CN1629300A - Process for preparing phenol and toluene from lignin by utilizing straw plants - Google Patents
Process for preparing phenol and toluene from lignin by utilizing straw plants Download PDFInfo
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- CN1629300A CN1629300A CN 200310121807 CN200310121807A CN1629300A CN 1629300 A CN1629300 A CN 1629300A CN 200310121807 CN200310121807 CN 200310121807 CN 200310121807 A CN200310121807 A CN 200310121807A CN 1629300 A CN1629300 A CN 1629300A
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Abstract
The invention provides a process for preparing phenol and toluene from lignin by utilizing straw plants which comprises, at room temperature, mixing stalk plants and thin acid solution by the weight ratio of 1:4.5-8.5, elevating temperature to 90-100 deg. C, keeping constant temperature, quickly dissolving hemicellulose in the stalk, abstracting glucose solution, charging undissolved cellulose in the cellulose hydrolysis glucose solution, obtaining water solution containing glucose and xylose, filtering for separation, thus obtaining nondissolved intermediate lignin for preparing hydroxybenzene and toluene.
Description
Technical field
The invention belongs to and utilize straw to prepare fields such as ethanol, phenol, toluene, specially refer to the method for utilizing the stalk plant to prepare the intermediate xylogen of aromatic compounds such as phenol and toluene.
Background technology
Contain a large amount of xylogen in the plant, in xylogen, all have the basic framework that phenyl-propane is a unit (the 69th page of the vegetable fibre chemistry third edition, China Light Industry Press).Told about chemistry, the physical properties of xylogen in 69 pages～162 pages of this book, xylogen contains functional groups such as a certain amount of phenolic hydroxyl group, methoxyl group.Xylogen and Mierocrystalline cellulose, hemicellulose interweave and are one, and for obtaining xylogen, the scientific worker has adopted different extracting method.
The extraction of xylogen has several different methods, and it is to use maximum a kind of method (xylogen, Chemical Industry Press at present that alkaline process extracts.2001, the third edition, P7), xylogen is that the form with the solubility phenates exists in basic solution, when adding acid, becomes insoluble phenol gradually and separates out from black liquor.Also have the people (PolymerDegradation and Stabitity.Vol.79.2003, P241-251) use organic solvent toluene: ethanol (2: 1) extracts, again with rare NaOH processing, with the acid neutralization, filter the filtrate evaporation, concentrate, precipitation obtains being insoluble to sour xylogen.Have again that (Ultrasonics Sonochemistry Vol.9.2002 P85-93) handles straw with the auxiliary alkaline method of ultrasonic wave, can extract purer xylogen from straw, can change the structure of xylogen hardly.
Summary of the invention
The purpose of this invention is to provide a kind of method of utilizing the stalk plant to prepare aromatic compound intermediate xylogen such as phenol and toluene.
The method of utilizing the straw plant to prepare aromatic compound intermediate xylogen such as phenol and toluene of the present invention may further comprise the steps:
(1) under the room temperature, according to the stalk plant: the weight ratio of dilute acid soln is that 1: 4.5～8.5 ratio is mixed stalk with dilute acid soln, 90～100 ℃ of constant temperature then heat up, hemicellulose in the quick hydrolyzing straw, extract sugar soln (with the straw be example sugar extraction yield be the straw nt wt net weight 15～20%), sugar soln can be used for alcohol prepared by fermenting; Sugar soln is based on wood sugar basically, is outside the main sugar soln extracting wood sugar, and this method also effectively raises the susceptibility of stalk inner cellulose such as straw to cellulase, helps the carrying out of next step;
Described dilute acid solution is the aqueous solution of dilute sulfuric acid aqueous solution, diluted hydrochloric acid aqueous solution or sulfuric acid and mixed in hydrochloric acid.Dilute acid concentration 0.5～1.5wt%.
(2). in the sugar soln of step (1), add not molten Mierocrystalline cellulose in the cellulase hydrolysis sugar soln, wherein, the add-on of cellulase and the weight ratio of stalk are 1: 10～1: 100, with lime carbonate, yellow soda ash, sodium hydroxide or their adjust pHs such as mixture 4.5～5.5, be warmed up to 45～60 ℃ then, can obtain containing the aqueous solution of glucose (2～4%) and wood sugar (2～4%), sugar soln can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
(3) water-insoluble fraction of separating step (2) obtains preparing aromatic compound intermediate xylogen (based on xylogen) such as phenol and toluene after the water-insoluble fraction drying
Stalk of the present invention comprises straw, wheat straw, reed, cornstalk, beanstalk etc.
The method of utilizing the straw plant to prepare aromatic compound intermediate xylogen such as phenol and toluene of the present invention; Have following characteristics:
One. the method for stalks such as dilute acid hydrolysis straw
1. prepare the sugar soln that contains wood sugar and glucose with the hemicellulose in the stalks such as dilute acid hydrolysis straw.
2. with in the stalks such as dilute acid hydrolysis straw hemicellulose the time, improved in the stalks such as straw fiber to the susceptibility of cellulase.
Two. the cellulase hydrolysis of stalk inner cellulose
1. do not need separating of dilute acid hydrolysis solution and Mierocrystalline cellulose, xylogen, directly add the cellulase hydrolysis Mierocrystalline cellulose;
2. earlier dilute acid hydrolysis solution and Mierocrystalline cellulose, lignin separation are come out, utilize the cellulase hydrolysis Mierocrystalline cellulose.
The present invention has not only obtained the sugar soln based on wood sugar, also effectively raises the susceptibility of fiber to cellulase, and 18 hours fiber enzymatic hydrolyzation reaches 75%～85% (the enzymic hydrolysis effect sees Table 1) under the condition of being fit to.
Table 1: straw is residual fiber and Xinhua's filter paper enzymic hydrolysis rate contrast behind dilute acid hydrolysis
| Cellulase | Enzymolysis 1 hour | Enzymolysis 18 hours | |||
| Glucose increment (mg/100ml) | Fiber rate of decomposition (%) | Glucose increment (mg/100ml) | Fiber rate of decomposition (%) | ||
| Straw after the hydrolysis | 1# | ??112.5 | ??21.6 | ??442.5 | ??85.1 |
| Xinhua's filter paper | 1# | ??107.5 | ??20.6 | ??445.5 | ??85.3 |
| Straw after the hydrolysis | 2# | ??97.5 | ??18.8 | ??445.0 | ??85.5 |
| Xinhua's filter paper | 2# | ??80.0 | ??15.4 | ??450.5 | ??86.0 |
| Straw after the hydrolysis | 3# | ??37.5 | ??7.2 | ??172.5 | ??33.2 |
| Xinhua's filter paper | 3# | ??32.5 | ??6.3 | ??130.0 | ??25.0 |
No. 1 Amresco company of cellulase provides
No. 2 Physical Chemistry Technology Inst., Chinese Academy of Sciences of cellulase provide
The zymin company of No. 3 Beijing U.S.s of cellulase provides
Three. be used to prepare the preparation of aromatic compound intermediate xylogen such as phenol and toluene as above-mentioned " one and two " are described, the xylogen that utilizes stalk to prepare aromatic compound intermediates such as phenol, toluene is first with the hydrolysis of hemicellulose in the stalk, the Mierocrystalline cellulose in the plain enzymic hydrolysis stalk of reprocess fibre; Filter to isolate water-insoluble xylogen at last.The characteristics of this method are that the extraction of xylogen is based upon and does not change basically on chemistry of lignin's architecture basics.
As can be seen, significantly expose out on the metamorphosis accompanying drawing before and after handling from example straw that the present invention lifted through the rice-straw fibre of art breading of the present invention, and by swelling.
Description of drawings
Figure 1A. the embodiment of the invention 8 straw stalks are handled preceding 400 times of amplification metamorphosis figure;
Figure 1B. the embodiment of the invention 8 straw stalks are handled back 400 times of amplification metamorphosis figure;
Fig. 2 A. embodiment of the invention 8 straw stalks are handled preceding 1000 times of amplification metamorphosis figure;
Fig. 2 B. embodiment of the invention 8 straw stalks are handled back 1000 times of amplification metamorphosis figure.
Embodiment
Embodiment 1
In the flask of getting ready, add entry 600g, H
2SO
46g and straw 80g (moisture 10%, below identical) are warmed up to 90～100 ℃ of constant temperature 1 hour then; The sugar aqueous solution that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 2
In the flask of getting ready, add entry 600g, H
2SO
45g, HCl 1g and straw 80g are warmed up to 90～100 ℃ of constant temperature 1 hour then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 3
In the flask of getting ready, add entry 600g, H
2SO
44g, HCl 2g and straw 80g are warmed up to 90～100 ℃ of constant temperature 1 hour then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 4
In the flask of getting ready, add entry 500g, HCl 5g and straw 80g, be warmed up to 90～100 ℃ of constant temperature 2 hours then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 5
In the flask of getting ready, add entry 500g, H
2SO
44g, HCl 1g and straw 80g are warmed up to 90～100 ℃ of constant temperature 3 hours then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 6
In the flask of getting ready, add entry 400g, H
2SO
45g and straw 80g are warmed up to 90～100 ℃ of constant temperature 3 hours then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 7
In the flask of getting ready, add entry 400g, H
2SO
44g, HCl 1g and straw 80g are warmed up to 90～100 ℃ of constant temperature 1 hour then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 8
In the flask of getting ready, add entry 400g, H
2SO
44g, HCl 1g and straw 80g are warmed up to 90～100 ℃ of constant temperature 4 hours then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 9
In the flask of getting ready, add entry 400g, H
2SO
44g, HCl 1g and straw 80g are warmed up to 96 ℃ of constant temperature 4 hours then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 10
In the flask of getting ready, add entry 450g, H
2SO
41.8g, HCl 0.2g and wheat straw 80g, be warmed up to 90 ℃～95 ℃ constant temperature 4 hours then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 11
In the flask of getting ready, add entry 450g, H
2SO
41.8g, HCl 1.2g and reed 80g, be warmed up to 90 ℃～95 ℃ constant temperature 3.5 hours then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 12
In the flask of getting ready, add entry 400g, H
2SO
44g, HCl 2g and corn stalk 85g are warmed up to 96 ℃ of constant temperature 4 hours then; The sugar soln that obtains can be used for alcohol prepared by fermenting, and water-insoluble fraction is used to prepare xylogen.
Embodiment 13
Isolate not molten Mierocrystalline cellulose, xylogen and other water-insoluble fraction among the embodiment 1, add entry 600g, it is 4.5～5.5 that yellow soda ash, sodium hydroxide are transferred pH, adds cellulase 1
#4g is warmed up to 45～46 ℃ of enzymolysis 40 hours then; Water-insoluble fraction is leached drying obtain xylogen 8g.
Embodiment 14
Add cellulase 2 in the sugar soln in embodiment 2
#2g, it is 4.5～5.5 that adding yellow soda ash, lime carbonate, sodium hydroxide are transferred pH, is warmed up to 50 ℃ of enzymolysis 70 hours then; Water-insoluble fraction is leached drying obtain xylogen 9g.
Embodiment 15
Embodiment 3 sugar soln in add yellow soda ash, lime carbonate, sodium hydroxide and transfer pH=4.5～5.5, add cellulase 2 again
#5g is warmed up to 55～60 ℃ of enzymolysis 60 hours then.Water-insoluble fraction is leached drying obtain xylogen 10g.
Embodiment 16
Isolate not molten Mierocrystalline cellulose, xylogen and other water-insoluble fraction among the embodiment 4, add 400ml water, transferring pH with yellow soda ash, lime carbonate is 4.5～5.5, adds cellulase 2
#5g is warmed up to 45～50 ℃ of enzymolysis 48 hours then.Water-insoluble fraction is leached drying obtain xylogen 10g.
Embodiment 17
Add cellulase 2 in the sugar soln in embodiment 5
#6g, it is 4.5～5.5 that adding yellow soda ash, lime carbonate, sodium hydroxide are transferred pH, is warmed up to 50 ℃ of enzymolysis 46 hours then; Water-insoluble fraction is leached drying obtain xylogen 9.5g.
Embodiment 18
Add cellulase 2 in the sugar soln in embodiment 6
#8g, it is 4.5～5.5 that adding yellow soda ash, lime carbonate, sodium hydroxide are transferred pH, is warmed up to 50 ℃ of enzymolysis 46 hours then; Water-insoluble fraction is leached drying obtain xylogen 9.6g.
Embodiment 19
Add cellulase 2 in the sugar soln in embodiment 7
#6g, it is 4.5～5.5 that adding yellow soda ash, lime carbonate, sodium hydroxide are transferred pH, is warmed up to 50 ℃ of enzymolysis 46 hours then; Water-insoluble fraction is leached drying obtain xylogen 9.2g.
Embodiment 20
Add cellulase 2 in the sugar soln in embodiment 8
#6g, it is 4.5～5.5 that adding yellow soda ash, lime carbonate, sodium hydroxide are transferred pH, is warmed up to 50 ℃ of enzymolysis 90 hours then; Water-insoluble fraction is leached drying obtain xylogen 9g.
Embodiment 21
Add cellulase 2 in the sugar soln in embodiment 9
#7g, it is 4.5～5.5 that adding yellow soda ash, lime carbonate, sodium hydroxide are transferred pH, is warmed up to 50 ℃ of enzymolysis 46 hours then; Water-insoluble fraction is leached drying obtain xylogen 8.5g.
Embodiment 22
Add cellulase 2 in the sugar soln in embodiment 10
#6g, it is 4.5～5.5 that adding yellow soda ash, lime carbonate, sodium hydroxide are transferred pH, is warmed up to 50 ℃ of enzymolysis 46 hours then; Water-insoluble fraction is leached drying obtain xylogen 19g.
Embodiment 23
Add cellulase 2 in the sugar soln in embodiment 11
#6g, it is 4.5～5.5 that adding yellow soda ash, lime carbonate, sodium hydroxide are transferred pH, is warmed up to 50 ℃ of enzymolysis 46 hours then; Water-insoluble fraction is leached drying obtain xylogen 20g.
Embodiment 24
Add cellulase 2 in the sugar soln in embodiment 12
#6g, it is 4.5～5.5 that adding yellow soda ash, lime carbonate, sodium hydroxide are transferred pH, is warmed up to 50 ℃ of enzymolysis 60 hours then; Water-insoluble fraction is leached drying obtain xylogen 20g.
Claims (4)
1. method of utilizing the straw plant to prepare phenol and toluene intermediate xylogen, it is characterized in that: described method may further comprise the steps:
(1) under the room temperature, according to the stalk plant: the weight ratio of dilute acid soln is that 1: 4.5～8.5 ratio is mixed stalk with dilute acid soln, 90～100 ℃ of constant temperature that heat up then, and the hemicellulose in the hydrolyzing straw extracts sugar soln fast;
(2). in the sugar soln of step (1), add not molten Mierocrystalline cellulose in the cellulase hydrolysis sugar soln, wherein, the add-on of cellulase and the weight ratio of stalk are 1: 10～1: 100, and adjust pH is 4.5～5.5, be warmed up to 45～60 ℃ then, obtain containing the aqueous solution of glucose and wood sugar;
(3) water-insoluble fraction of separating step (2) obtains preparing phenol and toluene intermediate xylogen after the water-insoluble fraction drying.
2. the method for claim 1, it is characterized in that: described dilute acid soln is the aqueous solution of dilute sulfuric acid aqueous solution, diluted hydrochloric acid aqueous solution or sulfuric acid and mixed in hydrochloric acid.
3. method as claimed in claim 1 or 2 is characterized in that: described dilute acid concentration 0.5～1.5wt%.
4. the method for claim 1 is characterized in that: described adjust pH is with yellow soda ash, lime carbonate, sodium hydroxide or their mixture.
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| CN1264985C CN1264985C (en) | 2006-07-19 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007095787A1 (en) * | 2006-02-27 | 2007-08-30 | Pficker Pharmaceuticals Ltd. | Novel method for production liquid fuel from biomass |
| CN102585247A (en) * | 2012-01-12 | 2012-07-18 | 安徽丰原发酵技术工程研究有限公司 | Method for preparing lignin sulfonate by utilizing residue from enzymatic hydrolysis of lignocellulose |
| US8618341B2 (en) | 2007-02-01 | 2013-12-31 | China Fuel (Huaibei) Bioenergy Technology Development Co. Ltd | Process of producing liquid fuel from cellulosic biomass |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100465373C (en) * | 2007-03-08 | 2009-03-04 | 上海交通大学 | Method of producing cellulose, lignin and xylose by biomass material |
| TWI422563B (en) | 2011-12-13 | 2014-01-11 | Ind Tech Res Inst | Method for preparing phenol compounds |
-
2003
- 2003-12-18 CN CN 200310121807 patent/CN1264985C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007095787A1 (en) * | 2006-02-27 | 2007-08-30 | Pficker Pharmaceuticals Ltd. | Novel method for production liquid fuel from biomass |
| JP2009528035A (en) * | 2006-02-27 | 2009-08-06 | 淮北市輝克薬業有限公司 | Production method of liquid fuel with new biomass |
| US8618341B2 (en) | 2007-02-01 | 2013-12-31 | China Fuel (Huaibei) Bioenergy Technology Development Co. Ltd | Process of producing liquid fuel from cellulosic biomass |
| CN102585247A (en) * | 2012-01-12 | 2012-07-18 | 安徽丰原发酵技术工程研究有限公司 | Method for preparing lignin sulfonate by utilizing residue from enzymatic hydrolysis of lignocellulose |
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