MX2015015187A - Metodo de produccion de azucar sin refinar y etanol usando fermentacion selectiva. - Google Patents

Metodo de produccion de azucar sin refinar y etanol usando fermentacion selectiva.

Info

Publication number
MX2015015187A
MX2015015187A MX2015015187A MX2015015187A MX2015015187A MX 2015015187 A MX2015015187 A MX 2015015187A MX 2015015187 A MX2015015187 A MX 2015015187A MX 2015015187 A MX2015015187 A MX 2015015187A MX 2015015187 A MX2015015187 A MX 2015015187A
Authority
MX
Mexico
Prior art keywords
sugar
condensed
production method
ethanol production
sugar solution
Prior art date
Application number
MX2015015187A
Other languages
English (en)
Inventor
Satoshi Ohara
Kazutoshi Kitai
Hidenori Hidaka
Megumi Shioura
Yosuke Hamada
Original Assignee
Asahi Group Holdings Ltd
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 Asahi Group Holdings Ltd filed Critical Asahi Group Holdings Ltd
Publication of MX2015015187A publication Critical patent/MX2015015187A/es

Links

Classifications

    • 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
    • C—CHEMISTRY; METALLURGY
    • C13—SUGAR INDUSTRY
    • C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B20/00—Purification of sugar juices
    • C13B20/16—Purification of sugar juices by physical means, e.g. osmosis or filtration
    • C13B20/165—Purification of sugar juices by physical means, e.g. osmosis or filtration using membranes, e.g. osmosis, ultrafiltration
    • C—CHEMISTRY; METALLURGY
    • C13—SUGAR INDUSTRY
    • C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B25/00—Evaporators or boiling pans specially adapted for sugar juices; Evaporating or boiling sugar juices
    • C—CHEMISTRY; METALLURGY
    • C13—SUGAR INDUSTRY
    • C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
    • C13B30/02—Crystallisation; Crystallising apparatus
    • C—CHEMISTRY; METALLURGY
    • C13—SUGAR INDUSTRY
    • C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B35/00—Extraction of sucrose from molasses
    • C13B35/005—Extraction of sucrose from molasses using microorganisms or enzymes
    • C—CHEMISTRY; METALLURGY
    • C13—SUGAR INDUSTRY
    • C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B50/00—Sugar products, e.g. powdered, lump or liquid sugar; Working-up of sugar
    • C13B50/006—Molasses; Treatment of molasses
    • 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
    • C—CHEMISTRY; METALLURGY
    • C13—SUGAR INDUSTRY
    • C13K—SACCHARIDES OBTAINED FROM NATURAL SOURCES OR BY HYDROLYSIS OF NATURALLY OCCURRING DISACCHARIDES, OLIGOSACCHARIDES OR POLYSACCHARIDES
    • C13K11/00—Fructose
    • 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
    • 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)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biochemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Microbiology (AREA)
  • General Engineering & Computer Science (AREA)
  • Biotechnology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Genetics & Genomics (AREA)
  • Emergency Medicine (AREA)
  • Food Science & Technology (AREA)
  • Water Supply & Treatment (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

La presente invención maneja la cuestión de proporcionar un método de producción de azúcar sin refinar y etanol donde la sacarosa no se descompone fácilmente durante fermentación de una solución de azúcar, el rendimiento de azúcar sin refinar es alta y el rendimiento de etanol es también alto. Una solución a la cuestión es un método de producción de azúcar sin refinar y etanol que incluyen: una etapa en la cual se calienta una solución de azúcar derivada de planta y refinada; una etapa en la cual se condensa la solución de azúcar refinada a un valor Brix de 15-50% una etapa en la cual la solución de azúcar condensada es enfriada a temperatura de fermentación, una etapa en la cual el contenido de azúcar no sacarosa en la solución de azúcar condensada es convertida selectivamente a etanol por fermentar la solución de azúcar condensada y una etapa en la cual el líquido de fermentación es condensado.
MX2015015187A 2013-05-28 2014-05-14 Metodo de produccion de azucar sin refinar y etanol usando fermentacion selectiva. MX2015015187A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2013112078 2013-05-28
PCT/JP2014/062861 WO2014192546A1 (ja) 2013-05-28 2014-05-14 選択的発酵方法による粗糖及びエタノールの製造方法

Publications (1)

Publication Number Publication Date
MX2015015187A true MX2015015187A (es) 2016-02-22

Family

ID=51988581

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2015015187A MX2015015187A (es) 2013-05-28 2014-05-14 Metodo de produccion de azucar sin refinar y etanol usando fermentacion selectiva.

Country Status (10)

Country Link
US (1) US20160108437A1 (es)
JP (1) JP5909598B2 (es)
CN (1) CN105247061A (es)
AU (1) AU2014272231B2 (es)
BR (1) BR112015028134A2 (es)
MX (1) MX2015015187A (es)
PH (1) PH12015502670B1 (es)
TW (1) TWI631216B (es)
WO (1) WO2014192546A1 (es)
ZA (1) ZA201508319B (es)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102406826B1 (ko) * 2016-03-17 2022-06-10 교와 핫꼬 바이오 가부시키가이샤 환원형 글루타티온의 결정 및 그 제조 방법
PL3392352T3 (pl) * 2017-04-21 2021-05-31 Co.Pro.B. Soc. Coop. Agricola Proces przygotowania cukru surowego z buraków cukrowych
CN110327647B (zh) * 2019-07-19 2021-12-10 张兵 一种改进型三塔三效的粗甲醇精制工艺方法

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3994743A (en) * 1965-07-01 1976-11-30 Paley Lewis A Clarification and treatment of sugar juice
JPS593196B2 (ja) * 1980-03-17 1984-01-23 日揮株式会社 アルコ−ル製造方法
JPS57189693A (en) * 1981-05-19 1982-11-22 Sumitomo Heavy Ind Ltd Concentrating method of mash and evaporating and separating method of alcohol
JPH07112436B2 (ja) * 1992-06-17 1995-12-06 新エネルギー・産業技術総合開発機構 繰り返し回分発酵法によるアルコールの製造法
ZA200507940B (en) * 2003-04-07 2007-03-28 Asahi Breweries Ltd Process for producing sugar and useful substance
JP3769734B2 (ja) * 2003-04-07 2006-04-26 アサヒビール株式会社 砂糖及び有用物質を製造する方法
JP4038577B2 (ja) * 2005-04-28 2008-01-30 国立大学法人 熊本大学 アルコール生産システムおよびアルコール生産方法
US8460725B2 (en) * 2008-09-16 2013-06-11 Asahi Group Holdings, Ltd. Method for producing sugar
JP2010246435A (ja) * 2009-04-14 2010-11-04 Nippon Steel Engineering Co Ltd エタノール製造方法
JP2011045277A (ja) * 2009-08-26 2011-03-10 Toshiba Corp セルロース系エタノール生産システムおよび生産方法
US20120220005A1 (en) * 2009-09-02 2012-08-30 The University Of Tokushima Method for producing ethanol from lignocellulosic biomass
JP2011109956A (ja) * 2009-11-26 2011-06-09 Asahi Breweries Ltd 砂糖の製造方法
WO2012011285A1 (ja) * 2010-07-22 2012-01-26 新日鉄エンジニアリング株式会社 エタノール製造装置及びエタノール製造方法
JP2013135615A (ja) * 2011-12-28 2013-07-11 Ihi Corp バイオマス糖化方法
EP2896699A4 (en) * 2012-09-14 2016-04-13 Asahi Group Holdings Ltd METHOD FOR THE PRODUCTION OF SUGAR AND ETHANOL BY SELECTIVE FERMENTATION

Also Published As

Publication number Publication date
TWI631216B (zh) 2018-08-01
BR112015028134A2 (pt) 2017-07-25
JPWO2014192546A1 (ja) 2017-02-23
TW201512402A (zh) 2015-04-01
AU2014272231A1 (en) 2015-11-26
JP5909598B2 (ja) 2016-04-26
US20160108437A1 (en) 2016-04-21
PH12015502670A1 (en) 2016-03-07
ZA201508319B (en) 2017-01-25
CN105247061A (zh) 2016-01-13
AU2014272231B2 (en) 2016-07-07
WO2014192546A1 (ja) 2014-12-04
PH12015502670B1 (en) 2016-03-07

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