HRP20211743T1 - Hidrotermalno-mehanička pretvorba lignocelulozne biomase u etanol ili druge produkte fermentacije - Google Patents
Hidrotermalno-mehanička pretvorba lignocelulozne biomase u etanol ili druge produkte fermentacije Download PDFInfo
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- HRP20211743T1 HRP20211743T1 HRP20211743TT HRP20211743T HRP20211743T1 HR P20211743 T1 HRP20211743 T1 HR P20211743T1 HR P20211743T T HRP20211743T T HR P20211743TT HR P20211743 T HRP20211743 T HR P20211743T HR P20211743 T1 HRP20211743 T1 HR P20211743T1
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- cellulose
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- digester
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- 238000000855 fermentation Methods 0.000 title claims 8
- 230000004151 fermentation Effects 0.000 title claims 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims 6
- 238000006243 chemical reaction Methods 0.000 title claims 5
- 239000002029 lignocellulosic biomass Substances 0.000 title claims 5
- 238000000034 method Methods 0.000 claims 26
- 229920002678 cellulose Polymers 0.000 claims 21
- 239000001913 cellulose Substances 0.000 claims 21
- 239000007790 solid phase Substances 0.000 claims 11
- 230000007071 enzymatic hydrolysis Effects 0.000 claims 10
- 238000006047 enzymatic hydrolysis reaction Methods 0.000 claims 10
- 238000007670 refining Methods 0.000 claims 9
- 239000007787 solid Substances 0.000 claims 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 8
- 239000000203 mixture Substances 0.000 claims 7
- 235000000346 sugar Nutrition 0.000 claims 7
- 150000008163 sugars Chemical class 0.000 claims 7
- 239000002994 raw material Substances 0.000 claims 6
- 229920002488 Hemicellulose Polymers 0.000 claims 5
- 238000004821 distillation Methods 0.000 claims 5
- 230000007062 hydrolysis Effects 0.000 claims 4
- 238000006460 hydrolysis reaction Methods 0.000 claims 4
- 230000003301 hydrolyzing effect Effects 0.000 claims 4
- 239000007788 liquid Substances 0.000 claims 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims 3
- 240000008042 Zea mays Species 0.000 claims 3
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 claims 3
- 235000002017 Zea mays subsp mays Nutrition 0.000 claims 3
- 235000005822 corn Nutrition 0.000 claims 3
- 239000007791 liquid phase Substances 0.000 claims 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims 2
- 108010059892 Cellulase Proteins 0.000 claims 2
- 229920003043 Cellulose fiber Polymers 0.000 claims 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims 2
- 240000000111 Saccharum officinarum Species 0.000 claims 2
- 235000007201 Saccharum officinarum Nutrition 0.000 claims 2
- 239000002253 acid Substances 0.000 claims 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 claims 2
- 238000004140 cleaning Methods 0.000 claims 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 claims 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims 2
- 239000002245 particle Substances 0.000 claims 2
- 238000011144 upstream manufacturing Methods 0.000 claims 2
- 241000609240 Ambelania acida Species 0.000 claims 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 claims 1
- 239000010905 bagasse Substances 0.000 claims 1
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 claims 1
- 230000006835 compression Effects 0.000 claims 1
- 238000007906 compression Methods 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 claims 1
- 239000000835 fiber Substances 0.000 claims 1
- 238000000227 grinding Methods 0.000 claims 1
- 239000011121 hardwood Substances 0.000 claims 1
- 239000003112 inhibitor Substances 0.000 claims 1
- 239000004310 lactic acid Substances 0.000 claims 1
- 235000014655 lactic acid Nutrition 0.000 claims 1
- 229920005610 lignin Polymers 0.000 claims 1
- 238000002203 pretreatment Methods 0.000 claims 1
- 238000004064 recycling Methods 0.000 claims 1
- 239000011122 softwood Substances 0.000 claims 1
- 239000010902 straw Substances 0.000 claims 1
- 238000005406 washing Methods 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
- 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
- C12P7/14—Multiple stages of fermentation; Multiple types of microorganisms or re-use of microorganisms
-
- 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
-
- 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
- D21C3/00—Pulping cellulose-containing materials
-
- 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
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
-
- 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
-
- 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
- C12P2203/00—Fermentation products obtained from optionally pretreated or hydrolyzed cellulosic or lignocellulosic material as the carbon source
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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
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Wood Science & Technology (AREA)
- Biotechnology (AREA)
- Zoology (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Microbiology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Genetics & Genomics (AREA)
- Emergency Medicine (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Processing Of Solid Wastes (AREA)
- Saccharide Compounds (AREA)
Claims (17)
1. Postupak proizvodnje produkta fermentacije iz lignocelulozne biomase, gdje se navedeni postupak sastoji u:
(a) dodavanju osnovne sirovine za lignoceluloznu biomasu u jednostadijski digestor, pri čemu navedena osnovna sirovina sadrži celulozu, hemicelulozu, te lignin;
(b) izlaganju navedene osnovne sirovine reakcijskoj otopini koja sadrži vodenu paru ili tekuću vruću vodu u navedenom digestoru, radi solubiliziranja barem dijela navedene hemiceluloze u tekućoj fazi i radi dobivanja čvrste faze bogate celulozom;
(c) rafiniranju navedene čvrste faze bogate celulozom, zajedno s navedenom tekućom fazom, u mehaničkom rafinatoru radi smanjivanja prosječne veličine čestica navedene čvrste faze bogate celulozom, čime se dobije smjesu koja sadrži rafinirane krutine bogate celulozom i navedenu tekuću fazu;
(d) enzimskoj hidrolizi navedene smjese u hidrolitičkom reaktoru s enzimima celulazama kako bi se dobilo fermentabilne šećere iz navedene smjese, pri čemu navedeni hidrolitički reaktor uključuje jedan ili više stadija hidrolize; i
(e) fermentiranju barem dijela navedenih fermentabilnih šećera u fermentoru kako bi se proizvelo produkt fermentacije.
2. Postupak u skladu s patentnim zahtjevom 1, pri čemu:
(i) navedenu osnovnu sirovinu za lignoceluloznu biomasu se bira iz skupine koju čine tvrdo drvo, meko drvo, bagasa od šećerne trske, slama od šećerne trske, energetska trska, kukuruzno krmivo, kukuruzni klipovi, kukuruzno vlakno, te njihove kombinacije; ili
(ii) navedenu osnovnu sirovinu za lignoceluloznu biomasu se predobrađuje, prije koraka (a), uz pomoć jedne ili više tehnika koje se bira iz skupine koju čine čišćenje, pranje, predobrada vodenom parom, sušenje, mljevenje, klasiranje čestica po veličini, te njihove kombinacije.
3. Postupak u skladu s patentnim zahtjevom 1, pri čemu se barem dio navedene reakcijske otopine dodaje u navedenu osnovnu sirovinu u predimpregnatoru prije koraka (b) ili pri čemu navedena reakcijska otopina dodatno sadrži kiselinu, pri čemu navedena kiselina može biti octena kiselina.
4. Postupak u skladu s patentnim zahtjevom 1, pri čemu se navedena reakcijska otopina sastoji od vodene pare ili tekuće vruće vode.
5. Postupak u skladu s patentnim zahtjevom 1, pri čemu korak (b) uključuje:
(i) vrijeme boravka u digestoru od otprilike 2 minute do otprilike 4 sati, pri čemu je po mogućnosti navedeno vrijeme boravka u digestoru otprilike 10 minuta ili kraće; ili
(ii) temperaturu digestora od otprilike 150 °C do otprilike 220 °C, pri čemu je po mogućnosti navedena temperatura digestora od otprilike 180 °C do otprilike 200 °C.
6. Postupak u skladu s patentnim zahtjevom 1, pri čemu se korak (b):
(i) provodi uz težinski omjer tekućina-krutina u digestoru od otprilike 1 do otprilike 4, pri čemu je po mogućnosti navedeni težinski omjer tekućina-krutina u digestoru otprilike 2 ili manji; ili
(ii) provodi kod pH digestora od otprilike 3 do otprilike 5, pri čemu je po mogućnosti navedeni pH digestora od otprilike 3,5 do otprilike 4,5.
7. Postupak u skladu s patentnim zahtjevom 1, gdje se u navedenom postupku upotrebljava ispusni spremnik konfiguriran za prihvat navedene čvrste faze bogate celulozom ili navedenih rafiniranih krutina bogatih celulozom pod tlakom nižim od tlaka u digestoru, pri čemu se navedeni ispusni spremnik može nalaziti nizvodno od navedenog digestora i uzvodno ili nizvodno od navedenog mehaničkog rafinatora ili pri čemu vodena para je odvojena od navedenog ispusnog spremnika, pri čemu po mogućnosti se toplinu rekuperira iz barem dijela navedene vodene pare ili pri čemu se barem dio navedene vodene pare kondenzira ili stlači, te vrati u navedeni digestor.
8. Postupak u skladu s patentnim zahtjevom 1, pri čemu se prvi ispusni spremnik nalazi uzvodno od navedenog mehaničkog rafinatora, a drugi ispusni spremnik se nalazi nizvodno od navedenog mehaničkog rafinatora.
9. Postupak u skladu s patentnim zahtjevom 1, pri čemu:
(i) navedeni mehanički rafinator radi pod rafinacijskim tlakom kojeg se bira od otprilike 1 bar (100 kPa) do otprilike 20 bara (2 MPa), pri čemu je po mogućnosti navedeni rafinacijski tlak otprilike 3 bara (300 kPa) ili manji, pri čemu navedeni mehanički rafinator može raditi pod ili pod otprilike atmosferskim tlakom; ili
(ii) navedeni mehanički rafinator radi pod električnim opterećenjem od otprilike 2 kW do otprilike 50 kW rafinacijske snage po toni navedene čvrste faze bogate celulozom, pri čemu po mogućnosti navedeni mehanički rafinator radi pod električnim opterećenjem od otprilike 5 kW do otprilike 20 kW rafinacijske snage po toni navedene čvrste faze bogate celulozom; ili
(iii) navedeni mehanički rafinator prenosi do otprilike 500 kWh rafinacijske energije po toni navedene čvrste faze bogate celulozom, pri čemu po mogućnosti navedeni mehanički rafinator prenosi od otprilike 50 kWh do otprilike 200 kWh rafinacijske energije po toni navedene čvrste faze bogate celulozom.
10. Postupak u skladu s patentnim zahtjevom 1, gdje se navedeni postupak sastoji u upotrebi više mehaničkih rafinatora u različitim segmentima navedenog postupka, gdje navedeni postupak može uključivati, između koraka (c) i (d), transportiranje barem dijela navedene smjese u drugi mehanički rafinator koji radi pod nižim rafinacijskim tlakom u usporedbi s onim u navedenom mehaničkom rafinatoru u koraku (c), pri čemu po mogućnosti navedeni mehanički rafinator u koraku (c) je rafinator pod povišenim tlakom, a navedeni drugi mehanički rafinator je rafinator pod atmosferskim tlakom.
11. Postupak u skladu s patentnim zahtjevom 1, pri čemu:
(i) korak (d) upotrebljava više reaktora za enzimsku hidrolizu;
(ii) korak (d) upotrebljava enzimsku hidrolizu u jednom stadiju konfiguriranu za likvefakciju celuloze i saharificiranje, pri čemu navedena enzimska hidroliza u jednom stadiju uključuje jedan ili više spremnika ili posuda; ili
(iii) korak (d) upotrebljava enzimsku hidrolizu u više stadija konfiguriranu za likvefakciju celuloze za kojom slijedi saharificiranje, pri čemu svaki stadij uključuje jedan ili više spremnika ili posuda, gdje navedeni postupak može dodatno uključivati dodatno mehaničko rafiniranje navedene smjese, ili njezina djelomično hidrolizirane varijante, nakon barem prvog stadija enzimske hidrolize, ili navedeni postupak dodatno uključuje:
dodavanje navedene smjese u prvi reaktor za enzimsku hidrolizu u djelotvornim uvjetima hidrolize kako bi se proizvelo tekući hidrolizat koji sadrži šećere iz navedenih rafiniranih krutina bogatih celulozom i izborno iz navedene hemiceluloze, te preostale čvrste faze bogate celulozom;
izborno odvajanje barem dijela navedenog tekućeg hidrolizata od navedene preostale čvrste faze bogate celulozom;
transportiranje navedene preostale čvrste faze bogate celulozom kroz dodatni mehanički rafinator i/ili recikliranje navedene preostale čvrste faze bogate celulozom kroz navedeni mehanički rafinator kako bi se dobilo rafinirane preostale krutine bogate celulozom; i
dodavanje navedenih rafiniranih preostalih krutina bogatih celulozom u drugi reaktor za enzimsku hidrolizu u djelotvornim uvjetima hidrolize kako bi se proizvelo dodatne šećere.
12. Postupak u skladu s patentnim zahtjevom 1, pri čemu se nizvodno od navedenog hidrolitičkog reaktora nalazi samočisteći filtar radi uklanjanja sukova celuloznih vlakana, pri čemu se navedene sukove celuloznih vlakana može reciklirati natrag u navedeni hidrolitički reaktor.
13. Postupak u skladu s patentnim zahtjevom 1, pri čemu se enzime celulaze dodaje izravno u navedeni mehanički rafinator ili u navedenu čvrstu fazu bogatu celulozom prije koraka (c), pri čemu navedeni mehanički rafinator može raditi na maksimalnoj temperaturi od 75 °C ili nižoj radi održavanja djelotvornih uvjeta hidrolize.
14. Postupak u skladu s patentnim zahtjevom 1, pri čemu korak (d) uključuje enzimsku hidrolizu hemiceluloznih oligomera kako bi se dobilo fermentabilne monomerne šećere, ili korak (e) uključuje enzimsku hidrolizu hemiceluloznih oligomera kako bi se dobilo fermentabilne monomerne šećere u navedenom fermentoru, izborno pri čemu se barem dio navedenih fermentabilnih monomernih šećera također fermentira kako bi se proizvelo navedeni produkt fermentacije.
15. Postupak u skladu s patentnim zahtjevom 1, gdje navedeni postupak dodatno uključuje:
(i) uklanjanje jednog ili više inhibitora fermentacije; ili
(ii) koncentriranje navedenog produkta fermentacije destiliranjem, pri čemu navedeno destiliranje može stvarati struju ostataka destilacije, te pri čemu se navedenu struju ostataka destilacije isparava u isparivaču ostatka destilacije koji je isparivač s mehaničkom kompresijom vodene pare ili je integriran u niz isparivača mnogostrukog učinka.
16. Postupak u skladu s patentnim zahtjevom 1, pri čemu se navedeni mehanički rafinator bira iz skupine koju čine rafinator s vrućim puhanjem, rafinator s vrućom šaržom, rafinator s linijom za puhanje, disk rafinator, stožasti rafinator, valjkasti rafinator, linijski defibrator, ekstruder, homogenizator, te njihove kombinacije.
17. Postupak u skladu s patentnim zahtjevom 1, pri čemu se navedeni produkt fermentacije bira iz skupine koju čine etanol, izopropanol, aceton, n-butanol, izobutanol, 1,4-butandiol, jantarna kiselina, mliječna kiselina, te njihove kombinacije, pri čemu je po mogućnosti navedeni produkt fermentacije etanol.
Applications Claiming Priority (10)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201562118335P | 2015-02-19 | 2015-02-19 | |
| US201562141664P | 2015-04-01 | 2015-04-01 | |
| US201562150643P | 2015-04-21 | 2015-04-21 | |
| US201562197160P | 2015-07-27 | 2015-07-27 | |
| US201562240461P | 2015-10-12 | 2015-10-12 | |
| US201562263292P | 2015-12-04 | 2015-12-04 | |
| US201562267533P | 2015-12-15 | 2015-12-15 | |
| US15/047,608 US20160244788A1 (en) | 2015-02-19 | 2016-02-18 | Hydrothermal-mechanical conversion of lignocellulosic biomass to ethanol or other fermentation products |
| EP16753095.5A EP3259360B1 (en) | 2015-02-19 | 2016-02-19 | Hydrothermal-mechanical conversion of lignocellulosic biomass to ethanol or other fermentation products |
| PCT/US2016/018556 WO2016134195A1 (en) | 2015-02-19 | 2016-02-19 | Hydrothermal-mechanical conversion of lignocellulosic biomass to ethanol or other fermentation products |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| HRP20211743T1 true HRP20211743T1 (hr) | 2022-02-04 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| HRP20211743TT HRP20211743T1 (hr) | 2015-02-19 | 2016-02-19 | Hidrotermalno-mehanička pretvorba lignocelulozne biomase u etanol ili druge produkte fermentacije |
Country Status (15)
| Country | Link |
|---|---|
| US (6) | US20160244788A1 (hr) |
| EP (2) | EP3259360B1 (hr) |
| CN (1) | CN107532183A (hr) |
| BR (1) | BR112016022614B1 (hr) |
| CA (1) | CA3015090A1 (hr) |
| DK (1) | DK3259360T3 (hr) |
| ES (1) | ES2898874T3 (hr) |
| HR (1) | HRP20211743T1 (hr) |
| HU (1) | HUE057204T2 (hr) |
| LT (1) | LT3259360T (hr) |
| PL (1) | PL3259360T3 (hr) |
| PT (1) | PT3259360T (hr) |
| RS (1) | RS62648B1 (hr) |
| SI (1) | SI3259360T1 (hr) |
| WO (1) | WO2016134195A1 (hr) |
Families Citing this family (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB201706831D0 (en) * | 2017-04-28 | 2017-06-14 | Fiberight Ltd | Hydrolysis |
| FR3069248B1 (fr) * | 2017-07-19 | 2020-07-31 | Ifp Energies Now | Procede de traitement de biomasse ligno-cellulosique . |
| IT201700098245A1 (it) * | 2017-09-01 | 2019-03-01 | Water & Soil Remediation S R L | Processo e impianto per il trattamento di biomasse lignocellulosiche. |
| US11229226B2 (en) * | 2018-05-06 | 2022-01-25 | Superbrewed Food, Inc. | Aqueous fermentation feedstock and a method for the production thereof |
| CN113163828B (zh) | 2018-08-15 | 2024-04-26 | 剑桥糖质科学有限公司 | 新型组合物、其用途及其形成方法 |
| JP2022509363A (ja) | 2018-10-24 | 2022-01-20 | ワグラー，ティモシー | 化学機械的細胞爆砕のためのプロセス、方法、およびシステム、ならびにこれにより製造された固体製品および液体製品 |
| SE542682C2 (en) * | 2018-10-31 | 2020-06-23 | Valmet Oy | A discharge screw arrangement for discharging lignocellulosic material from a lignocellulosic treatment reactor |
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- 2016-02-19 HU HUE16753095A patent/HUE057204T2/hu unknown
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| RS62648B1 (sr) | 2021-12-31 |
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| US10557154B2 (en) | 2020-02-11 |
| US20180237806A1 (en) | 2018-08-23 |
| PL3259360T3 (pl) | 2022-01-31 |
| US10344303B2 (en) | 2019-07-09 |
| LT3259360T (lt) | 2021-12-27 |
| BR112016022614B1 (pt) | 2024-01-30 |
| CA3015090A1 (en) | 2016-08-25 |
| US20200172939A1 (en) | 2020-06-04 |
| CN107532183A (zh) | 2018-01-02 |
| US20190360006A1 (en) | 2019-11-28 |
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