CN101514349B - Method for preparing fuel ethanol from bamboo fibers - Google Patents

Method for preparing fuel ethanol from bamboo fibers Download PDF

Info

Publication number
CN101514349B
CN101514349B CN200810080614XA CN200810080614A CN101514349B CN 101514349 B CN101514349 B CN 101514349B CN 200810080614X A CN200810080614X A CN 200810080614XA CN 200810080614 A CN200810080614 A CN 200810080614A CN 101514349 B CN101514349 B CN 101514349B
Authority
CN
China
Prior art keywords
hydrolysis
bamboo
acid
organic acid
liquid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN200810080614XA
Other languages
Chinese (zh)
Other versions
CN101514349A (en
Inventor
张金萍
周本智
王敬文
杜孟浩
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Research Institute of Subtropical Forestry of Chinese Academy of Forestry
Original Assignee
Research Institute of Subtropical Forestry of Chinese Academy of Forestry
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Research Institute of Subtropical Forestry of Chinese Academy of Forestry filed Critical Research Institute of Subtropical Forestry of Chinese Academy of Forestry
Priority to CN200810080614XA priority Critical patent/CN101514349B/en
Publication of CN101514349A publication Critical patent/CN101514349A/en
Application granted granted Critical
Publication of CN101514349B publication Critical patent/CN101514349B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Abstract

The invention discloses a method for preparing fuel ethanol from bamboo fibers. The method comprises the following steps that: waste from bamboo (or other non-wood biomass) processing is used as a raw material, the raw material is cut, dried, crushed and passed through a 80-mesh sieve, the powder passing through the 80-mesh sieve is fine bamboo powder and the powder failing to pass through the 80-mesh sieve is coarse bamboo powder; the coarse bamboo powder is cooked in a mixed liquid of formic acid, acetic acid and water for hydrolyzing hemicellulose and delignification, and fibers are obtained and subjected to hydrolysis by an organic acid to form a reducing monosaccharide; the fine bamboo powder is hydrolyzed directly by the organic acid to form the reducing monosaccharide; the reducing monosaccharide obtained from the hydrolysis of the hemicelluloses, the fibers and the fine bamboo powder are detoxicated by an excess amount of Ca(OH)2, the pH of the mixture is reduced, and the fuel ethanol is obtained after fermentation and rectification. The method for producing the fuel ethanol ensures the yield of the fuel ethanol, reduces the energy consumption for hydrolysis, and allows the organic acid used for hydrolysis to be recycled. In addition, the process of the fuel ethanol preparation using the method requires less water, and reduces environmental pollution and cost.

Description

A kind of method for preparing alcohol fuel by bamboo fiber
Technical field
The present invention relates to a kind ofly prepare the method for alcohol fuel by bamboo fiber, promptly is raw material with the bamboo wood, obtains reducing sugar with organic acid hydrolysis bamboo fibers, and the reducing sugar of gained is fermented obtains alcohol fuel again.Wherein, used organic acid can be recycled.
Technical background
Along with the increase of world population and the raising of various countries' industrialization degree, the energy and environmental problem have become the focus that the whole world is paid close attention to.Fossil energy materials such as oil, coal and Sweet natural gas are petered out; Be protection environment and the target that realizes human kind sustainable development, from renewable resources particularly Wooden Biomass production chemical products with high added-value become the important development strategy of many countries and the hot fields of scientific research.Biomass energy is reproducible clean energy, utilizes biomass to produce Chemicals such as alcohol fuel for the concurrent ferment of raw material hydrolysis and receives extensive concern just day by day.
The technology that employing contains the farm crop preparing ethanol by fermentation of sugar and starch etc. has reached its maturity, and widespread use.Yet along with world population increases, staple food supply is nervous, is that the method for feedstock production alcohol fuel can not be launched on a large scale with food crop, and therefore adopting wood fibre is raw material, and it is significant to produce alcohol fuel through biomass by hydrolyzation.The three big components of forming Wooden Biomass are polymkeric substance such as Mierocrystalline cellulose, semicellulose and lignin, and wherein Mierocrystalline cellulose and semicellulose can be converted into ethanol, and theoretical yield can similar with grain (greater than 400L/t).See that from total amount Mierocrystalline cellulose, semicellulose and lignin are only the resource of renewable biomass the most widely that exists in the world.Bamboo belongs to grass, and Mierocrystalline cellulose and hemicellulose level are higher, and content of lignin is lower, and the phenolic acids secondary substance is also less.China has abundant bamboo plant resource as bamboo kingdom.Bamboo grove distributes extensively, and growth is fast, and it is short to cut down the phase, and output is high, is the important Forest Types of China.Therefore, bamboo can become the high-quality of producing alcohol fuel and abundant desirable feedstock.
Since the seventies in 20th century; The whole world has started the research boom of one cleaning substitute energy; The alcohol fuel that wherein derives from biomass energy with its recyclability, nonstaining property, do not cause Greenhouse effect and improve the characteristics such as explosion-proof performance of automobile and be acknowledged as one of renewable energy source of prospects for commercial application is arranged most, obtained extensive studies.Wood Adhesives from Biomass is that ethanol will be fermentable raw material-reducing sugar with Wood Adhesives from Biomass at first.Main at present mineral acid (rare or dense) and the enzymic hydrolysis filamentary material of adopting produces reducing sugar.
1. acid-hydrolysis method
Acid hydrolysis can be divided into dilute acid hydrolysis and concentrated acid hydrolysis, and dilute acid hydrolysis is a five-carbon sugar with hydrolysis of hemicellulose earlier usually at a lower temperature, and then adds acid hydrolysis residual solids under comparatively high temps, obtains hydrolysate glucose.The transformation efficiency of dilute acid hydrolysis sugar has only 50%, and has more depolymerization product can stop yeast fermentation to generate ethanol.Vitriol oil hydrolysis has 90% Mierocrystalline cellulose and semicellulose to be converted into fermentable sugars approximately, but the acid in the hydrolysis is difficult to reclaim, with in the lime with a large amount of gypsum of back generation, its value is very low.
2. enzyme hydrolysis method
Enzymic hydrolysis is a biochemical reaction, and biological material is put into hydrolysis reactor through after the pre-treatment, adds cellulase.Katalysis through cellulase is cellulose hydrolysis the monose that can ferment.This hydrolytic process reaction conditions is gentle, does not generate poisonous degraded product.But because the cost of production of cellulose enzyme is high at present, hydrolysis time is long, and productive rate relies on effects of pretreatment, equipment that pre-treatment need be bigger and higher running cost to a great extent.
Summary of the invention
The object of the present invention is to provide a kind of is the method for feedstock production alcohol fuel with the bamboo wood, and promptly with organic acid hydrolysis bamboo fine powder (or organic acid handled bamboo meal) preparation reducing sugar, the hydrolyzed solution that ferments then obtains alcohol fuel.
Conception of the present invention
The biomass by hydrolyzation process be exactly semicellulose and cellulose degradation be the process of pentose and glucose.But under hot conditions, pentose and glucose are also unstable, can further be degraded to by products such as furfural and hydroxymethylfurfural, to follow-up microbial fermentation deleterious impact.Therefore, hydrolytic process should reduce production of by-products as far as possible when improving sugared concentration.
Compare with Mierocrystalline cellulose, the hydrolysis ratio of semicellulose is easier to carry out.When temperature during at 100-105 ℃; Add certain density organic acid boiling, can stripping be enclosed in Mierocrystalline cellulose xylogen on every side, semicellulose is degraded to pentose simultaneously; Pentose and lignin are dissolved in the organic acid soln simultaneously; Thin up, lignin deposition leach, and will filtrate must the wood sugar liquid concentrator after concentrating.Isolated solid residue Mierocrystalline cellulose adds catalyzer hydrolysis at normal temperatures with organic acid again after the boiling, distills out organic acid and promptly obtains reducing sugar.Consider factors such as fermentation costs and equipment, pentose is become alcohol fuel with shehatae candida with fermentation by saccharomyces cerevisiae with follow-up cellulose hydrolysis gained reducing sugar.The lignin that reclaims can continue to prepare the chemical of other high added value or act as a fuel burning etc.
The present invention imagination with organic acid formic acid and acetate, is used formic acid when hydrolysis bamboo fine powder and the Mierocrystalline cellulose that prepared by the bamboo meal, and is made catalyzer with hydrochloric acid when boiling bamboo meal.
Technical scheme
1, the present invention is starting material with mao bamboon tankage (also being applicable to other non-timber biomass), and it is blocked, dries, pulverizes, crosses 80 mesh sieves.Through 80 mesh sieves be the bamboo fine powder, what cross 80 mesh sieves is the bamboo meal.
2, the bamboo meal is added in the pulp digester, with the mixed solution (liquid-solid ratio is 10: 1) of formic acid, acetate and water (ratio is 10/70/20) at 100-105 ℃ of following boiling 2h.Hydrolysis of hemicellulose is that wood sugar is dissolved in the acid solution, and lignin also is dissolved in the acid solution, and acid solution thin up lignin deposition is separated out, and gets the pentose liquid concentrator after cooking liquor is concentrated, and the gained solid residue is a cellulose components.
Above-mentioned gained solid residue Mierocrystalline cellulose adds 60 ℃ of hydrolysis 6h of 4% hydrochloric acid with 85% formic acid, and the formic acid underpressure distillation obtains reducing sugar after reclaiming.
3, the bamboo fine powder is added in the hydrolysis reactor, add 85% formic acid and 4% hydrochloric acid at 25: 1 at 60 ℃ of following hydrolysis 6h, after formic acid and salt acid recovery, obtain reducing sugar with liquid-solid ratio.
4, above-mentioned gained reducing sugar is mixed, after the detoxification treatment, with yeast saccharomyces cerevisiae and shehatae candida, 30 ℃ of fermentations 48 hours.
Description of drawings
Fig. 1 bamboo fiber prepares the alcohol fuel schematic flow sheet
The practical implementation method
Through instance the present invention is further specified below, but does not influence protection scope of the present invention:
Embodiment 1
The mao bamboon tankage are blocked, dry, pulverize.Cross 80 mesh sieves, through 80 mesh sieves be the bamboo fine powder, not through the person be the bamboo meal.Take by weighing 400 gram bamboo meal and add in the digestion reactors, with the mixed solution of liquid-solid ratio adding in 10: 1 formic acid/acetic acid/water (10/70/20), 105 ℃ of boiling 2h cross and filter 50.2% filter residue (staple is a Mierocrystalline cellulose); There is deposition to separate out behind the filtrating thin up, crosses and filter 16% xylogen; Test contains 20% piperylene after the concentrating filter liquor.
Embodiment 2
Embodiment 1 gained Mierocrystalline cellulose is added in the hydrolysis reactor, add 85% formic acid and 4% hydrochloric acid at 25: 1 at 60 ℃ of following hydrolysis 6h with liquid-solid ratio, underpressure distillation can obtain 55% reducing sugar after reclaiming formic acid.
Embodiment 3
Bamboo fine powder 400 grams that take by weighing among the embodiment 1 preparation add in the hydrolysis reactors, add 85% formic acid and 4% hydrochloric acid at 25: 1 at 60 ℃ of following hydrolysis 6h with liquid-solid ratio, with after formic acid and the hydrochloric acid underpressure distillation recovery, obtain 72.7% reducing sugar.
Embodiment 4
With embodiment 1,2,3 gained reductive hydrolysis liquid glucoses, with Ca (OH) 2Adjust pH is used H again to 9-10 (excessive alkaline process overliming) 2SO 4Recall to pH5.5.With hydrolysis sugar liquid 150ml after the detoxification treatment and the yeast saccharomyces cerevisiae bacterial classification liquid concentrator 50mL mixed fermentation behind the multiplication culture; Ferment after 48 hours; Fermented liquid is drawn off, the bacterial classification in the reactor drum is kept 50mL as inoculum, in 72 hours, add hydrolyzed solution 400mL continuously.Leavening temperature is 30 ℃, and alcohol yied is 0.40g/g.
The used yeast bacterial classification is yeast saccharomyces cerevisiae (Saccharomyces cerevisiae Meyen et Hansen 2157) and shehatae candida (Candida shehatae) in the zymocyte liquid.
The acclimation method of used bacterial classification is following:
Substratum (g/L): peptone 3, yeast extract paste 2.5, MgSO 40.25, KH 2PO 42.5, CaCl 20.25, glucose 15.00,121 ℃ of sterilizations of pH5.0-5.5. substratum 20 minutes.
The enrichment culture of bacterial classification: with the bacterial classification inoculation of preservation in the 100mL liquid nutrient medium, 30 ℃, 80rpm activation 24h.Change fresh culture then into, breed 48h down in similarity condition.

Claims (3)

1. one kind is the method that the hydrolysis of raw material organic acid prepares alcohol fuel with the bamboo wood, it is characterized in that, comprises the steps:
A, be starting material, it blocked, dry, pulverize, cross 80 mesh sieves with the mao bamboon tankage, through 80 mesh sieves be the bamboo fine powder, mistake 80 mesh sieves is the bamboo meal;
B, boiling bamboo meal, are removed lignin at hydrolyzed hemicellulose, isolate Mierocrystalline cellulose: with the bamboo meal with formic acid/acetic acid/water mixed solution in 100-105 ℃ of boiling 2h; Remaining residue is a Mierocrystalline cellulose after the boiling, adds entry in the filtrating lignin deposition is leached, and hydrolysis of hemicellulose is that pentose is dissolved in the acid solution, after evaporation concentration, obtains the pentose liquid concentrator;
C, organic acid hydrolysis de-fibering element: the formic acid with 85% adds hydrochloric acid and makes catalyzer, the Mierocrystalline cellulose of hydrolysing step b preparation, and liquid-solid ratio 25: 1, at 60 ℃ of hydrolysis 6h, underpressure distillation Separation and Recovery formic acid obtains the reductibility liquid glucose;
D, organic acid hydrolysis bamboo fine powder: the bamboo fine powder is added hydrochloric acid with 85% formic acid make catalyzer, liquid-solid ratio 25: 1, at 60 ℃ of hydrolysis 6h, underpressure distillation Separation and Recovery formic acid obtains the reductibility liquid glucose;
E, with step b, c, d hydrolysis gained liquid glucose detoxification secondary fermentation.
According to claim 1 said a kind of be the method that the hydrolysis of raw material organic acid prepares alcohol fuel with the bamboo wood, it is characterized in that among the said step e, the detoxification process is with excessive Ca (OH) 2Adjust pH is used H again to 9-10 2SO 4Recall to pH5.5.
According to claim 2 said a kind of be the method that the hydrolysis of raw material organic acid prepares alcohol fuel with the bamboo wood, it is characterized in that, after the step e adjust pH; With liquid glucose 150ml after the detoxification treatment and the yeast saccharomyces cerevisiae bacterial classification liquid concentrator 50mL mixed fermentation behind the multiplication culture;, after 48 hours fermented liquid is drawn off 30 ℃ of fermentations, the bacterial classification in the reactor drum is kept 50mL as inoculum; Liquid glucose 400mL in 72 hours after the continuous adding detoxification treatment; Obtain tunning, carry out rectifying, collect ethanol wherein.
CN200810080614XA 2008-02-21 2008-02-21 Method for preparing fuel ethanol from bamboo fibers Expired - Fee Related CN101514349B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200810080614XA CN101514349B (en) 2008-02-21 2008-02-21 Method for preparing fuel ethanol from bamboo fibers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200810080614XA CN101514349B (en) 2008-02-21 2008-02-21 Method for preparing fuel ethanol from bamboo fibers

Publications (2)

Publication Number Publication Date
CN101514349A CN101514349A (en) 2009-08-26
CN101514349B true CN101514349B (en) 2012-01-04

Family

ID=41038972

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200810080614XA Expired - Fee Related CN101514349B (en) 2008-02-21 2008-02-21 Method for preparing fuel ethanol from bamboo fibers

Country Status (1)

Country Link
CN (1) CN101514349B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9303226B2 (en) 2009-12-31 2016-04-05 Shell Oil Company Direct aqueous phase reforming of bio-based feedstocks

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101693905B (en) * 2009-10-27 2011-09-07 哈尔滨工业大学 Improved method of excess calcium hydrate detoxification during cellulose ethanol production
CN101857885B (en) * 2010-05-28 2013-10-09 农业部沼气科学研究所 Process for producing fuel ethanol by utilizing bamboo biomass waste
EP2588619A1 (en) * 2010-06-30 2013-05-08 Earnest Stuart Universal biomass refinery
CN102660882B (en) * 2012-05-17 2015-01-28 刘德江 Method for producing cellulose and fuel ethanol by dissolving plant straw with solvent
US9695484B2 (en) 2012-09-28 2017-07-04 Industrial Technology Research Institute Sugar products and fabrication method thereof
CN103061179B (en) * 2012-12-25 2015-06-17 济南圣泉集团股份有限公司 Comprehensive utilization process for lignocellulose biomass
CN103102334B (en) * 2012-12-25 2014-11-19 济南圣泉集团股份有限公司 Process for producing furfural from biomass raw material
CN103898787B (en) * 2012-12-25 2016-06-15 济南圣泉集团股份有限公司 A kind of comprehensive utilization process of biomass material
CN103966367B (en) 2013-02-01 2016-01-20 财团法人工业技术研究院 Process for the preparation of saccharides
CN103352057B (en) * 2013-07-12 2015-06-10 浙江农林大学 Method for preparing fuel ethanol by taking bamboo shoot processing residues as raw materials
CN103910766A (en) * 2014-02-25 2014-07-09 北京林业大学 Preparation method for poplar acetic acid lignin through separation and purification
CN104450830A (en) * 2015-01-04 2015-03-25 南京林业大学 Method for producing multiple kinds of monosaccharide through bamboo processing residues
CN109337936A (en) * 2018-10-30 2019-02-15 孙金良 Association fibre element Ethanol Method
CN111269947A (en) * 2020-03-11 2020-06-12 吉林大学 Method for detoxifying acid hydrolysis liquid and preparing cellulosic ethanol
CN112458127B (en) * 2020-12-04 2022-12-30 浙江华康药业股份有限公司 Method for improving high-solid-state enzymolysis rate of biomass

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101016703A (en) * 2007-03-08 2007-08-15 上海交通大学 Method of producing cellulose, lignin and xylose by biomass material
AU2006285712B2 (en) * 2005-08-31 2009-11-12 Mie University Method of producing saccharide composition starting with biomass

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2006285712B2 (en) * 2005-08-31 2009-11-12 Mie University Method of producing saccharide composition starting with biomass
CN101016703A (en) * 2007-03-08 2007-08-15 上海交通大学 Method of producing cellulose, lignin and xylose by biomass material

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
许凤.有机溶剂制浆技术研究进展.《中国造纸学报》.2004,第19卷(第2期),全文. *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9303226B2 (en) 2009-12-31 2016-04-05 Shell Oil Company Direct aqueous phase reforming of bio-based feedstocks
US9447349B2 (en) 2009-12-31 2016-09-20 Shell Oil Company Direct aqueous phase reforming of bio-based feedstocks

Also Published As

Publication number Publication date
CN101514349A (en) 2009-08-26

Similar Documents

Publication Publication Date Title
CN101514349B (en) Method for preparing fuel ethanol from bamboo fibers
Ayodele et al. An overview of integration opportunities for sustainable bioethanol production from first-and second-generation sugar-based feedstocks
Sindhu et al. Water hyacinth a potential source for value addition: an overview
CN101434913B (en) Wine brewing yeast strain and method for producing ethanol by efficient stalk fermentation
CA2567824C (en) Process for producing ethanol
CN102154381B (en) Method for joint production of ethanol and microbial lipid by using methyl cellulose as raw material
CN101784668B (en) Concurrent saccharification and fermentation of fibrous biomass
CN104774876B (en) A kind of method of lignocellulose biomass comprehensive utilization
CN101220379B (en) Method for producing ethyl alcohol by using sorgo stalk
CN102251010B (en) Method for producing ethanol by high-efficiency simultaneous saccharification and cofermentation
CN104774877A (en) Method for co-producing ethanol, acetone and butanol by lignocellulose biomass
CN101497894B (en) Method for preparing ethanol from wood fiber raw material
CN103352057B (en) Method for preparing fuel ethanol by taking bamboo shoot processing residues as raw materials
CN109112172B (en) Method for saccharifying straw through microbial enzymolysis
CN109182418B (en) Method for saccharifying straw through microbial enzymolysis
Manmai et al. Transformation of lignocellulose from corn stove for bioethanol production
CN101497897B (en) Method for preparing ethanol from wood fiber raw material
CN101497896B (en) Method for preparing ethanol from wood fiber raw material
CN109971806A (en) Mix lignocellulose pretreatment method and its zymotechnique
CN112746088B (en) Method for co-producing xylitol and fuel ethanol by fermenting lignocellulose serving as raw material
CN105925622A (en) Method for producing ethanol by utilizing bagasse hemicellulose
Somaprabha et al. Evaluation and production of bioethanol using agricultural waste with banana Pseudostem and peels of pine apple and banana peel
CN101544996A (en) New process of plant material diastatic fermented koji (mycoprotein provender) and alcoholic fermentation production
CN101886092B (en) Method for fermenting cellulosic ethanol by taking DDGS as nutrient
CN110438172B (en) Method for producing grease by co-utilizing starch and lignocellulose raw materials

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120104

Termination date: 20170221