Method for producing lactic acid from glycerin catalyzed by a supported catalyst

A catalyst-catalyzed glycerol, supported technology, used in chemical instruments and methods, physical/chemical process catalysts, oxidation of carboxylic acids, etc., can solve the problem of high reaction temperature and reaction pressure, low reaction concentration of glycerol, long reaction time, etc. problem, to achieve the effect of low reaction temperature and reaction pressure, good industrial prospects, and fast reaction rate

Inactive Publication Date: 2016-03-02
JIANGSU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Glycerol is a by-product in the production process of biodiesel. For every ten tons of biodiesel produced, one ton of glycerin is produced. With the increase of biodiesel production year by year, the production of glycerin is also very large. A series of chemicals are produced by converting glycerin As well as chemical intermediates, it has the characteristics of renewable and zero carbon dioxide emissions, and glycerol is rich in active hydroxyl groups, which can be easily replaced to synthesize specialty chemicals. Therefore, the development and utilization of glycerin has great prospects; recent studies have found that the use of glycerin to prepare lactic acid Not only has the new use of glycerin been developed, but it has also provided a sustainable source of raw materials for lactic acid; it can be seen from literature reports that there are fermentation methods and chemical synthesis methods for the preparation of lactic acid from glycerol, and the chemical synthesis methods include noble metal aerobic catalysis and high temperature hydrothermal anaerobic Oxidation method, while the fermentation method and noble metal aerobic catalysis method have the disadvantages of high cost, low glycerol reaction concentration and long reaction time; high temperature hydrothermal anaerobic oxidation method has higher requirements for reaction temperature and reaction pressure; DebdutRoy et al. adopt industrial production Cu / SiO 2 , CuO / Al 2 o 3 and Cu 2 O, can effectively reduce the reaction temperature, but the reaction temperature, reaction time and lactic acid selectivity need to be improved

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] Weigh 4.58g of sodium hydroxide (Sinopharm Chemical Reagent Co., Ltd.) and 0.46g of 5% CuO / MgO into a 400mL autoclave, then weigh 9.20g of glycerin (Sinopharm Chemical Reagent Co., Ltd.) with a 100mL volumetric flask Make constant volume, add it into the reaction kettle, ventilate it with nitrogen gas, then seal it well, heat it to 230°C, time it, and react for 2 hours.

[0021] At the end of the reaction, take 20mL of the reaction solution and acidify it with hydrochloric acid until the pH is 2~3, measure the volume after acidification, transfer 1mL with a pipette and dilute it to 25mL with deionized water, and perform high performance liquid chromatography detection to determine the content of lactic acid. Yield; then use a pipette to pipette 1 mL of the acidified sample and 20 μL of n-butanol for gas chromatography analysis; the analysis shows that the conversion rate of glycerol is 95%, and the selectivity of lactic acid is 89%.

[0022] Reaction conditions: Glycero...

Embodiment 2

[0024] Weigh 4.58g sodium hydroxide (Sinopharm Chemical Reagent Co., Ltd.) and 0.46g20%CuO / ZrO 2 , put them together into a 400mL autoclave, then weigh 9.20g of glycerin (Sinopharm Chemical Reagent Co., Ltd.) and use a 100mL volumetric flask to make a constant volume, add it to the autoclave, pass in nitrogen to evacuate, then seal it well, and heat After reaching 230°C, the timer was used to react for 4 hours.

[0025] At the end of the reaction, take 20mL of the reaction solution and acidify it with hydrochloric acid until the pH is 2~3, measure the volume after acidification, transfer 1mL with a pipette and dilute it to 25mL with deionized water, and perform high performance liquid chromatography detection to determine the content of lactic acid. Yield; pipette 20 μL of 1 mL acidified sample for gas chromatography analysis; analysis shows that the conversion rate of glycerol is 75%, and the selectivity of lactic acid is 70%.

[0026] Reaction conditions: Glycerol concentra...

Embodiment 3

[0028] Weigh 4.58g sodium hydroxide (Sinopharm Chemical Reagent Co., Ltd.) and 0.46g20%CuO / TiO 2 , put them together into a 400mL autoclave, then weigh 9.20g of glycerin (Sinopharm Chemical Reagent Co., Ltd.) and use a 100mL volumetric flask to make a constant volume, add it to the autoclave, pass in nitrogen to evacuate, then seal it well, and heat After reaching 230°C, time it and react for 2 hours.

[0029] At the end of the reaction, take 20mL of the reaction solution and acidify it with hydrochloric acid until the pH is 2~3, measure the volume after acidification, transfer 1mL with a pipette and dilute it to 25mL with deionized water, and perform high performance liquid chromatography detection to determine the content of lactic acid. Yield; then pipette 20 μL of 1 mL acidified sample for gas chromatography analysis; the analysis shows that the conversion rate of glycerol is 85%, and the selectivity of lactic acid is 90%.

[0030] Reaction conditions: Glycerol concentrat...

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PUM

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Abstract

The invention relates to the technical field of lactic acid preparation, in particular to a method for preparing lactic acid from glycerin with a supported catalyst. The selectivity of lactic acid can reach 70-90%, and the conversion rate of glycerin can reach 72-100%. As a raw material, the supported copper oxide is used as a catalyst, and the reaction is carried out in a high-pressure reactor to obtain lactic acid under an oxygen-free and alkaline condition provided by an alkali source. The carrier of the supported copper oxide catalyst includes MgO, ZrO2, Metal oxides including TiO2, CeO2 and ZnO, activated carbon or hydroxyapatite. The supported copper oxide catalyst is easy to prepare, low in price and long in service life. The invention has the advantages of low reaction temperature and pressure, high catalyst activity and good selectivity, fast reaction rate, safe and environment-friendly process, etc., and has good industrial prospect.

Description

technical field [0001] The invention relates to the technical field of lactic acid preparation, in particular to a method for preparing lactic acid from glycerol with a supported catalyst. Background technique [0002] Lactic acid, chemical system name 2-hydroxypropanoic acid (2-Hydroxypropanoic Acid), because the carbon atom at the α position of the carboxyl group in the lactic acid molecule is an asymmetric carbon atom, so lactic acid has two kinds of optical activity: left-handed (L-type) and right-handed (Type D) enantiomer; lactic acid was first discovered in yoghurt by Scheele in 1850, hence the name of lactic acid; lactic acid is one of the three recognized organic acids in the world, and widely exists in the human body, animals and microorganisms Metabolism also exists in every aspect of people's life. [0003] Lactic acid is an organic acid with a wide range of uses, mainly used in the food and pharmaceutical industries; the use of lactic acid with a mass fraction ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C51/02C07C51/16C07C59/08B01J23/72B01J23/83B01J23/80B01J27/18
CPCB01J23/002B01J23/72B01J23/80B01J23/83B01J27/1817C07C51/02C07C51/16C07C59/08
Inventor 张长华尹海旭殷恒波王爱丽冯永海沈灵沁鲁华胜
Owner JIANGSU UNIV
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