powder, filtering and separating the generated silver powder, washing with deionized water and ethyl alcohol sequentially, and drying to obtain the superfine silver powder, wherein the reduction yield of the silver powder is 99.4 per cent to 100 per cent; acidizing filter liquor after the silver powder is separated, performing decarboxylation on 3-methoxy-4-hydroxy benzoylformic acid to generate the vanillin, using methylbenzene to extract the vanillin therein, recycling the methylbenzene solvent, and performing recrystallization on residues in an ethanol aqueous solution to obtain the vanillin, wherein the oxidation yield of the methoxy-4-hydroxy mandelic acid is 95.7 per cent to 98.5 per cent. The silver nitrate is taken as an oxidizing agent to prepare the vanillin, so that the oxidation yield is improved, and the oxidation reaction time is shortened. Two practical fine chemical products can be produced simultaneously, the raw materials can be sufficiently utilized, the generation of waste materials is reduced, the production cost is reduced, and the technological process is safe and environment-friendly.

Description

technical field [0001] The invention relates to a clean production method of vanillin, in particular to a clean production method for jointly producing vanillin and superfine silver powder by oxidizing 3-methoxy-4-hydroxymandelic acid under alkaline conditions with silver nitrate, Two kinds of practical fine chemical products can be obtained at the same time, belonging to the fields of new chemical materials and environmental protection. Background technique [0002] Vanillin (English name Vanillin), chemical name 3-methoxy-4-hydroxybenzaldehyde, chemical formula C 8 h 8 O 3 , Molecular weight 152.2, white needle crystal, melting point 81-83 ℃, boiling point 284 ℃, slightly soluble in water, soluble in ethanol and chloroform, with vanilla aroma and strong milky aroma. Vanillin is one of the most produced synthetic flavors in the world, and it is also an important intermediate for synthetic drugs and chemical products. China has a production capacity of 25,000 tons of vani...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C47/58C07C45/67B22F9/24
CPCB22F9/24B22F2009/245C07C45/676C07C51/353C07C51/367C07C51/373C07C47/58C07C59/90C07C59/64
Inventor 李建生李霞于韶梅王会影梁红娟
Owner TIANJIN VOCATIONAL INST
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