CN102153527A - Method for preparing 5-hydroxymethylfurfural with fructose - Google Patents

Method for preparing 5-hydroxymethylfurfural with fructose Download PDF

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CN102153527A
CN102153527A CN2011100478058A CN201110047805A CN102153527A CN 102153527 A CN102153527 A CN 102153527A CN 2011100478058 A CN2011100478058 A CN 2011100478058A CN 201110047805 A CN201110047805 A CN 201110047805A CN 102153527 A CN102153527 A CN 102153527A
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fructose
hydroxymethyl furfural
prepare
catalyzer
quality
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CN102153527B (en
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吴廷华
高尤剑
肖文军
吴瑛
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Haining Yuanhua Town Industrial Investment Co., Ltd
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Zhejiang Normal University CJNU
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Abstract

The invention discloses a method for preparing 5-hydroxymethylfurfural with fructose. The method includes the following steps: taking N, N-dimethyl acetamide as solvent, lithium chloride as additive, fructose as a reaction material, and heteropoly acid loaded by titanium dioxide as a catalyst, reacting at the temperature of 80-150DEG C to generate 5-hydroxymethylfurfural. The method has the characteristics of few by-products, high yield, environment-friendly property, moderate reaction conditions, small corrosion to equipment, recyclability of catalyst, and the like, and has industrial prospect.

Description

A kind of method for preparing 5 hydroxymethyl furfural by fructose
Technical field
The present invention relates to the green synthetic compound field that transforms of biomass, be specifically related to a kind of method for preparing 5 hydroxymethyl furfural by fructose.
Background technology
The required energy and the Organic Chemicals overwhelming majority in the world derives from oil, coal and Sweet natural gas at present.These fossil class resources have been made huge contribution for the development and the prosperity of economy of society.But along with non-renewable fossil energy peter out and in order to realize the purpose of human kind sustainable development, make full use of renewable, degradable resource, it is the effective means that solves resource exhaustion and environmental pollution that the method by chemosynthesis makes it become important industrial raw material.The biomass resource reserves are big, renewable, cost is low, and the method by chemosynthesis can prepare the medicine industry intermediate of high added value and the monomer of synthesized polymer material, therefore paid attention to by people gradually.
In recent years, a kind of product 5 hydroxymethyl furfural (5-HMF) of hexose dehydration is considered to produce from biomass the key substance of fuel and industrial chemicals, it can be converted into acids, the aldehydes of various economically valuables, but and a kind of transport fuel 2 that has some commercial potential, 5-dimethyl furan (DMF).Therefore how the synthetic efficiently 5 hydroxymethyl furfural of low value becomes the focus that people study.
Prepare the more existing bibliographical informations of 5 hydroxymethyl furfural by hexose: application number is to disclose a kind of isomerase/dilute hydrochloric acid coupling and catalyzing glucose in the Chinese patent application of CN200910228921.2 to prepare the preparation method of 5 hydroxymethyl furfural, steps of the method are: at first adding Sodium Tetraborate and fixed glucose isomerase react in glucose solution, refilter, isomerase is reclaimed, obtain the mixed solution of glucose and fructose, in mixed solution, add hydrochloric acid, sodium-chlor and propyl carbinol and carry out the synthetic 5 hydroxymethyl furfural of acid catalysis; The shortcoming of this method: the price of isomerase is comparatively expensive, and in reaction process, temperature is wayward, and the active of enzyme lost efficacy easily.Application number is to disclose a kind of method for preparing 5 hydroxymethyl furfural in the Chinese patent application of CN 200810011726.X, and this patent is a reaction solvent with saturated sodium-chloride-propyl carbinol system, and phospho-wolframic acid is a catalyzer, and fructose is converted into 5 hydroxymethyl furfural; The shortcoming of this method: phosphate-tungstic acid is difficult for reclaiming, and product yield is not very high.Application number is to disclose a kind of method for preparing 5 hydroxymethyl furfural in the Chinese patent application of CN200710158825.6, this method is a reaction solvent with ionic liquid 1-methyl-3-alkyl imidazole bromine etc., with acidic ion liquid (imidazole bisulfate, 1-methyl-3-butyl imidazole hydrosulfate), mineral acid (hydrochloric acid, nitric acid, phosphoric acid) and organic acid (formic acid, acetate, citric acid) is catalyzer, and 5 hydroxymethyl furfural is produced in the dehydration of catalysis hexose; The shortcoming of this method: ion liquid viscosity is big, price is comparatively expensive, and mineral acid acidity such as hydrochloric acid, sulfuric acid are bigger, and is comparatively serious to equipment corrosion, is difficult for suitability for industrialized production.
Application number is to disclose the method that a kind of microwave promotes to prepare 5 hydroxymethyl furfural in the Chinese patent application of CN 200710158826.0, with ionic liquid 1-ethyl-3-Methylimidazole bromine etc. is solvent, under the condition of microwave power 200~2000W, 50~100 ℃ of temperature of reaction, reaction times 0.5~30min, 5 hydroxymethyl furfural is produced in the dehydration of biomass monose; The shortcoming of this method: (1) with the type of heating of microwave, can only small batch production, can not realize scale operation; (2) ion liquid viscosity is big, price is comparatively expensive, can only be confined to laboratory study as solvent.
Summary of the invention
What the invention provides a kind of yield height, energy-saving and environmental protection and have an industrial prospect prepares the method for 5 hydroxymethyl furfural by fructose.
A kind ofly prepare the method for 5 hydroxymethyl furfural, may further comprise the steps by fructose:
With N,N-dimethylacetamide (DMA) is solvent, and lithium chloride is an additive, and fructose is reaction raw materials, and the heteropolyacid of titanium dichloride load is a catalyzer, generates 5 hydroxymethyl furfural 80 ℃~150 ℃ reactions.
In order to reach better invention effect, preferably:
The quality of described lithium chloride is 5%~25% of a solvent quality, more preferably 15%~25%.
The quality of described fructose is 5%~35% of a solvent quality, more preferably 5%~25%.
The quality of described catalyzer is 2%~15% of a solvent quality.
The mass ratio of titanium dioxide and heteropolyacid is 1: 1~6 in the described catalyzer, more preferably 1: 2.
Described heteropolyacid (being called for short HPA) mainly can be selected phospho-molybdic acid (H for use 3PMo 12O 40/ TiO 2), phospho-wolframic acid (H 3PW 12O 40/ TiO 2), silicotungstic acid (H 4SiW 12O 40/ TiO 2), silicomolybdic acid (H 4SiMo 12O 40/ TiO 2) in one or more.
Described Preparation of catalysts method can adopt the preparation method of existing loaded catalyst, is generally: with TiO 2Active carrier joins in the heteropolyacid aqueous solution and floods 12h~48h, takes out at 60 ℃~100 ℃ down after the oven dry, activates 2h~5h in temperature is 100 ℃~600 ℃ retort furnace, makes catalyzer; TiO wherein 2The mass ratio of active carrier and heteropolyacid is 1: 1~6.The HPA/TiO that concentration and dipping time by control heteropolyacid solution can make the different loads amount 2Catalyzer, but drop into TiO in the catalyzer that makes under the certain situation of ratio at raw material 2The mass ratio of active carrier and heteropolyacid and raw material drop into the ratio basically identical.
Described TiO 2The preparation method of active carrier can adopt existing TiO 2The preparation method of active carrier is generally: with 1 weight part butyl (tetra) titanate (Ti (OC 4H 9)) be dissolved in 2~6 weight part dehydrated alcohols, in 0.5h~1h, add 3~8 weight parts waters and make the butyl (tetra) titanate hydrolysis, obtain stable TiO 2Gel.Then with TiO 2Gel is put into inherent 500 ℃~800 ℃ insulations (calcination) 8h~10h of retort furnace behind 60 ℃~100 ℃ dry 2h~5h, naturally cool to room temperature after the taking-up, promptly gets TiO after the grinding 2Active carrier.
Described reaction is the fructose dehydration reaction, and the deionized water of available 10mL~50mL stops reaction.
In order to improve the yield of product, described temperature of reaction is preferably 120 ℃~140 ℃.
The qualification that the described reaction times is not strict can be passed through timing sampling, and (TLC) carries out trace analysis with tlc, finishes when raw material fructose reacts, and the terminal point that is considered as reacting gets final product.Through overtesting, to carry out fully in order to make reaction, the described reaction times is generally 10min~300min, more preferably 60min~90min.
Detection method for product yield among the present invention is:
At first dispose the standard model solution of a series of 5 hydroxymethyl furfural standard substance, make absorbancy-concentration standard curve under the 284nm with ultraviolet spectrophotometry.The reaction solution of described reaction is carried out centrifugal, measures the volume of supernatant liquor, obtain the concentration of product again with the uv-spectrophotometric external standard method, calculate the mole number of product 5 hydroxymethyl furfural, calculate yield according to following formula:
5 hydroxymethyl furfural yield=(5 hydroxymethyl furfural mole number/fructose mole number) * 100%.
Compared with prior art, the present invention has following advantage:
The present invention is raw material with fructose, and N,N-dimethylacetamide is as reaction solvent, and lithium chloride is an additive, and carried heteropoly acid is a catalyzer, the preparation 5 hydroxymethyl furfural; The purpose of adding lithium chloride is in order to suppress production of by-products, to improve the productive rate of 5 hydroxymethyl furfural; With the carried heteropoly acid is catalyzer, and titanium dioxide had both guaranteed catalytic activity as the carrier of heteropolyacid, and catalyzer is easier separated, to reduce the consumption of catalyzer.
The present invention can be by further change catalyzer the ratio, starting point concentration, catalyst consumption, content of additive, temperature of reaction and the reaction times of fructose of maturing temperature, dipping time, heteropolyacid and carrier optimize reaction conditions, obtained yield and surpassed 90% 5 hydroxymethyl furfural, had significantly with respect to the yield that has the preparation method now and improved.
The inventive method has that by product is few, productive rate is high, environmental friendliness, reaction conditions gentleness,, characteristics such as catalyzer can reclaim little to equipment corrosion, has industrial prospect.
Embodiment
Embodiment 1
Preparation of catalysts: with 1 weight part butyl (tetra) titanate (Ti (OC 4H 9)) be dissolved in the 1.3 weight part dehydrated alcohols, in 0.5h, add 1 weight parts water and make the butyl (tetra) titanate hydrolysis, obtain stable TiO 2Gel.Then with TiO 2Gel is put into inherent 500 ℃ of insulations (calcination) 10h of retort furnace behind 80 ℃ of dry 3h, naturally cool to room temperature after the taking-up, promptly gets TiO after the grinding 2Active carrier.Then, with TiO 2It is to flood 36h in 15% the phospho-molybdic acid aqueous solution that active carrier joins mass percentage concentration, wherein TiO 2With the mass ratio of phospho-molybdic acid be 1: 2, take out at 80 ℃ down after the oven dry, place activation 3h in 150 ℃ of retort furnaces again, promptly get required catalyzer: the phospho-molybdic acid of titanium dichloride load, i.e. H 3PMo 12O 40/ TiO 2
Embodiment 2
Except phospho-molybdic acid is replaced to silicomolybdic acid, all the other are operated with embodiment 1, make required catalyzer: the silicomolybdic acid of titanium dichloride load, i.e. H 4SiMo 12O 40/ TiO 2
Embodiment 3
Except phospho-molybdic acid is replaced to phospho-wolframic acid, all the other are operated with embodiment 1, make required catalyzer: the phospho-wolframic acid of titanium dichloride load, i.e. H 3PW 12O 40/ TiO 2
Embodiment 4
Except phospho-molybdic acid is replaced to silicotungstic acid, all the other are operated with embodiment 1, make required catalyzer: the silicotungstic acid of titanium dichloride load, i.e. H 4SiW 12O 40/ TiO 2
Embodiment 5~8
In the small test tube of 4 band numberings, add 1g N respectively, N-N,N-DIMETHYLACETAMIDE, 0.1g lithium chloride and 0.1g fructose, stirring and dissolving is warming up to 80 ℃ respectively, 100 ℃, 120 ℃, 140 ℃, add each 60mg of catalyzer that embodiment 1 prepares then, stirring reaction 1h, the deionized water that adds 10mL at last stops reaction.Reaction solution is carried out centrifugal, measures the volume of supernatant liquor, obtain the concentration of product 5 hydroxymethyl furfural again with the uv-spectrophotometric external standard method, yield that draws such as following table 1:
The nucleus magnetic hydrogen spectrum data of product: 1H-NMR (D 2O, 400MHz) δ: 9.320 (s, 1H ,-CHO), 7.348 (d, 1H, H), 6.546 (d, 1H, H), 4.569 (s, 2H, CH 2). the nucleus magnetic hydrogen spectrum data conform to 5-HMF standard spectrogram.
The ir data of product: use coating method, the KBr compressing tablet records the infrared spectra of product.The infared spectrum data of product: 3420cm -1(-OH), 1713cm -1(-CHO), 1670cm -1(C=C), 1026cm -1(C-O-C), 2935cm -1, 2852cm -1(CH 2); Ir data is consistent with the ir data of 5-HMF.
The yield of 5 hydroxymethyl furfural under the table 1 differential responses temperature
Implementation sequence number Temperature (℃) Yield (%)
5 80 15
6 100 56
7 120 77
8 140 75
Embodiment 9~13
In the small test tube of 5 band numberings, add 1g N respectively, the N-N,N-DIMETHYLACETAMIDE, 0.15g lithium chloride and 0.1g fructose, stirring and dissolving is warming up to 120 ℃, adds each 80mg of catalyzer for preparing under embodiment 1 condition then, reaction times is got 0.5h, 1h, 1.5h, 2h, 5h respectively, and the deionized water that adds 10mL at last stops reaction.Reaction solution is carried out centrifugal, measures the volume of supernatant liquor, obtain the concentration of product 5 hydroxymethyl furfural again with the uv-spectrophotometric external standard method, the yield such as the table 2 that draw:
Pairing reaction yield of table 2 differential responses time
Implementation sequence number Time (h) Yield (%)
9 0.5 65
10 1 85
11 1.5 82
12 2 76
13 5 70
Embodiment 14~18
In the small test tube of 5 band numberings, add 1g N respectively, the N-N,N-DIMETHYLACETAMIDE, 0.1g lithium chloride and 0.1g fructose, stirring is dissolved, and is warming up to 120 ℃, add the catalyzer for preparing under embodiment 1 condition then, get 60mg, 80mg, 100mg, 120mg, 150mg respectively, stirring reaction 1h, the deionized water that adds 10mL at last stops reaction.Reaction solution is carried out centrifugal, measures the volume of supernatant liquor, obtain the concentration of product 5 hydroxymethyl furfural again with the uv-spectrophotometric external standard method, the yield such as the table 3 that draw:
The pairing reaction yield of table 3 different catalysts consumption
Implementation sequence number The amount of catalyzer (mg) Yield (%)
14 60 72
15 80 80
16 100 86
17 120 83
18 150 80
Embodiment 19~23
In the small test tube of 5 band numberings, add 1g N respectively, the N-N,N-DIMETHYLACETAMIDE, 0.1g fructose and 0mg, 50mg, 150mg, 200mg, 250mg lithium chloride, stirring is dissolved, and is warming up to 120 ℃, adds each 100mg of catalyzer for preparing under embodiment 1 condition then, stirring reaction 1h, the last deionized water that adds 10mL in each test tube stops reaction.Reaction solution is carried out centrifugal, measures the volume of supernatant liquor, obtain the concentration of product 5 hydroxymethyl furfural again with the uv-spectrophotometric external standard method, the yield such as the table 4 that draw:
The pairing yield of the amount of table 4 different additive
Implementation sequence number The consumption of lithium chloride (mg) Yield (%)
19 / 45
20 50 68
21 150 92
22 200 84
23 250 80
Embodiment 24~28
In the small test tube of 5 band numberings, add 1g N respectively, the N-N,N-DIMETHYLACETAMIDE, 0.15g lithium chloride and 0.05g, 0.1g, 0.15g, 0.2g or 0.25g fructose, stirring is dissolved, and is warming up to 100 ℃, adds each 60mg of catalyzer for preparing under embodiment 1 condition then, stirring reaction 1h, the last deionized water that adds 10mL in each test tube stops reaction.Reaction solution is carried out centrifugal, measures the volume of supernatant liquor, obtain the concentration of product 5 hydroxymethyl furfural again with the uv-spectrophotometric external standard method, the yield such as the table 5 that draw:
The yield of the different fructose original bulk of table 5 correspondence
Implementation sequence number The consumption of fructose (mg) Yield (%)
24 50 63
25 100 62
26 150 62
27 200 61
28 250 60
Embodiment 29~32
In the small test tube of 5 band numberings, add the 1g N,N-dimethylacetamide respectively, 0.15g lithium chloride and 0.1g fructose, stirring is dissolved, and is warming up to 120 ℃, adds the catalyzer H for preparing under embodiment 1 condition then respectively 3PMo 12O 40/ TiO 2, the catalyzer H for preparing under embodiment 2 conditions 4SiMo 12O 40/ TiO 2, the catalyzer H for preparing under embodiment 3 conditions 3PW 12O 40/ TiO 2, the catalyzer H for preparing under embodiment 4 conditions 4SiW 12O 40/ TiO 2Each 60mg, stirring reaction 1h, the last deionized water that adds 10mL in each test tube stops reaction.Reaction solution is carried out centrifugal, measures the volume of supernatant liquor, obtain the concentration of product 5 hydroxymethyl furfural again with the uv-spectrophotometric external standard method, the yield such as the table 6 that draw:
The pairing yield of table 6 different catalysts
Implementation sequence number Catalyzer Yield (%)
29 H 3PMo 12O 4O/TiO 2 80
30 H 4SiMo 12O 4O/TiO 2 79
31 H 3PW 12O 4O/TiO 2 82
32 H 4SiW 12O 40/TiO 2 76

Claims (10)

1. one kind prepares the method for 5 hydroxymethyl furfural by fructose, may further comprise the steps:
With the N,N-dimethylacetamide is solvent, and lithium chloride is an additive, and fructose is reaction raw materials, and the heteropolyacid of titanium dichloride load is a catalyzer, generates 5 hydroxymethyl furfural 80 ℃~150 ℃ reactions.
2. according to claim 1ly prepare the method for 5 hydroxymethyl furfural, it is characterized in that the quality of described lithium chloride is 5%~25% of a solvent quality by fructose.
3. according to claim 2ly prepare the method for 5 hydroxymethyl furfural, it is characterized in that the quality of described lithium chloride is 15%~25% of a solvent quality by fructose.
4. according to claim 1ly prepare the method for 5 hydroxymethyl furfural, it is characterized in that the quality of described fructose is 5%~35% of a solvent quality by fructose; The quality of described catalyzer is 2%~15% of a solvent quality.
5. according to claim 4ly prepare the method for 5 hydroxymethyl furfural, it is characterized in that the quality of described fructose is 5%~25% of a solvent quality by fructose.
6. describedly prepare the method for 5 hydroxymethyl furfural according to claim 1 or 4, it is characterized in that by fructose, in the described catalyzer mass ratio of titanium dioxide and heteropolyacid be 1: 1~6.
7. according to claim 6ly prepare the method for 5 hydroxymethyl furfural, it is characterized in that the mass ratio of titanium dioxide and heteropolyacid is 1: 2 in the described catalyzer by fructose.
8. according to claim 1ly prepare the method for 5 hydroxymethyl furfural, it is characterized in that described heteropolyacid is one or more in phospho-molybdic acid, phospho-wolframic acid, silicotungstic acid, the silicomolybdic acid by fructose.
9. according to claim 1ly prepare the method for 5 hydroxymethyl furfural, it is characterized in that described temperature of reaction is 120 ℃~140 ℃ by fructose.
10. according to claim 1ly prepare the method for 5 hydroxymethyl furfural, it is characterized in that the described reaction times is 10min~300min by fructose.
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CN103113326A (en) * 2013-01-24 2013-05-22 西北师范大学 Preparation method of 5-hydroxymethylfurfural
CN103694203A (en) * 2013-12-24 2014-04-02 华南理工大学 Method of catalyzing fructose by cellulose base sulfonic acid catalyst to prepare 5-hydroxymethyl furfural
CN103788033A (en) * 2012-11-05 2014-05-14 中国科学院大连化学物理研究所 Method for preparing 5-hydroxymethyl furfural through dehydration of fructose
CN104072450A (en) * 2014-07-14 2014-10-01 南京林业大学 Novel method for preparing 5-hydroxymethylfurfural and furfural by adopting biomass raw material
CN104817524A (en) * 2015-04-07 2015-08-05 中南民族大学 Method for preparing 5-hydroxymethyl furoic acid through catalytic conversion on fructose
CN105418561A (en) * 2015-12-07 2016-03-23 南京工业大学 Method for preparing 2,5-furandicarboxylic acid by supported bifunctional catalyst by catalyzing fructose
CN106699703A (en) * 2017-01-06 2017-05-24 吉林大学 Method for preparing 5-hydroxymethylfurfural through catalyzing biomass sugar by zirconium phosphate-supported titanium dioxide
CN107185510A (en) * 2016-12-22 2017-09-22 青岛大学 It is catalyzed the preparation of the titanate radical nanopipe of fructose dehydration 5 hydroxymethylfurfurals of generation
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CN111295377A (en) * 2017-09-28 2020-06-16 Ifp 新能源公司 Method for producing 5-hydroxymethylfurfural in the presence of an inorganic dehydration catalyst and a chloride source
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CN103113326B (en) * 2013-01-24 2016-04-13 西北师范大学 A kind of preparation method of 5 hydroxymethyl furfural
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CN104817524B (en) * 2015-04-07 2017-03-08 中南民族大学 A kind of method that catalyzed conversion fructose prepares 5 methylol furancarboxylic acids
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CN106699703B (en) * 2017-01-06 2020-09-29 吉林大学 Method for preparing 5-hydroxymethylfurfural by catalyzing biomass sugar with zirconium phosphate loaded titanium dioxide
CN111295377A (en) * 2017-09-28 2020-06-16 Ifp 新能源公司 Method for producing 5-hydroxymethylfurfural in the presence of an inorganic dehydration catalyst and a chloride source
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