Method for preparing lactic acid through catalyzing glycerol by supported catalyst

A catalyst-catalyzed glycerol, supported technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc. The problems of low concentration and long reaction time can achieve the effect of low reaction temperature and reaction pressure, good industrial prospects and fast reaction rate.

Inactive Publication Date: 2014-09-17
JIANGSU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004]Glycerin is a by-product in the production of biodiesel. For every ten tons of biodiesel produced, one ton of glycerin is produced. With the increase of biodiesel production year by year, glycerin The output is also very large, using glycerin to produce a series of chemicals and chemical intermediates, with the characteristics of renewable and zero carbon dioxide emissions, and glycerin is rich in active hydroxyl groups, which can be easily replaced to synthesize special chemicals, so glycerin's Development and utilization have great prospects; recent studies have found that the use of glycerol to prepare lactic acid not only develops new uses of glycerin, but also provides 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. Chemical synthesis methods include noble metal aerobic catalysis and high-temperature hydrothermal anaerobic oxidation, while fermentation and noble metal aerobic catalysis have the disadvantages of high cost, low glycerol reaction concentration and long reaction time; high-temperature hydrothermal anaerobic oxidation Higher requirements on reaction temperature and reaction pressure; Debdut Roy et al. used industrially produced Cu / SiO2, CuO / Al2O3 and Cu2O 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 4.58 g of sodium hydroxide (Sinopharm Chemical Reagent Co., Ltd.) and 0.46 g of 5% CuO / MgO into a 400 mL autoclave, then weigh 9.20 g of glycerin (Sinopharm Chemical Reagent Co., Ltd.) with 100 The mL volumetric flask was fixed to volume, added to the reaction kettle, ventilated with nitrogen gas, then sealed well, heated to 230 °C, timed, and reacted for 2 hours.

[0021] At the end of the reaction, take 20 mL of the reaction solution and acidify it with hydrochloric acid until the pH is 2~3, measure the volume after acidification, transfer 1 mL with a pipette and dilute to 25 mL with deionized water, and perform high performance liquid chromatography detection. Measure the production of lactic acid; 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: glycerol concentration: 1.0 M; NaOH / g...

Embodiment 2

[0024] Weigh 4.58 g sodium hydroxide (Sinopharm Chemical Reagent Co., Ltd.) and 0.46 g 20% ​​CuO / ZrO 2 , together into a 400 mL autoclave, then weighed 9.20 g of glycerin (Sinopharm Chemical Reagent Co., Ltd.) with a 100 mL volumetric flask for constant volume, added it to the autoclave, ventilated it with nitrogen gas, and then sealed it well , heated to 230°C and timed, and reacted for 4 hours.

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

[0026] Reaction conditions: Glycerol concentr...

Embodiment 3

[0028] Weigh 4.58 g sodium hydroxide (Sinopharm Chemical Reagent Co., Ltd.) and 0.46 g 20% ​​CuO / TiO 2 , together into a 400 mL autoclave, then weighed 9.20 g of glycerin (Sinopharm Chemical Reagent Co., Ltd.) with a 100 mL volumetric flask for constant volume, added it to the autoclave, ventilated it with nitrogen gas, and then sealed it well , after heating to 230°C, timed and reacted for 2 hours.

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

[0030] Reaction conditions: Glycerol concentr...

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PUM

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Abstract

The invention relates to the technical field of lactic acid preparation and particularly relates to a method for preparing lactic acid through catalyzing glycerol by a supported catalyst. According to the method, the selectivity of lactic acid can reach 70-90%, and the conversion ratio of glycerol can reach 72-100%. The method is characterized in that reaction is carried out on glycerol which serves as a raw material in a high-pressure reactor under anaerobic and alkali source provided alkaline conditions in the presence of supported copper oxide which serves as a catalyst, thereby obtaining lactic acid, wherein a support of the supported copper oxide catalyst contains metal oxides, including MgO, ZrO2, TiO2, CeO2 and ZnO, activated charcoal or hydroxyapatite; the supported copper oxide catalyst is easy to prepare, low in cost and relatively long in service life. The method has the advantages that the reaction temperature and reaction pressure are low, the catalyst activity is high, the selectivity is good, the reaction rate is high, and the process flow is safe and environmental-friendly and the like, so that the industrial prospect is good.

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, the chemical system is named 2-hydroxypropanoic acid (2-Hydroxypropanoic acid). Since the carbon atom at the alpha position of the carboxyl group in the lactic acid molecule is an asymmetric carbon atom, lactic acid has two kinds of optical activity: left-handed (L-type) and The dextrorotatory (D-type) 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, widely present in the human body, animals and The metabolism of microorganisms also exists in all aspects of people's lives. [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...

Claims

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Application Information

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Patent Type & Authority Applications(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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