CA2144302A1 - BEI Hydrolysis Process System and Improved Process for the Continuous Hydrolysis Sacchararification of Ligno-Cellulosics in a Two-Stage Plug-Flow-Reactor System - Google Patents
BEI Hydrolysis Process System and Improved Process for the Continuous Hydrolysis Sacchararification of Ligno-Cellulosics in a Two-Stage Plug-Flow-Reactor SystemInfo
- Publication number
- CA2144302A1 CA2144302A1 CA2144302A CA2144302A CA2144302A1 CA 2144302 A1 CA2144302 A1 CA 2144302A1 CA 2144302 A CA2144302 A CA 2144302A CA 2144302 A CA2144302 A CA 2144302A CA 2144302 A1 CA2144302 A1 CA 2144302A1
- Authority
- CA
- Canada
- Prior art keywords
- hydrolysis
- flow
- alpha
- ligno
- dilute
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title abstract 6
- 230000007062 hydrolysis Effects 0.000 title abstract 4
- 238000006460 hydrolysis reaction Methods 0.000 title abstract 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 3
- 239000000413 hydrolysate Substances 0.000 abstract 3
- 235000000346 sugar Nutrition 0.000 abstract 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 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 abstract 2
- 239000002253 acid Substances 0.000 abstract 2
- 239000008103 glucose Substances 0.000 abstract 2
- -1 hexose sugars Chemical class 0.000 abstract 2
- 239000002028 Biomass Substances 0.000 abstract 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 abstract 1
- 241000006364 Torula Species 0.000 abstract 1
- 238000005903 acid hydrolysis reaction Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 238000000354 decomposition reaction Methods 0.000 abstract 1
- 239000004615 ingredient Substances 0.000 abstract 1
- 229920005610 lignin Polymers 0.000 abstract 1
- 239000002029 lignocellulosic biomass Substances 0.000 abstract 1
- 239000012263 liquid product Substances 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 150000002972 pentoses Chemical class 0.000 abstract 1
- 238000004886 process control Methods 0.000 abstract 1
- 230000035484 reaction time Effects 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000012265 solid product Substances 0.000 abstract 1
- 150000008163 sugars Chemical class 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- 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
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- General Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
The invention relates to an improved two-stage dilute-acid hydrolysis process and apparatus for the continuous saccharification of ligno-cellulosic biomass or other cellulosic material feedstocks, with higher efficiency and better economics than known-art, is disclosed. It comprises two double-tube heat-exchanger and plug-flow-reactor systems, in series . The improved process is primarily by reverse insterstage transfer-flow, opposite to biomass , of second-stage surplus of: 1 .
process heat, 2. dilute-acid and 3. ingredient and solution water, all in an alpha cellulose hydrolysate and dilute acid solution. It also comprises recycle of a fraction of unhydrolyzed alpha-cellulose hydrolysis residue, thereby achieving higher hydrolysis conversion of alpha-cellulose to glucose; and providing: 1. lower hydrolysate sugar decomposition, 2. reduced reaction time and 3. increased reactor processing capacity, without increased dimensions. The process is ideal for process control to efficiency to produce a primary final liquid product, which is the combined hydrolysate sugars into a single solution, including pentose and hexose sugars, including glucose, which are readily fermented into Ethanol and/or Torula Yeast. The final solid product is the unhydrolyzed lignin residue solids.
process heat, 2. dilute-acid and 3. ingredient and solution water, all in an alpha cellulose hydrolysate and dilute acid solution. It also comprises recycle of a fraction of unhydrolyzed alpha-cellulose hydrolysis residue, thereby achieving higher hydrolysis conversion of alpha-cellulose to glucose; and providing: 1. lower hydrolysate sugar decomposition, 2. reduced reaction time and 3. increased reactor processing capacity, without increased dimensions. The process is ideal for process control to efficiency to produce a primary final liquid product, which is the combined hydrolysate sugars into a single solution, including pentose and hexose sugars, including glucose, which are readily fermented into Ethanol and/or Torula Yeast. The final solid product is the unhydrolyzed lignin residue solids.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002144302A CA2144302C (en) | 1995-03-09 | 1995-03-09 | Bei hydrolysis process system and improved process for the continuous hydrolysis sacchararification of ligno-cellulosics in a two-stage plug-flow-reactor system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002144302A CA2144302C (en) | 1995-03-09 | 1995-03-09 | Bei hydrolysis process system and improved process for the continuous hydrolysis sacchararification of ligno-cellulosics in a two-stage plug-flow-reactor system |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2144302A1 true CA2144302A1 (en) | 1996-09-10 |
CA2144302C CA2144302C (en) | 1998-06-16 |
Family
ID=4155395
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002144302A Expired - Fee Related CA2144302C (en) | 1995-03-09 | 1995-03-09 | Bei hydrolysis process system and improved process for the continuous hydrolysis sacchararification of ligno-cellulosics in a two-stage plug-flow-reactor system |
Country Status (1)
Country | Link |
---|---|
CA (1) | CA2144302C (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1793944A1 (en) * | 2004-09-30 | 2007-06-13 | Iogen Energy Corporation | Continuous flowing pre-treatment system with steam recovery |
WO2010011675A1 (en) * | 2008-07-23 | 2010-01-28 | Novozymes A/S | Methods for producing charcoal and uses thereof |
-
1995
- 1995-03-09 CA CA002144302A patent/CA2144302C/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1793944A1 (en) * | 2004-09-30 | 2007-06-13 | Iogen Energy Corporation | Continuous flowing pre-treatment system with steam recovery |
EP1793944A4 (en) * | 2004-09-30 | 2011-12-07 | Iogen Energy Corp | Continuous flowing pre-treatment system with steam recovery |
WO2010011675A1 (en) * | 2008-07-23 | 2010-01-28 | Novozymes A/S | Methods for producing charcoal and uses thereof |
Also Published As
Publication number | Publication date |
---|---|
CA2144302C (en) | 1998-06-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5188673A (en) | Concentrated sulfuric acid process for converting lignocellulosic materials to sugars | |
US5411594A (en) | Bei hydrolysis process system an improved process for the continuous hydrolysis saccharification of ligno-cellulosics in a two-stage plug-flow-reactor system | |
CN101743257B (en) | Combined thermochemical pretreatment and refining of lignocellulosic biomass | |
US5125977A (en) | Two-stage dilute acid prehydrolysis of biomass | |
US4376163A (en) | Process for producing ethanol by continuous fermentation of polysaccharide-containing raw materials | |
CA2158430A1 (en) | Method of producing sugars using strong acid hydrolysis of cellulosic and hemicellulosic materials | |
WO2008017145A1 (en) | Process for recovery of holocellulose and near-native lignin from biomass | |
EP3094734B1 (en) | Process for fractionation of oligosaccharides from agri-waste | |
Dale et al. | Enzymatic simultaneous saccharification and fermentation (SSF) of biomass to ethanol in a pilot 130 liter multistage continuous reactor separator | |
US20240175060A1 (en) | Processes for co-producing xylitol with ethanol or other fermentation products | |
CA2144302A1 (en) | BEI Hydrolysis Process System and Improved Process for the Continuous Hydrolysis Sacchararification of Ligno-Cellulosics in a Two-Stage Plug-Flow-Reactor System | |
Leathers et al. | Xylitol production from corn fibre hydrolysates by a two-stage fermentation process | |
EP2167672B1 (en) | Process for the fermentative production of ethanol from a hemicellulose hydrolysate derived from sugarcane bagasse employing Pichia stipitis | |
Viikari et al. | Rate and yield limiting factors in continuous fermentation of sucrose by Zymomonas mobilis | |
CN101497896B (en) | Method for preparing ethanol from wood fiber raw material | |
Brelsford | Bei hydrolysis process system an improved process for the continuous hydrolysis saccharification of lignocellulosics in a two-stage plug-flow-reactor system | |
Nancib et al. | Statistical optimization of dilute acid hydrolysis of wood sawdust for lactic acid production | |
KR100968439B1 (en) | Development of a novel process and equipment of the fractionation and saccharification of biomass | |
US4235968A (en) | Saccharification of cellulose | |
Zeikus et al. | Utilizing fermentation as a processing alternative | |
US20150125917A1 (en) | D(-) lactic acid production | |
AU5701796A (en) | Process for the production of ethanol | |
US20110104772A1 (en) | Method of Cultivating Yeast for Enhancing Pentitol Production | |
Deverell et al. | Induced flocculation of Pachysolen tannophilus using the tower fermentor | |
ES8702327A1 (en) | CONVERSION OF SUCROSE TO ETHANOL USING THE BACTERIUM -i(ZYMOMONAS MOBILIS). |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKLA | Lapsed |