CN106834361A - The method that stalk produces cellulosic ethanol - Google Patents
The method that stalk produces cellulosic ethanol Download PDFInfo
- Publication number
- CN106834361A CN106834361A CN201710181164.2A CN201710181164A CN106834361A CN 106834361 A CN106834361 A CN 106834361A CN 201710181164 A CN201710181164 A CN 201710181164A CN 106834361 A CN106834361 A CN 106834361A
- Authority
- CN
- China
- Prior art keywords
- fermentation
- stalk
- cellulosic ethanol
- yeast
- treatment
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/02—Preparation of oxygen-containing organic compounds containing a hydroxy group
- C12P7/04—Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
- C12P7/06—Ethanol, i.e. non-beverage
- C12P7/08—Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate
- C12P7/10—Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate substrate containing cellulosic material
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12F—RECOVERY OF BY-PRODUCTS OF FERMENTED SOLUTIONS; DENATURED ALCOHOL; PREPARATION THEREOF
- C12F3/00—Recovery of by-products
- C12F3/02—Recovery of by-products of carbon dioxide
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
- C12N1/14—Fungi; Culture media therefor
- C12N1/16—Yeasts; Culture media therefor
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/14—Preparation of compounds containing saccharide radicals produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase, e.g. by cellulase, hemicellulase
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P2201/00—Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Health & Medical Sciences (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Genetics & Genomics (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Mycology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Medicinal Chemistry (AREA)
- Tropical Medicine & Parasitology (AREA)
- Virology (AREA)
- Biomedical Technology (AREA)
- Botany (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
A kind of method that stalk produces cellulosic ethanol.Existing cellulosic ethanol production technique is mainly the agricultural wastes such as stalk and is crushed, raw material is pre-processed into pretreatment unit after crushing, material is digested into enzymolysis device after pretreatment, enzymolysis mixed liquor carries out separation of solid and liquid into separator, enzymolysis liquid glucose is proportionally added into zymophyte and is fermented into fermentation tank, and zymotic fluid obtains cellulosic ethanol through distilling apparatus separating-purifying.A kind of method that stalk produces cellulosic ethanol, comprises the following steps：（1）The treatment of stalk early stage and thermal and hydric environment pretreatment；（2）Batch mixing and enzymatic saccharification are processed；（3）Fermentation purification processes；（4）Ferment the CO for producing2Treatment；（5）The useless wine with dregs treatment of distillation；（6）Yeast fermentation after fermentation mash separating thallus albumen.The present application relates to biorefinery field, stalk production cellulosic ethanol and five kinds of methods of byproduct are more particularly to applied to.
Description
Technical field：
The present invention relates to biorefinery field, more particularly to a kind of stalk production cellulosic ethanol and five kinds of methods of byproduct.
Background technology：
The exploitation of new energy is to solve China's energy wilderness demand main method for lacking present situation relative with the energy, is also to solve ring
The only way which must be passed of border problem, new energy has the advantages that high efficiency, low stain and sustainability, mainly including nuclear energy, wind energy, water
Energy, solar energy and biomass energy etc., wherein biomass energy are even more a kind of unique reproducible carbon source, can change into conventional consolidating
State, liquid or gaseous fuel；By agricultural wastes carry out recycling treatment production biomass energy, can not only become give up into
Treasured, can reduce pollutant emission, environmental protection again, due to the structural complexity and the efficient fiber of shortage of natural cellulosic feedstocks
Plain enzyme preparation so that current cellulosic ethanol production enterprise's production capacity is higher, single production cellulosic ethanol product is difficult to reality
Now profit turns into the bottleneck of industry development；Existing cellulosic ethanol production technique is mainly the agricultural wastes such as stalk carries out powder
Broken, raw material is pre-processed into pretreatment unit after crushing, and material is digested into enzymolysis device after pretreatment, and enzymolysis is mixed
Close liquid carries out separation of solid and liquid into separator, and enzymolysis liquid glucose is proportionally added into zymophyte and is fermented, ferments into fermentation tank
Liquid obtains cellulosic ethanol through distilling apparatus separating-purifying, and the solid slag of separation is burnt as fuel；And prior art
The product variety of scheme production is single, and production cost is higher；Raw materials for production need to carry out pulverization process；Enzymolysis liquid need to carry out solid-liquid point
From so that Partial digestion liquid glucose loses, and also increases technological process of production complexity；Enzymolysis slag charge carries out burning reduction product and adds
Value, is not implemented making full use of for raw material full constituent.
The content of the invention：
Cellulosic ethanol is produced using stalk it is an object of the invention to provide one kind, and obtains five kinds of methods of byproduct simultaneously.
Above-mentioned purpose is realized by following technical scheme：
The method that stalk produces cellulosic ethanol, comprises the following steps：（1）The treatment of stalk early stage and thermal and hydric environment pretreatment；（2）
Batch mixing and enzymatic saccharification are processed；（3）Fermentation purification processes；（4）Ferment the CO for producing2Treatment；（5）The useless wine with dregs treatment of distillation；（6）Ferment
Mother's fermentation after fermentation mash separating thallus albumen, described fermentation purification processes process is：After through enzymolysis, liquid glucose is cooled to 32
20% yeast is accessed after DEG C carries out alcoholic fermentation, and fermentation time 70h carries out temperature control, hair is taken away using frozen water in fermentation process
The fermentation fever that ferment is produced, control fermentation temperature is in 30-35 DEG C, residual sugar<0.3% is considered as fermentation ends, terminates the alcohol hair of fermentation
Ferment mash delivers to distilling apparatus and carries out distilation and obtain cellulosic ethanol after precipitating 48h yeast separations, and distillation is using double
Thick column differential-pressure distillation device carries out distillation procedure, and operation temperature is 103-108 DEG C of thick tower, 0.06-0.15mpa of tower top pressure,
85-95 DEG C of combined column temperature, tower top pressure-0.05-- 0.08mpa；Smart 120-128 DEG C of tower temperature degree, tower top pressure 0.06-
0.15mpa。
The method that described stalk produces cellulosic ethanol, described stalk early stage treatment and thermal and hydric environment preprocessing process
For：Enter alcohol production device after maize straw is collected into bundling, stacking storage, conveying crushing, dedusting removal of impurities, drying, briquetting
Area, the briquetting stalk of 15% moisture delivers to hot water environment after Water spray pre-soaking, washing after moisture reaches 60% in device area
In formula plug flow reactor, 1.3-1.8mpa steam is passed through in the reactor, ton stalk needs 0.2-0.5t of steam, stop
12-15min is reacted.
The method that described stalk produces cellulosic ethanol, described batch mixing and enzymatic saccharification processing procedure be：Through hydro-thermal
Stalk material delivers to enzymatic vessel by blender after environmental treatment, added in blender liquid NaOH regulation PH to 4.8-
5.0,2-5kg/ tons of stalk of liquid NaOH additions, cellulase 10kg/t stalks carry out enzymatic saccharification, controlled enzymatic hydrolysis temperature 50-
55℃。
A kind of carbon dioxide of the method by-product of described stalk production cellulosic ethanol, the CO that described fermentation is produced2
Processing procedure is：Ferment the CO for producing2Dissolved organic matter gas is removed by Water spray washing, the CO2 gases warp after purification
0.06% liquor potassic permanganate carries out spray washing and removes insoluble grease, and first point of water is crossed by the gas after two-step purification
Boosted into carbon-dioxide gas compressor after tank point water, after boosting to 3.0MPa, proceeding through the first cooler, second point of water
Tank and drying bed are further dehydrated, and the CO2 after dehydration enters adsorbent bed after the second cooler is cooled down, and carries out at removing impurities matter
Reason, adsorbent bed is by eight kinds of different types of adsorbents layered arrangement in proportion, it is ensured that efficient impurity absorption curve, is purifying
One of key equipment, the forecooler and pressure of -30 DEG C of CO2 entrance after purification are liquefied for the liquefier of 3.0MPa, cold
Source is liquefied ammonia;Liquefier liquid CO 2 out enters in finished pot.
A kind of mycoprotein of the method by-product of described stalk production cellulosic ethanol, described yeast fermentation after fermentation
Mash processing procedure is：Stop fermentation stirring fermentation liquid after yeast fermentation and staticly settle 48h, the sample examination in the middle part of tank body
It is considered as sedimentation when distiller's yeast cell number is less than 2,000,000 plants/ml in karusen flow container to terminate, centrifuge obtains yeast thalline egg after separating
White feed, through being dried to obtain commodity mycoprotein.
Beneficial effects of the present invention：
1. stalk of the invention produces the agricultural wastes such as cellulosic ethanol and five kinds of methods of byproduct, stalk in the art
Six kinds of products such as cellulosic ethanol, lignin, biogas, bio-feritlizer, animal feeding-stuff containing somatic protein, CO2 are produced simultaneously, realize raw material
Full constituent makes full use of.
2. stalk of the invention produces cellulosic ethanol and five kinds of methods of byproduct, the agricultural wastes such as stalk in production process
The yield of raw material stalk is greatly improved using thermal and hydric environment processing mode, the generation of harmful toxic matter is reduced.
Stalk of the invention produces cellulosic ethanol and five kinds of methods of byproduct, and the useless mash of distillation directly carries out anaerobism hair
Ferment treatment, biogas slurry carries out separating production lignin after anaerobism, improves the operability of lignin separation.
Stalk of the invention produces cellulosic ethanol and five kinds of methods of byproduct, and using two-stage UF membrane, technology will detest
Oxygen sewage carries out advanced treating, reaches boiler soft water requirement and produces biomass fertilizers.
Stalk of the invention produces the agricultural wastes such as cellulosic ethanol and five kinds of methods of byproduct, stalk in this technique
In produce cellulosic ethanol, lignin, protein feed, bio-feritlizer, biogas, six kinds of products such as liquid CO 2 simultaneously.
Stalk of the invention produces cellulosic ethanol and five kinds of methods of byproduct, and the enzymolysis liquid glucose for being produced is not required to carry out
Separation of solid and liquid, can directly be fermented.
Stalk of the invention produces cellulosic ethanol and five kinds of methods of byproduct, and the useless wine with dregs of produced distillation carries out anaerobism
After fermentation, lignin, bio-feritlizer, technique Water circulation can be separated.
Stalk of the invention produces cellulosic ethanol and five kinds of methods of byproduct, and the fermentation later stage realizes distillery yeast
Separate production animal feeding-stuff containing somatic protein.
Stalk of the invention produces cellulosic ethanol and five kinds of methods of byproduct, in process of production, the agricultural such as stalk
Discarded object uses thermal and hydric environment processing method.
Brief description of the drawings：
Accompanying drawing 1 is structural representation of the invention.
Specific embodiment：
Embodiment 1：
The method that stalk produces cellulosic ethanol, comprises the following steps：（1）The treatment of stalk early stage and thermal and hydric environment pretreatment；（2）
Batch mixing and enzymatic saccharification are processed；（3）Fermentation purification processes；（4）Ferment the CO for producing2Treatment；（5）The useless wine with dregs treatment of distillation；（6）Ferment
Mother's fermentation after fermentation mash separating thallus albumen, described fermentation purification processes process is：After through enzymolysis, liquid glucose is cooled to 32
20% yeast is accessed after DEG C carries out alcoholic fermentation, and fermentation time 70h carries out temperature control, hair is taken away using frozen water in fermentation process
The fermentation fever that ferment is produced, control fermentation temperature is in 30-35 DEG C, residual sugar<0.3% is considered as fermentation ends, terminates the alcohol hair of fermentation
Ferment mash delivers to distilling apparatus and carries out distilation and obtain cellulosic ethanol after precipitating 48h yeast separations, and distillation is using double
Thick column differential-pressure distillation device carries out distillation procedure, and operation temperature is 103-108 DEG C of thick tower, 0.06-0.15mpa of tower top pressure,
85-95 DEG C of combined column temperature, tower top pressure-0.05-- 0.08mpa；Smart 120-128 DEG C of tower temperature degree, tower top pressure 0.06-
0.15mpa。
Embodiment 2：
The method that described stalk produces cellulosic ethanol, described stalk early stage treatment and thermal and hydric environment preprocessing process are：
Enter alcohol production device area after maize straw is collected into bundling, stacking storage, conveying crushing, dedusting removal of impurities, drying, briquetting,
The briquetting stalk of 15% moisture delivers to hot water environment formula bolt after Water spray pre-soaking, washing after moisture reaches 60% in device area
In plug flow reactor, 1.3-1.8mpa steam is passed through in the reactor, ton stalk needs 0.2-0.5t of steam, stop 12-
15min is reacted.
Embodiment 3：
The method that stalk described in embodiment 1 or 2 produces cellulosic ethanol, described batch mixing and enzymatic saccharification processing procedure be：
Stalk material delivers to enzymatic vessel by blender after being processed through thermal and hydric environment, added in blender liquid NaOH adjust PH to
4.8-5.0,2-5kg/ tons of stalk of liquid NaOH additions, cellulase 10kg/t stalks carry out enzymatic saccharification, controlled enzymatic hydrolysis temperature
50-55 DEG C of degree.
Embodiment 4：
The carbon dioxide of the method by-product of the stalk production cellulosic ethanol described in embodiment 1 or 2 or 3, described fermentation is produced
CO2Processing procedure is：Ferment the CO for producing2Dissolved organic matter gas, the CO2 gas after purification are removed by Water spray washing
Body carries out spray washing and removes insoluble grease through 0.06% liquor potassic permanganate, and first is crossed by the gas after two-step purification
Boosted into carbon-dioxide gas compressor after water distributing can point water, after boosting to 3.0MPa, proceeding through the first cooler, second
Water distributing can and drying bed are further dehydrated, and the CO2 after dehydration enters adsorbent bed after the second cooler is cooled down, and carries out removing impurities matter
Treatment, adsorbent bed is by eight kinds of different types of adsorbents layered arrangement in proportion, it is ensured that efficient impurity absorption curve, is pure
One of key equipment of change, the forecooler and pressure of -30 DEG C of CO2 entrance after purification are liquefied for the liquefier of 3.0MPa,
Low-temperature receiver is liquefied ammonia;Liquefier liquid CO 2 out enters in finished pot.
Embodiment 5：
The mycoprotein of the method by-product of one of embodiment 1-4 described stalk production cellulosic ethanol, described yeast fermentation
After fermentation mash processing procedure is：Stop fermentation stirring fermentation liquid after yeast fermentation to staticly settle 48h, taken according to tank body middle part
It is considered as sedimentation when distiller's yeast cell number is less than 2,000,000 plants/ml in sample chemical examination karusen flow container to terminate, centrifuge obtains yeast after separating
Animal feeding-stuff containing somatic protein, through being dried to obtain commodity mycoprotein.
Embodiment 6：
The method that cellulosic ethanol is produced according to one of embodiment 1-4 described stalk, described stalk early stage treatment and hydro-thermal
Environment preprocessing process is：Maize straw is collected into bundling, stacking storage, conveying crushing, dedusting removal of impurities, drying, briquetting granulation
Afterwards, in plug flow reactor, steam is added, is pre-processed by thermal and hydric environment device, control steam explosion pressure 1.3-
1.8Mpa。
Embodiment 7：
The method that stalk according to one of embodiment 1-4 or embodiment 6 produces cellulosic ethanol, described batch mixing and enzyme
Solving saccharification processing procedure is：Stalk material delivers to enzymatic vessel by blender after being processed through thermal and hydric environment, and work is pressed in blender
Skill requirement addition liquid caustic soda, cellulase carry out enzymatic saccharification, 50-55 DEG C of controlled enzymatic hydrolysis temperature.
Embodiment 8：
The method that stalk according to one of embodiment 1-4 or embodiment 6 or 7 produces cellulosic ethanol, described fermentation
Purification processes process is：Accessing yeast after through enzymolysis, after liquid glucose is cooled into 32 DEG C carries out alcoholic fermentation, and ferment after ripening mash
Distilation is carried out by delivering to distilling apparatus after yeast separation and obtains cellulosic ethanol.
Embodiment 9：
The method that stalk according to one of embodiment 1-4 or embodiment 6 or 7 or 8 produces cellulosic ethanol, described hair
The CO that ferment is produced2Processing procedure is：Ferment the CO for producing2Washed by washing, potassium, compressed, be dehydrated, freezing production liquid CO2。
Claims (5)
1. a kind of method that stalk produces cellulosic ethanol, it is characterized in that：Comprise the following steps：（1）The treatment of stalk early stage and water
Thermal environment is pre-processed；（2）Batch mixing and enzymatic saccharification are processed；（3）Fermentation purification processes；（4）Ferment the CO for producing2Treatment；（5）Steam
Evaporate useless wine with dregs treatment；（6）Yeast ferments after fermentation mash separating thallus albumen, and described fermentation purification processes process is：Through enzymolysis
Afterwards, liquid glucose is cooled to after 32 DEG C and accesses 20% yeast and carry out alcoholic fermentation, fermentation time 70h enters trip temperature control in fermentation process
System, the fermentation fever that fermentation is produced is taken away using frozen water, and control fermentation temperature is in 30-35 DEG C, residual sugar<0.3% is considered as fermentation ends,
Terminate the alcoholic fermented liquor of fermentation after precipitating 48h yeast separations, deliver to distilling apparatus and carry out distilation and obtain fiber
Plain ethanol, distillation carries out distillation procedure using double thick column differential-pressure distillation devices, and operation temperature is 103-108 DEG C of thick tower, tower top pressure
0.06-0.15mpa of power, 85-95 DEG C of combined column temperature, tower top pressure-0.05-- 0.08mpa；Smart tower temperature degree 120-128
DEG C, 0.06-0.15mpa of tower top pressure.
2. the method that stalk according to claim 1 produces cellulosic ethanol, it is characterized in that：Described stalk early stage treatment
And thermal and hydric environment preprocessing process is：Maize straw is collected into bundling, stacking storage, conveying crushing, dedusting removal of impurities, drying, pressure
Enter alcohol production device area after block, the briquetting stalk of 15% moisture moisture after Water spray pre-soaking, washing reaches in device area
Delivered to after to 60% in hot water environment formula plug flow reactor, 1.3-1.8mpa steam is passed through in the reactor, ton stalk needs
0.2-0.5t of steam, stops 12-15min and is reacted.
3. the method that stalk according to claim 1 and 2 produces cellulosic ethanol, it is characterized in that：Described batch mixing and enzyme
Solving saccharification processing procedure is：Stalk material delivers to enzymatic vessel by blender after being processed through thermal and hydric environment, is added in blender
Liquid NaOH adjusts PH to 4.8-5.0, and 2-5kg/ tons of stalk of liquid NaOH additions, cellulase 10kg/t stalks carry out enzyme
Solution saccharification, 50-55 DEG C of controlled enzymatic hydrolysis temperature.
4. the stalk described in a kind of claim 1 produces the carbon dioxide of the method by-product of cellulosic ethanol, it is characterized in that：It is described
Fermentation produce CO2Processing procedure is：Ferment the CO for producing2Dissolved organic matter gas, purification are removed by Water spray washing
CO2 gases afterwards carry out spray washing and remove insoluble grease through 0.06% liquor potassic permanganate, by the gas after two-step purification
Body is boosted after crossing the first water distributing can point water into carbon-dioxide gas compressor, cold proceeding through first after boosting to 3.0MPa
But device, the second water distributing can and drying bed are further dehydrated, and the CO2 after dehydration enters adsorbent bed after the second cooler is cooled down,
Carry out de- impurity treatment, adsorbent bed is by eight kinds of different types of adsorbents layered arrangement in proportion, it is ensured that efficient impurity is inhaled
Attached curve, is one of key equipment of purifying, and the forecooler and pressure of -30 DEG C of CO2 entrance after purification are the liquefaction of 3.0MPa
Device is liquefied, and low-temperature receiver is liquefied ammonia;Liquefier liquid CO 2 out enters in finished pot.
5. a kind of one of claim 1-3 described stalk produces the mycoprotein of the method by-product of cellulosic ethanol, its feature
It is：Described yeast fermentation after fermentation mash processing procedure is：Stop fermentation stirring fermentation liquid after yeast fermentation to staticly settle
48h, it is considered as sedimentation and terminates when being less than 2,000,000 plants/ml according to distiller's yeast cell number in the sample examination karusen flow container of tank body middle part, from
Scheming obtains yeast animal feeding-stuff containing somatic protein after separating, through being dried to obtain commodity mycoprotein.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710181164.2A CN106834361A (en) | 2017-03-24 | 2017-03-24 | The method that stalk produces cellulosic ethanol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710181164.2A CN106834361A (en) | 2017-03-24 | 2017-03-24 | The method that stalk produces cellulosic ethanol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106834361A true CN106834361A (en) | 2017-06-13 |
Family
ID=59130458
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710181164.2A Pending CN106834361A (en) | 2017-03-24 | 2017-03-24 | The method that stalk produces cellulosic ethanol |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106834361A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108841912A (en) * | 2018-06-20 | 2018-11-20 | 冯国青 | A kind of technique preparing and separate biological butanol and bio-ethanol |
| CN110846345A (en) * | 2019-12-06 | 2020-02-28 | 白博 | Production process of cotton straw fulvic acid and cellulosic ethanol |
| CN114560557A (en) * | 2022-01-25 | 2022-05-31 | 太原市润民环保节能有限公司 | Efficient composite carbon source for denitrification treatment of wastewater |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101555495A (en) * | 2009-05-18 | 2009-10-14 | 徐守才 | Ethanol-guiding straw bio-refining full-sealing integration system |
| CN102131940A (en) * | 2008-08-29 | 2011-07-20 | 艾欧基能源公司 | Method for low water hydrolysis or pretreatment of polysaccharides in a lignocellulosic feedstock |
| CN102643867A (en) * | 2012-04-23 | 2012-08-22 | 天津大学 | Device and method for producing cellulosic ethanol |
| CN105907801A (en) * | 2016-04-20 | 2016-08-31 | 山西农业大学 | Method of continuously producing dietary fibers, alcohol and single-cell protein with potato residue |
-
2017
- 2017-03-24 CN CN201710181164.2A patent/CN106834361A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102131940A (en) * | 2008-08-29 | 2011-07-20 | 艾欧基能源公司 | Method for low water hydrolysis or pretreatment of polysaccharides in a lignocellulosic feedstock |
| CN101555495A (en) * | 2009-05-18 | 2009-10-14 | 徐守才 | Ethanol-guiding straw bio-refining full-sealing integration system |
| CN102643867A (en) * | 2012-04-23 | 2012-08-22 | 天津大学 | Device and method for producing cellulosic ethanol |
| CN105907801A (en) * | 2016-04-20 | 2016-08-31 | 山西农业大学 | Method of continuously producing dietary fibers, alcohol and single-cell protein with potato residue |
Non-Patent Citations (6)
| Title |
|---|
| 党建章等: "《发酵工艺教程 第2版》", 31 July 2016 * |
| 刘荣厚等: "《生物质生物转换技术》", 31 December 2015 * |
| 沈煜如: "《新型染整技术》", 30 November 1999, 中国纺织出版社 * |
| 王伟东等: "《微生物学》", 31 August 2015 * |
| 赵二永等: "双粗塔差压热耦合蒸馏生产燃料乙醇", 《酿酒科技》 * |
| 陆强等: "《液体生物燃料技术与工程》", 31 January 2013, 上海科学技术出版社 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108841912A (en) * | 2018-06-20 | 2018-11-20 | 冯国青 | A kind of technique preparing and separate biological butanol and bio-ethanol |
| CN110846345A (en) * | 2019-12-06 | 2020-02-28 | 白博 | Production process of cotton straw fulvic acid and cellulosic ethanol |
| CN114560557A (en) * | 2022-01-25 | 2022-05-31 | 太原市润民环保节能有限公司 | Efficient composite carbon source for denitrification treatment of wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2019154110A1 (en) | Process for producing ethanol fuel by using corn starch as raw material | |
| US7670813B2 (en) | Inorganic salt recovery during processing of lignocellulosic feedstocks | |
| US10513714B2 (en) | Lignocellulosic conversion process comprising sulfur dioxide and/or sulfurous acid pretreatment | |
| Song et al. | Improving biohydrogen production through dark fermentation of steam-heated acid pretreated Alternanthera philoxeroides by mutant Enterobacter aerogenes ZJU1 | |
| CN102061323B (en) | Comprehensive utilization process of wood cellulose | |
| US7585652B2 (en) | Recovery of inorganic salt during processing of lignocellulosic feedstocks | |
| US9139852B2 (en) | Method and apparatus for pretreating biomass using internal heat | |
| CN104630307B (en) | A kind of biorefinery integrated technique of corn complete stool component separation classified utilization | |
| BG100071A (en) | Method for the production of sugars by hydrolysis with strong acid of cellulose and hemicellulose products | |
| CN102010882A (en) | Method for performing lignocelluloses raw material high-temperature diluted acid pretreatment by using extremely small amount of water | |
| CN106834361A (en) | The method that stalk produces cellulosic ethanol | |
| CN110791532A (en) | Method for preparing ethanol from cellulose and comprehensively utilizing biomass | |
| WO2016201360A1 (en) | Cellulosic biofuel and co-products | |
| EA014457B1 (en) | Method for coproduction of bioethanol and energy from a starchy plant starting material | |
| CN106929546A (en) | The method that rice straw produces cellulosic ethanol | |
| CA2565433C (en) | Inorganic salt recovery during processing of lignocellulosic feedstocks | |
| US10597688B2 (en) | Method for preparing fermentable sugar from wood-based biomass | |
| CN102605003B (en) | Method for producing alcohol from potato raw materials | |
| CN111234888A (en) | System and method for recycling supercritical water reaction product and wet biomass | |
| CN112111540A (en) | Method for adding acidic reagent to carry out pretreatment and biotransformation in densification process of lignocellulose raw material | |
| KR101504197B1 (en) | Method for preparing bioethanol from lignocellulosic biomass | |
| CN211896835U (en) | System for supercritical water reaction product is wet biomass resource in coordination | |
| CN203794890U (en) | Biomass fertilizer preparation and gas gathering system based on straws | |
| CN111172228B (en) | Method for producing biogas by using camellia oleifera shells | |
| CN107190027A (en) | The method that alkali grinds pretreated straw |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |