DK3241907T3 - Fremgangsmåde til fremstilling af et bio-produkt - Google Patents
Fremgangsmåde til fremstilling af et bio-produkt Download PDFInfo
- Publication number
- DK3241907T3 DK3241907T3 DK16425038.3T DK16425038T DK3241907T3 DK 3241907 T3 DK3241907 T3 DK 3241907T3 DK 16425038 T DK16425038 T DK 16425038T DK 3241907 T3 DK3241907 T3 DK 3241907T3
- Authority
- DK
- Denmark
- Prior art keywords
- ligno
- cellulosic biomass
- pressure
- lignocellulosic biomass
- biomass
- Prior art date
Links
Classifications
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- 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
- C12P19/02—Monosaccharides
-
- 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
- C12P19/04—Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds
-
- 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
- C13—SUGAR INDUSTRY
- C13K—SACCHARIDES OBTAINED FROM NATURAL SOURCES OR BY HYDROLYSIS OF NATURALLY OCCURRING DISACCHARIDES, OLIGOSACCHARIDES OR POLYSACCHARIDES
- C13K1/00—Glucose; Glucose-containing syrups
- C13K1/02—Glucose; Glucose-containing syrups obtained by saccharification of cellulosic materials
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13K—SACCHARIDES OBTAINED FROM NATURAL SOURCES OR BY HYDROLYSIS OF NATURALLY OCCURRING DISACCHARIDES, OLIGOSACCHARIDES OR POLYSACCHARIDES
- C13K13/00—Sugars not otherwise provided for in this class
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13K—SACCHARIDES OBTAINED FROM NATURAL SOURCES OR BY HYDROLYSIS OF NATURALLY OCCURRING DISACCHARIDES, OLIGOSACCHARIDES OR POLYSACCHARIDES
- C13K13/00—Sugars not otherwise provided for in this class
- C13K13/002—Xylose
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C1/00—Pretreatment of the finely-divided materials before digesting
- D21C1/02—Pretreatment of the finely-divided materials before digesting with water or steam
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C11/00—Regeneration of pulp liquors or effluent waste waters
- D21C11/0007—Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
-
- 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
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- 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)
- Biochemistry (AREA)
- Zoology (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Microbiology (AREA)
- Biotechnology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- Genetics & Genomics (AREA)
- Emergency Medicine (AREA)
- Processing Of Solid Wastes (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Claims (11)
1. Fremgangsmåde til fremstilling af et bio-produkt fra en lignocelluloseholdig biomasse der består afen samlet mængde xylaner, en samlet mængde glukaner, en samlet mængde lignin, og vand, hvor fremgangsmåden omfatter trinnene: a. at indføre den lignocelluloseholdige biomasse, en samlet mængde gas og damp i en trykreaktor i en trykreaktoranordning der drives på en kontinuerlig måde under forhold, hvor der er et damp-tomrum i trykreaktoren, hvor en del af dampen kondenseres i den lignocelluloseholdige biomasse med trykreaktoren; b. at fastholde denlignocelluloseholdige biomasse i trykreaktoren ved et lignocelluloseholdig biomassetryk der er større end 10 bar i en opholdstid fra 0,5 minutter til 120 minutter, ved en damp-tomrumtemperatur i et område fra 130°C til 230°C, hvor lignocelluloseholdig biomassetrykket er mindst 1 bar større end et ren damp-ligevægtstryk ved damp-tomrumtemperaturen; c. at raffinere den lignocelluloseholdige biomasse ved hurtigt at lette det lignocelluloseholdige biomassetryk mens den lignocelluloseholdige biomasse udledes fra trykreaktoranordningen for at danne en forbehandlet lignocelluloseholdig biomasse; d. at hydrolysere mindst en del af glukanerne til en mængde glukose; og e. at omdanne mindst en del af mængden af glukose til bio-produktet.
2. Fremgangsmåde ifølge krav 1, hvor den lignocelluloseholdige biomasse endvidere omfatter indespærret luft, og mindst en del af gassen er den indespærrede luft indført i trykreaktoren som del af den lignocelluloseholdige biomasse.
3. Fremgangsmåde ifølge et hvilket som helst af kravene 1 til 2, hvor fremgangsmåden endvidere omfatter et xylan-separationstrin, hvor mindre end 15% af den samlede mængde af xylaner separeres fra den lignocelluloseholdige biomasse inden indførelse i trykreaktoren.
4. Fremgangsmåde ifølge et hvilket som helst af kravene 1 til 2, hvor fremgangsmåden ikke omfatter et xylan-separationstrin inden indførelse i trykreaktoren.
5. Fremgangsmåde ifølge et hvilket som helst af kravene 1 til 4, hvor fremgangsmåden endvidere omfatter et iblødsætningstrin, hvor lignocelluloseholdig biomassen lægges i blød i en væske der består af vand inden lignocelluloseholdig biomassen indføres i trykreaktoren.
6. Fremgangsmåde ifølge krav 5, hvor fremgangsmåden endvidere omfatter et luftningstrin, hvor den lignocelluloseholdige biomasse luftes efter iblødsætningstrinnet ved at eksponere den lignocelluloseholdige biomasse for luft.
7. Fremgangsmåde ifølge et hvilket som helst af kravene 1 til 6, hvor den lignocelluloseholdige biomasse komprimeres ved en komprimeringstemperatur i et område fra 25°C til lavere end 100 °C inden den lignocelluloseholdige biomasse indføres i trykreaktoren.
8. Fremgangsmåde ifølge et hvilket som helst af kravene 1 til 7, hvor trykreaktoren har et trykreaktorvolumen, og damp-tomrummet har et damp-tomrum-volumen, der er mellem 5% og 80% af trykreaktorvolumenet.
9. Fremgangsmåde ifølge et hvilket som helst af kravene 1 til 8, hvor det lignocelluloseholdige biomassetryk er valgt således, at damp fra raffineringstrinnet sprænger den lignocelluloseholdige biomasse.
10. Fremgangsmåde ifølge et hvilket som helst af kravene 1 til 9, hvor damp-tomrumtemperaturen og opholdstiden styres således, at mere end 65% af den samlede mængde af xylaner genvindes i den forbehandlede lignocelluloseholdige biomasse.
11. Fremgangsmåde ifølge et hvilket som helst af kravene 1 til 10, hvor det lignocelluloseholdige biomassetryk styres således, at den forbehandlede lignocelluloseholdige biomasse omfatter en mængde tilgængelige glukaner, og mængden af tilgængelige glukaner i den forbehandlede lignocelluloseholdige biomasse i forhold til den samlede mængde glukaner i den forbehandlede lignocelluloseholdige biomasse er større end 80%.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP16425038.3A EP3241907B1 (en) | 2016-05-03 | 2016-05-03 | Process for producing a bio-product |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DK3241907T3 true DK3241907T3 (da) | 2019-04-15 |
Family
ID=56121009
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DK16425038.3T DK3241907T3 (da) | 2016-05-03 | 2016-05-03 | Fremgangsmåde til fremstilling af et bio-produkt |
Country Status (14)
| Country | Link |
|---|---|
| US (1) | US11174498B2 (da) |
| EP (1) | EP3241907B1 (da) |
| CN (1) | CN109072269B (da) |
| BR (1) | BR112018071665A2 (da) |
| DK (1) | DK3241907T3 (da) |
| ES (1) | ES2717825T3 (da) |
| HR (1) | HRP20190560T1 (da) |
| HU (1) | HUE042465T2 (da) |
| LT (1) | LT3241907T (da) |
| PL (1) | PL3241907T3 (da) |
| PT (1) | PT3241907T (da) |
| RS (1) | RS58648B1 (da) |
| SI (1) | SI3241907T1 (da) |
| WO (1) | WO2017191091A1 (da) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE543000C2 (en) * | 2018-06-26 | 2020-09-22 | Valmet Oy | Method and system for discharging hydrothermally treated lignocellulosic material |
| FI128936B (en) * | 2020-03-11 | 2021-03-31 | Luonnonvarakeskus | RECOVERY OF VALUE COMPONENTS FROM BIOMASS |
| CN115341004A (zh) * | 2021-05-12 | 2022-11-15 | 国投生物科技投资有限公司 | 生物质原料制备单糖的方法 |
| IT202100031070A1 (it) | 2021-12-10 | 2023-06-10 | Versalis Spa | Procedimento per l’idratazione di lieviti in forma disidratata. |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2516833A (en) | 1947-06-09 | 1950-08-01 | Ant-Wuorinen Olli Viljo Anton | Process for hydrolyzing cellulosic materials |
| US4136207A (en) | 1977-01-24 | 1979-01-23 | Stake Technology Ltd. | Method of treating lignocellulose materials to produce ruminant feed |
| ES8201627A1 (es) | 1980-02-23 | 1981-12-16 | Reitter Franz Johann | Procedimiento e instalacion para la hidrolisis continua de hemicelulosas que contienen pentosanas de celulosa. |
| CN1190373C (zh) | 2000-02-17 | 2005-02-23 | 里索国家实验室 | 处理木质纤维素材料的方法 |
| US7666637B2 (en) | 2006-09-05 | 2010-02-23 | Xuan Nghinh Nguyen | Integrated process for separation of lignocellulosic components to fermentable sugars for production of ethanol and chemicals |
| US8057639B2 (en) | 2008-02-28 | 2011-11-15 | Andritz Inc. | System and method for preextraction of hemicellulose through using a continuous prehydrolysis and steam explosion pretreatment process |
| TW201040279A (en) | 2009-03-31 | 2010-11-16 | Chemtex Italia S R L | Improved biomass pretreatment process |
| WO2013063478A1 (en) | 2011-10-28 | 2013-05-02 | Treefree Biomass Solutions, Inc. | Bioconversion of biomass to ethanol |
| EA026271B9 (ru) * | 2012-08-01 | 2017-07-31 | Инбикон А/С | Способы переработки лигноцеллюлозной биомассы путем применения одностадийного аутогидролиза и ферментативного гидролиза с отводом c5 и постгидролизом |
| AU2013318273B2 (en) | 2012-09-19 | 2017-08-31 | Andritz Inc. | Method and apparatus for adding steam for a steam explosion pretreatment process |
| EP2765178A1 (en) | 2013-02-07 | 2014-08-13 | Arbaflame Technology AS | Method of producing carbon-enriched biomass material |
| ITTO20130711A1 (it) | 2013-09-02 | 2015-03-03 | Biochemtex Spa | Composizioni di glicole etilenico bioderivato per bottiglie di poliestere |
| CN104212531A (zh) | 2014-09-25 | 2014-12-17 | 江南大学 | 一种利用外源气体辅助蒸汽爆破生物质废弃物制备固体燃料的方法 |
| BR112017008188A2 (pt) | 2014-10-29 | 2017-12-26 | Cambi Tech As | método e dispositivo para tratamento de biomassa e resíduos orgânicos |
-
2016
- 2016-05-03 HU HUE16425038A patent/HUE042465T2/hu unknown
- 2016-05-03 LT LTEP16425038.3T patent/LT3241907T/lt unknown
- 2016-05-03 DK DK16425038.3T patent/DK3241907T3/da active
- 2016-05-03 RS RS20190396A patent/RS58648B1/sr unknown
- 2016-05-03 PT PT16425038T patent/PT3241907T/pt unknown
- 2016-05-03 PL PL16425038T patent/PL3241907T3/pl unknown
- 2016-05-03 EP EP16425038.3A patent/EP3241907B1/en active Active
- 2016-05-03 ES ES16425038T patent/ES2717825T3/es active Active
- 2016-05-03 SI SI201630217T patent/SI3241907T1/sl unknown
-
2017
- 2017-05-02 CN CN201780025661.1A patent/CN109072269B/zh active Active
- 2017-05-02 WO PCT/EP2017/060336 patent/WO2017191091A1/en active Application Filing
- 2017-05-02 US US16/095,996 patent/US11174498B2/en active Active
- 2017-05-02 BR BR112018071665-0A patent/BR112018071665A2/pt active IP Right Grant
-
2019
- 2019-03-22 HR HRP20190560TT patent/HRP20190560T1/hr unknown
Also Published As
| Publication number | Publication date |
|---|---|
| RS58648B1 (sr) | 2019-05-31 |
| WO2017191091A1 (en) | 2017-11-09 |
| EP3241907A1 (en) | 2017-11-08 |
| CN109072269A (zh) | 2018-12-21 |
| US11174498B2 (en) | 2021-11-16 |
| BR112018071665A2 (pt) | 2019-02-19 |
| EP3241907B1 (en) | 2018-12-26 |
| LT3241907T (lt) | 2019-05-27 |
| SI3241907T1 (sl) | 2019-05-31 |
| ES2717825T3 (es) | 2019-06-25 |
| US20190136279A1 (en) | 2019-05-09 |
| CN109072269B (zh) | 2022-02-11 |
| PT3241907T (pt) | 2019-04-15 |
| HUE042465T2 (hu) | 2019-07-29 |
| HRP20190560T1 (hr) | 2019-05-03 |
| PL3241907T3 (pl) | 2019-07-31 |
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