HRP20221258T1 - Unaprrijeđeni proces za ubrzanu hidrolizu biomase sa visokim udjelom čvrstih materija - Google Patents
Unaprrijeđeni proces za ubrzanu hidrolizu biomase sa visokim udjelom čvrstih materija Download PDFInfo
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- HRP20221258T1 HRP20221258T1 HRP20221258TT HRP20221258T HRP20221258T1 HR P20221258 T1 HRP20221258 T1 HR P20221258T1 HR P20221258T T HRP20221258T T HR P20221258TT HR P20221258 T HRP20221258 T HR P20221258T HR P20221258 T1 HRP20221258 T1 HR P20221258T1
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- 238000000034 method Methods 0.000 title claims 29
- 230000007062 hydrolysis Effects 0.000 title claims 7
- 238000006460 hydrolysis reaction Methods 0.000 title claims 7
- 239000002028 Biomass Substances 0.000 title claims 6
- 239000007787 solid Substances 0.000 title claims 4
- 239000002904 solvent Substances 0.000 claims 25
- 239000002994 raw material Substances 0.000 claims 17
- 229920002678 cellulose Polymers 0.000 claims 11
- 239000001913 cellulose Substances 0.000 claims 11
- 239000003054 catalyst Substances 0.000 claims 10
- 241000894007 species Species 0.000 claims 8
- 150000001875 compounds Chemical class 0.000 claims 3
- 102000004190 Enzymes Human genes 0.000 claims 2
- 108090000790 Enzymes Proteins 0.000 claims 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims 2
- 229920002488 Hemicellulose Polymers 0.000 claims 2
- 239000008103 glucose Substances 0.000 claims 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 2
- LUEWUZLMQUOBSB-FSKGGBMCSA-N (2s,3s,4s,5s,6r)-2-[(2r,3s,4r,5r,6s)-6-[(2r,3s,4r,5s,6s)-4,5-dihydroxy-2-(hydroxymethyl)-6-[(2r,4r,5s,6r)-4,5,6-trihydroxy-2-(hydroxymethyl)oxan-3-yl]oxyoxan-3-yl]oxy-4,5-dihydroxy-2-(hydroxymethyl)oxan-3-yl]oxy-6-(hydroxymethyl)oxane-3,4,5-triol Chemical compound O[C@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@@H](O[C@@H]2[C@H](O[C@@H](OC3[C@H](O[C@@H](O)[C@@H](O)[C@H]3O)CO)[C@@H](O)[C@H]2O)CO)[C@H](O)[C@H]1O LUEWUZLMQUOBSB-FSKGGBMCSA-N 0.000 claims 1
- GUBGYTABKSRVRQ-CUHNMECISA-N D-Cellobiose Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-CUHNMECISA-N 0.000 claims 1
- 229920002581 Glucomannan Polymers 0.000 claims 1
- 229920001706 Glucuronoxylan Polymers 0.000 claims 1
- 229920002000 Xyloglucan Polymers 0.000 claims 1
- UGXQOOQUZRUVSS-ZZXKWVIFSA-N [5-[3,5-dihydroxy-2-(1,3,4-trihydroxy-5-oxopentan-2-yl)oxyoxan-4-yl]oxy-3,4-dihydroxyoxolan-2-yl]methyl (e)-3-(4-hydroxyphenyl)prop-2-enoate Chemical compound OC1C(OC(CO)C(O)C(O)C=O)OCC(O)C1OC1C(O)C(O)C(COC(=O)\C=C\C=2C=CC(O)=CC=2)O1 UGXQOOQUZRUVSS-ZZXKWVIFSA-N 0.000 claims 1
- 229920000617 arabinoxylan Polymers 0.000 claims 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 claims 1
- 238000010924 continuous production Methods 0.000 claims 1
- 239000000539 dimer Substances 0.000 claims 1
- 229940046240 glucomannan Drugs 0.000 claims 1
- 230000003301 hydrolyzing effect Effects 0.000 claims 1
- 229920005610 lignin Polymers 0.000 claims 1
- 239000002029 lignocellulosic biomass Substances 0.000 claims 1
- 244000005700 microbiome Species 0.000 claims 1
- 150000007522 mineralic acids Chemical class 0.000 claims 1
- 239000003960 organic solvent Substances 0.000 claims 1
- 229920000642 polymer Polymers 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- 229920001221 xylan Polymers 0.000 claims 1
- 150000004823 xylans Chemical class 0.000 claims 1
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
- C12P19/04—Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B1/00—Preparatory treatment of cellulose for making derivatives thereof, e.g. pre-treatment, pre-soaking, activation
- C08B1/02—Rendering cellulose suitable for esterification
-
- 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
- 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
- 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
Claims (20)
1. Proces za hidrolizu ligno-celulozne biomase koji obuhvaća slijedeće korake
A) Dovođenje u kontakt ligno-celulozne sirovine, sirovine sačinjene od biomase koja ima suhi sadržaj i vodu sa barem dijelom rastvarača, rastvarača sačinjenog od u vodi topivih hidroliziranih vrsta; pri čemu je barem dio u vodi topivih hidroliziranih vrsta isti kao u vodi topive hidrolizirane vrste koje se mogu dobiti hidrolizom biomase u sirovini;
B) održavanje kontakta između sirovine iz toka sirovine i rastvarača u prisustvu kompozicije katalizatora, na temperaturi u rasponu od 20°C do 200°C tijekom vremena u rasponu od 5 minuta do 72 sata za stvaranje hidroliziranog proizvoda iz biomase u sirovini;
pri čemu spomenuti katalizator sadrži barem jedan enzim ili mikroorganizam koji konvertira barem jedan od spojeva u biomasi u spoj ili spojeve niže molekulske mase;
pri čemu odnos količine celuloze zajedno sa količinom proizvoda iz hidrolizirane celuloze u rastvaraču prema količini celuloze u sirovini je barem 0.8:1;
i pri čemu spomenute u vodi topive hidrolizirane vrste su u vodi topive hidrolizirane vrste celuloze izabrane od glukoze, celobioze, i visokih glukoznih polimera, uključujući njihove odgovarajuće dimere i oligomere;
i u vodi topive hidrolizirane vrste hemiceluloze izabrane od ksilana, glukuronoksilana, arabinoksilana, glukomanana, i ksiloglukana;
i pri čemu se spomenuti proces izvršava bez dodavanja neorganske kiseline ili organskih rastvarača za solubilizaciju lignina; i pri čemu spomenuta ligno-celulozna sirovina sadrži više od 5% mase suhog sadržaja celuloze.
2. Proces prema patentnom zahtjevu 1, pri čemu suhi sadržaj obuhvaća celulozu, hemicelulozu, pri čemu je barem dio u vodi topivih hidroliziranih vrsta isti kao u vodi topive hidrolizirane vrste koje se mogu dobiti iz hidrolize celuloze u sirovini, a kontakt između sirovine i rastvarača je u prisustvu katalizatora za hidrolizu celuloze.
3. Proces prema patentnom zahtjevu 2, pri čemu odnos mase celuloze zajedno sa proizvodima hidrolize celuloze u rastvaraču prema masi celuloze u ligno- celuloznoj sirovini je izabran iz grupe koja se sastoji od više od 1 :1, više od 1.5:1, više od 2:1, više od 3:1, više od 4:1, i više od 5:1.
4. Proces prema bilo kojem od patentnih zahtjeva 2 do 3, pri čemu barem dio kompozicije katalizatora je u kontaktu sa sirovinom prije nego što sirovna dođe u kontakt sa barem dijelom rastvarača.
5. Proces prema bilo kojem od patentnih zahtjeva 1 do 4, pri čemu odnos biomase prema vodi sirovine odabran je iz grupe koja se sastoji od više od 1 :4, više od 1 :3, više od 1 :2, više od 1 :1.5, više od 1 :1, i više od 1 :0.9.
6. Proces prema bilo kojem od patentnih zahtjeva 2 do 5, gdje kompozicija katalizatora sadrži enzim.
7. Proces prema bilo kojem od patentnih zahtjeva 1 do 6, pri čemu je temperatura u rasponu izabranom iz grupe koja se sastoji od 20 do 105°C, i 20 do 95°C.
8. Proces prema bilo kojem od patentnih zahtjeva 1 do 7, pri čemu je vrijeme u rasponu izabranom iz grupe koja se sastoji od 5 minuta do 48 sati, 5 minuta do 36 sati, 5 minuta do 24 sati, 5 minuta do 12 sati, 5 minuta do 8 sati.
9. Proces prema bilo kojem od patentnih zahtjeva 1 do 8, pri čemu proces predstavlja serijski proces koji obuhvaća sljedeće korake
A) uvođenje sirovine u posudu koja već sadrži barem dio rastvarača,
B) uvođenje kompozicije katalizatora u posudu prije, u isto vrijeme sa, ili poslije uvođenja sirovine u posudu,
C) održavanje sirovine, rastvarača, i kompozicije katalizatora u posudi u spomenutom temperaturnom rasponu od 20°C do 200°C tijekom vremena u rasponu od 5 minuta do 72 sata,
D) uklanjanje hidroliziranog proizvoda iz posude.
10. Proces iz patentnog zahtjeva 9 pri čemu je sav hidrolizirani proizvod uklonjen iz posude prije uvođenja dodatne sirovine i rastvarača koji sadrži u vodi topive hidrolizirane vrste.
11. Proces prema patentnom zahtjevu 9, pri čemu dio hidroliziranog proizvoda, naime ostatak, je ostavljen u posudi.
12. Proces prema bilo kojem od patentnih zahtjeva 1 do 8, pri čemu je proces neprekidan proces koji obuhvaća sljedeće korake
A) neprekidno uvođenje sirovine u posudu koja već sadrži barem dio rastvarača, B) uvođenje kompozicije katalizatora u posudu,
C) neprekidno uklanjanje mase hidroliziranog proizvoda iz posude.
13. Proces prema patentnom zahtjevu 12, pri čemu proces predstavlja proces sa klipnim protjecanjem.
14. Proces prema patentnom zahtjevu 12, pri čemu proces koristi reaktor sa neprekidnim miješanjem.
15. Proces prema bilo kojem od patentnih zahtjeva 9 do 14, pri čemu je dio u toku rastvarača pomiješan sa sirovinom prije uvođenja u posudu, a odnos rastvarača prema toku sirovine je zasnovan na količini rastvarača u posudi zajedno sa količinom rastvarača u toku sirovine.
16. Proces prema bilo kojem od patentnih zahtjeva 1 do 15, pri čemu prije kontaktiranja ligno-celulozne sirovine sa rastvaračem, količina sirovine je raspoređena u barem prvi tok sirovine kako bi se stvorio prvi tok rastvarača hidrolizom sirovine prvog toka sirovine sa dodatkom katalizatora u prvi tok sirovine pri čemu je količina katalizatora u rasponu od 0.1 do 150 FPU / g suhog sadržaja cjelokupne sirovine i hidroliza je izvršena na temperaturi u rasponu od 20°C do 95°C tijekom vremena u rasponu od 5 minuta do 72 sata i ligno-celulozna sirovina, rastvarač, i rastvarač prvog toka rastvarača su u kontaktu jedan sa drugim i taj kontakt se održava na temperaturi u rasponu od 20°C do 95°C u vremenskom rasponu od 5 minuta do 72 sati.
17. Proces prema patentnom zahtjevu 16, pri čemu je dio prvog toka rastvarača pomiješan sa sirovinom koja nije prvi tok sirovine pre uvođenja u posudu i svi odnosi toka rastvarača prema toku sirovine su zasnovani na ukupnoj količini toka rastvarača što je količina prvog toka rastvarača i rastvarača u thp posudi.
18. Proces prema bilo kojem od patentnih zahtjeva 1 do 17, pri čemu je barem dio čvrstih materija u hidroliziranom proizvodu razdvojen od hidroliziranog proizvoda.
19. Proces prema bilo kojem od patentnih zahtjeva 1 do 18, pri čemu je barem dio čvrstih materija razdvojen od hidroliziranog proizvoda i recikliran u proces.
20. Proces prema bilo kojem od patentnih zahtjeva 1 do 18, pri čemu razdvajanje barem dijela čvrstih materija od toka hidroliziranog proizvoda je izvršeno pomoću uređaja izabranog iz grupe koja se sastoji od hidrociklona i centrifuga.
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ITPCT/IT2009/000124 | 2009-03-31 | ||
| ITPCT/IT2009/000127 | 2009-03-31 | ||
| IBPCT/IB2009/055737 | 2009-12-14 | ||
| IBPCT/IB2009/055736 | 2009-12-14 | ||
| PCT/IB2010/051413 WO2010113130A2 (en) | 2009-03-31 | 2010-03-31 | An improved process for the rapid hydrolysis of high solids biomass |
| EP10715357.9A EP2414532B1 (en) | 2009-03-31 | 2010-03-31 | An improved process for the rapid hydrolysis of high solids biomass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| HRP20221258T1 true HRP20221258T1 (hr) | 2022-12-09 |
Family
ID=42828782
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| HRP20221258TT HRP20221258T1 (hr) | 2009-03-31 | 2010-03-31 | Unaprrijeđeni proces za ubrzanu hidrolizu biomase sa visokim udjelom čvrstih materija |
Country Status (28)
| Country | Link |
|---|---|
| US (1) | US9200302B2 (hr) |
| EP (1) | EP2414532B1 (hr) |
| JP (2) | JP2012521778A (hr) |
| KR (1) | KR20120024575A (hr) |
| CN (1) | CN102449159B (hr) |
| AR (1) | AR075995A1 (hr) |
| AU (1) | AU2010231588B2 (hr) |
| BR (1) | BRPI1006467B1 (hr) |
| CA (1) | CA2756541C (hr) |
| CO (1) | CO6620075A2 (hr) |
| CU (1) | CU23986B1 (hr) |
| DK (1) | DK2414532T3 (hr) |
| EG (1) | EG26965A (hr) |
| ES (1) | ES2927855T3 (hr) |
| HR (1) | HRP20221258T1 (hr) |
| HU (1) | HUE060368T2 (hr) |
| LT (1) | LT2414532T (hr) |
| MA (1) | MA33226B1 (hr) |
| MX (1) | MX2011010185A (hr) |
| NZ (1) | NZ595851A (hr) |
| PE (1) | PE20120929A1 (hr) |
| PL (1) | PL2414532T3 (hr) |
| PT (1) | PT2414532T (hr) |
| RU (1) | RU2550264C2 (hr) |
| SG (1) | SG174956A1 (hr) |
| TN (1) | TN2011000480A1 (hr) |
| TW (1) | TW201100547A (hr) |
| WO (1) | WO2010113130A2 (hr) |
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| EP3594354A1 (en) | 2010-03-19 | 2020-01-15 | Poet Research Incorporated | Method for producing a fermentation product from biomass |
| CA2795503C (en) | 2010-03-19 | 2020-02-18 | Poet Research, Inc. | System for treatment of biomass to facilitate the production of ethanol |
| CN103068996B (zh) | 2010-06-17 | 2016-03-09 | 宝丽格公司 | 纤维素的酶促水解 |
| BR112012032999B1 (pt) | 2010-06-26 | 2022-11-29 | Virdia, Llc | Hidrolisado lignocelulósico e métodos de hidrólise ácida e desacidificação para gerar misturas de açúcar a partir de lignocelulose |
| IL206678A0 (en) | 2010-06-28 | 2010-12-30 | Hcl Cleantech Ltd | A method for the production of fermentable sugars |
| IL207329A0 (en) | 2010-08-01 | 2010-12-30 | Robert Jansen | A method for refining a recycle extractant and for processing a lignocellulosic material and for the production of a carbohydrate composition |
| IL207945A0 (en) | 2010-09-02 | 2010-12-30 | Robert Jansen | Method for the production of carbohydrates |
| CA2811144A1 (en) * | 2010-09-13 | 2012-03-22 | Greenfield Ethanol Inc. | De icing formulation utilizing co-products from lignocellulose to bio fuel process |
| PT106039A (pt) | 2010-12-09 | 2012-10-26 | Hcl Cleantech Ltd | Processos e sistemas para o processamento de materiais lenhocelulósicos e composições relacionadas |
| WO2012099967A1 (en) | 2011-01-18 | 2012-07-26 | Poet, Llc | Systems and methods for hydrolysis of biomass |
| US9512495B2 (en) | 2011-04-07 | 2016-12-06 | Virdia, Inc. | Lignocellulose conversion processes and products |
| US9982317B2 (en) | 2011-07-07 | 2018-05-29 | Poet Research, Inc. | Systems and methods for acid recycle |
| US9617608B2 (en) | 2011-10-10 | 2017-04-11 | Virdia, Inc. | Sugar compositions |
| ITTO20111219A1 (it) * | 2011-12-28 | 2013-06-29 | Beta Renewables Spa | Procedimento migliorato di pre-impregnazione per la conversione di biomassa |
| US9493851B2 (en) | 2012-05-03 | 2016-11-15 | Virdia, Inc. | Methods for treating lignocellulosic materials |
| CA3060976C (en) | 2012-05-03 | 2022-08-23 | Virdia, Inc. | Methods for treating lignocellulosic materials |
| US9611493B2 (en) | 2013-08-01 | 2017-04-04 | Renmatix, Inc. | Method for biomass hydrolysis |
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| US20150104842A1 (en) | 2013-10-10 | 2015-04-16 | E I Du Pont De Nemours And Company | Fuel compositions containing lignocellulosic biomass fermentation process syrup |
| US9499451B2 (en) | 2013-10-10 | 2016-11-22 | E I Du Pont De Nemours And Company | Soil conditioner compositions containing lignocellulosic biomass fermentation process syrup |
| US9435002B2 (en) * | 2014-06-07 | 2016-09-06 | Api Intellectual Property Holdings, Llc | Continuous processes for hydrolyzing hemicelluloses from ligocellulosic materials with cleaning system |
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| CN112226466A (zh) | 2015-01-07 | 2021-01-15 | 威尔迪亚公司 | 萃取和转化半纤维素糖的方法 |
| BR112017019325A2 (pt) | 2015-03-12 | 2018-06-05 | Du Pont | composição para a aplicação de paisagem e método para o tratamento de uma paisagem |
| US11091815B2 (en) | 2015-05-27 | 2021-08-17 | Virdia, Llc | Integrated methods for treating lignocellulosic material |
| JP2017139973A (ja) | 2016-02-08 | 2017-08-17 | 川崎重工業株式会社 | セルロース系バイオマスを原料とする酵素法による糖化液製造方法 |
| ES2789328T3 (es) | 2016-02-22 | 2020-10-26 | Versalis Spa | Proceso para la propagación de una levadura capaz de fermentar glucosa y xilosa |
| ES2713749T3 (es) | 2016-02-22 | 2019-05-23 | Versalis Spa | Proceso para propagar una levadura capaz de fermentar glucosa y xilosa |
| WO2018053058A1 (en) | 2016-09-14 | 2018-03-22 | Danisco Us Inc. | Lignocellulosic biomass fermentation-based processes |
| CN110381746B (zh) | 2016-12-21 | 2023-12-01 | 杜邦营养生物科学有限公司 | 使用热稳定丝氨酸蛋白酶的方法 |
| JP2019103416A (ja) | 2017-12-11 | 2019-06-27 | 川崎重工業株式会社 | セルロース系バイオマスを原料とする酵素法による糖化液製造方法 |
| CN112367853A (zh) | 2018-05-10 | 2021-02-12 | 彗星生物炼制公司 | 含有葡萄糖和半纤维素的组合物及其用途 |
| RU2735429C1 (ru) * | 2019-12-06 | 2020-11-02 | Федеральное государственное бюджетное научное учреждение "Всероссийский научно-исследовательский институт сельскохозяйственной микробиологии" | Бактериальное удобрение |
| IT202100031070A1 (it) | 2021-12-10 | 2023-06-10 | Versalis Spa | Procedimento per l’idratazione di lieviti in forma disidratata. |
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| US4578353A (en) * | 1982-07-19 | 1986-03-25 | St. Lawrence Reactors Limited | Fermentation of glucose with recycle of non-fermented components |
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| FR2609046B1 (fr) * | 1986-12-30 | 1989-07-13 | Bourgogne Biodyne | Procede de production d'ethanol en continu par hydrolyse a froid et fermentation simultanees d'un substrat amylace broye |
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| PL1828373T3 (pl) * | 2004-11-29 | 2012-01-31 | Inbicon As | Hydroliza enzymatyczna biomas o dużej zawartości suchej masy (SM) |
| BRPI0500534A (pt) * | 2005-02-15 | 2006-10-10 | Oxiteno Sa Ind E Comercio | processo de hidrólise ácida de materiais celulósicos e lignocelulósicos, vaso de digestão e reator de hidrólise |
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| WO2007120210A2 (en) * | 2005-11-23 | 2007-10-25 | Natureworks Llc | Process for fractionating lignocellulosic biomass into liquid and solid products |
| JP4788578B2 (ja) * | 2006-11-30 | 2011-10-05 | 王子製紙株式会社 | キシロオリゴ糖の製造方法 |
| WO2008115891A2 (en) * | 2007-03-16 | 2008-09-25 | Weyerhaeuser Company | Systems and methods for enzymatic hydrolysis of lignocellulosic materials |
| JP5425766B2 (ja) * | 2007-06-20 | 2014-02-26 | ナーガルジュナ エナジー プライベート リミテッド | セルロースの糖化プロセスおよびリアクタ |
| WO2009095781A1 (en) * | 2008-02-01 | 2009-08-06 | Inbicon A/S | Methods for reducing enzyme consumption in second generation bioethanol fermentation in the presence of lignin |
| JP2009189250A (ja) * | 2008-02-12 | 2009-08-27 | Honda Motor Co Ltd | リグノセルロースの糖化方法 |
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