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 System

Info

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
Application number
CA2144302A
Other languages
French (fr)
Other versions
CA2144302C (en
Inventor
Donald L. Brelsford
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BRELSFORD ENGINEERING Inc
Original Assignee
Donald L. Brelsford
Brelsford Engineering, Inc.
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Donald L. Brelsford, Brelsford Engineering, Inc. filed Critical Donald L. Brelsford
Priority to CA002144302A priority Critical patent/CA2144302C/en
Publication of CA2144302A1 publication Critical patent/CA2144302A1/en
Application granted granted Critical
Publication of CA2144302C publication Critical patent/CA2144302C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13KSACCHARIDES OBTAINED FROM NATURAL SOURCES OR BY HYDROLYSIS OF NATURALLY OCCURRING DISACCHARIDES, OLIGOSACCHARIDES OR POLYSACCHARIDES
    • C13K1/00Glucose; Glucose-containing syrups
    • C13K1/02Glucose; Glucose-containing syrups obtained by saccharification of cellulosic materials

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Emergency Medicine (AREA)
  • General Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (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.
CA002144302A 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 Expired - Fee Related CA2144302C (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (3)

* Cited by examiner, † Cited by third party
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
CA2158430A1 (en) Method of producing sugars using strong acid hydrolysis of cellulosic and hemicellulosic materials
WO1998014270A1 (en) Hydrolysis and fractionation of lignocellulosic 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
US20230121068A1 (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
Afschar et al. Bacterial conversion of molasses to acetone and butanol
KR100968439B1 (en) Development of a novel process and equipment of the fractionation and saccharification of biomass
Zeikus et al. Utilizing fermentation as a processing alternative
US8278078B2 (en) Method of cultivating yeast for enhancing pentitol production
AU2013255835A1 (en) D(-) lactic acid production
AU5701796A (en) Process for the production of ethanol
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).
Beck Study of bioconversion of dilute acid hydrolyzates of hardwood to ethanol.[Pachysolen tannophilus, Saccharomyces uvarum, S. cerevisiae, S. carlsbergenesis]
US20110003354A1 (en) Method for converting herbaceous plant fibers into fuel alcohol
Wilke Cellulose, food and energy

Legal Events

Date Code Title Description
EEER Examination request
MKLA Lapsed