RU2014133168A - Способ получения химического вещества - Google Patents

Способ получения химического вещества Download PDF

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RU2014133168A
RU2014133168A RU2014133168A RU2014133168A RU2014133168A RU 2014133168 A RU2014133168 A RU 2014133168A RU 2014133168 A RU2014133168 A RU 2014133168A RU 2014133168 A RU2014133168 A RU 2014133168A RU 2014133168 A RU2014133168 A RU 2014133168A
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chemical product
fermentation
pentose
product according
microorganism
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RU2014133168A
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RU2595387C2 (ru
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Кодзи КОБАЯСИ
Сиоми ВАТАНАБЕ
Киохей ИСОБЕ
Кендзи САВАИ
Кюнгсу НА
Синго ХИРАМАЦУ
Кацусиге ЯМАДА
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Торэй Индастриз, Инк.
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    • C12P7/02—Preparation of oxygen-containing organic compounds containing a hydroxy group
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    • C12P7/06—Ethanol, i.e. non-beverage
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    • C12P7/04—Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
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    • C12P7/02—Preparation of oxygen-containing organic compounds containing a hydroxy group
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    • C12P7/06—Ethanol, i.e. non-beverage
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    • C12P7/00—Preparation of oxygen-containing organic compounds
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    • C12P7/00—Preparation of oxygen-containing organic compounds
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    • C12P7/40—Preparation of oxygen-containing organic compounds containing a carboxyl group including Peroxycarboxylic acids
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  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Zoology (AREA)
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  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

1. Способ получения химического продукта посредством непрерывной ферментации (культивирования), включающий фильтрование суспензионной культуры микроорганизма(ов) (культуральной жидкости) через разделительную мембрану; сохранение не подвергнутой фильтрованию жидкости, или возращение не подвергнутой фильтрованию жидкости, в культуральной(ую) жидкости(ь); добавление в культуральную жидкость исходного материала для ферментации и выделение продукта в фильтрате, причем указанный микроорганизм(ы) является микроорганизмом(ами), который подвергается подавлению катаболитами, а указанный исходный материал для ферментации включает гексозу и пентозу.2. Способ получения химического продукта по п. 1, в котором концентрация указанной пентозы в общем количестве указанного фильтрата составляет не более чем 5 г/л.3. Способ получения химического продукта по п. 1 или 2, в котором весовое соотношение между гексозой и пентозой, содержащимися в указанном исходном материале для ферментации, составляет от 1:9 до 9:1.4. Способ получения химического продукта по п. 1 или 2, в котором указанный исходный материал для ферментации включает сахарный сироп, получаемый из биомассы.5. Способ получения химического продукта по п. 1 или 2, в котором указанной пентозой является ксилоза.

Claims (5)

1. Способ получения химического продукта посредством непрерывной ферментации (культивирования), включающий фильтрование суспензионной культуры микроорганизма(ов) (культуральной жидкости) через разделительную мембрану; сохранение не подвергнутой фильтрованию жидкости, или возращение не подвергнутой фильтрованию жидкости, в культуральной(ую) жидкости(ь); добавление в культуральную жидкость исходного материала для ферментации и выделение продукта в фильтрате, причем указанный микроорганизм(ы) является микроорганизмом(ами), который подвергается подавлению катаболитами, а указанный исходный материал для ферментации включает гексозу и пентозу.
2. Способ получения химического продукта по п. 1, в котором концентрация указанной пентозы в общем количестве указанного фильтрата составляет не более чем 5 г/л.
3. Способ получения химического продукта по п. 1 или 2, в котором весовое соотношение между гексозой и пентозой, содержащимися в указанном исходном материале для ферментации, составляет от 1:9 до 9:1.
4. Способ получения химического продукта по п. 1 или 2, в котором указанный исходный материал для ферментации включает сахарный сироп, получаемый из биомассы.
5. Способ получения химического продукта по п. 1 или 2, в котором указанной пентозой является ксилоза.
RU2014133168/10A 2012-01-13 2013-01-11 Способ получения химического вещества RU2595387C2 (ru)

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PCT/JP2013/050435 WO2013105651A1 (ja) 2012-01-13 2013-01-11 化学品の製造方法

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AU (1) AU2013208439B2 (ru)
BR (1) BR112014017215B8 (ru)
CA (1) CA2860756A1 (ru)
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CN104039971A (zh) * 2012-01-13 2014-09-10 东丽株式会社 化学品的制造方法
JP6303984B2 (ja) * 2014-10-31 2018-04-04 トヨタ自動車株式会社 連続培養によるエタノールの製造方法及び連続培養装置
CN110832081B (zh) * 2017-06-30 2023-06-27 东丽株式会社 基于连续发酵的化学品的制造方法及制造装置
CN109207652A (zh) * 2018-09-14 2019-01-15 许昌鑫瑞德化工科技有限公司 一种皮革化学品生产工艺
CN109207653A (zh) * 2018-09-17 2019-01-15 许昌鑫瑞德化工科技有限公司 一种皮革化学品制备方法

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CN104039971A (zh) * 2012-01-13 2014-09-10 东丽株式会社 化学品的制造方法

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CN107043791A (zh) 2017-08-15
EP2803732B1 (en) 2020-12-09
PH12014501607A1 (en) 2014-10-13
RU2595387C2 (ru) 2016-08-27
BR112014017215B8 (pt) 2021-11-03
US20140349354A1 (en) 2014-11-27
JPWO2013105651A1 (ja) 2015-05-11
WO2013105651A1 (ja) 2013-07-18
CA2860756A1 (en) 2013-07-18
ES2837800T3 (es) 2021-07-01
PH12014501607B1 (en) 2014-10-13
CN104039971A (zh) 2014-09-10
MY173716A (en) 2020-02-18
BR112014017215B1 (pt) 2021-10-13
BR112014017215A8 (pt) 2017-07-04
AU2013208439B2 (en) 2016-11-24
JP6447682B2 (ja) 2019-01-09
EP2803732A4 (en) 2015-08-26
US10378029B2 (en) 2019-08-13
EP2803732A1 (en) 2014-11-19
KR20140116844A (ko) 2014-10-06
AU2013208439A1 (en) 2014-08-21
BR112014017215A2 (pt) 2017-06-13

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