AR013797A1 - Procedimiento para producir un complemento de alimentacion de l-lisina granular con una cantidad ajustable de pureza de l-lisina - Google Patents

Procedimiento para producir un complemento de alimentacion de l-lisina granular con una cantidad ajustable de pureza de l-lisina

Info

Publication number
AR013797A1
AR013797A1 ARP980106270A ARP980106270A AR013797A1 AR 013797 A1 AR013797 A1 AR 013797A1 AR P980106270 A ARP980106270 A AR P980106270A AR P980106270 A ARP980106270 A AR P980106270A AR 013797 A1 AR013797 A1 AR 013797A1
Authority
AR
Argentina
Prior art keywords
lysine
lisine
purity
supplement
dryer
Prior art date
Application number
ARP980106270A
Other languages
English (en)
Original Assignee
Archer Daniels Midland Co
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=25536926&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=AR013797(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Archer Daniels Midland Co filed Critical Archer Daniels Midland Co
Publication of AR013797A1 publication Critical patent/AR013797A1/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
    • C12P13/00—Preparation of nitrogen-containing organic compounds
    • C12P13/04—Alpha- or beta- amino acids
    • C12P13/08—Lysine; Diaminopimelic acid; Threonine; Valine
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K20/00—Accessory food factors for animal feeding-stuffs
    • A23K20/10—Organic substances
    • A23K20/142—Amino acids; Derivatives thereof
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K40/00—Shaping or working-up of animal feeding-stuffs
    • A23K40/10—Shaping or working-up of animal feeding-stuffs by agglomeration; by granulation, e.g. making powders

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Organic Chemistry (AREA)
  • Wood Science & Technology (AREA)
  • Food Science & Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Biotechnology (AREA)
  • Animal Husbandry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Fodder In General (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)

Abstract

Un procedimiento que produce un complemento de alimentacion de L-Lisina con una pureza de L-Lisina en el orden teorico del 35% al 80%, calculado como unporcentaje de base libre por kg, y más preferentemente, del 50% al 80% de L-Lisina a uncald o de fermentacion de L-Lisina. El material agregado seencuentra en una cantidad que lleva a obtener un complemento de alimentacion de L-Lisina con un pureza de L-Lisina dentro del orden teorico del 35% al 80%,calculado como un porcentaje debase libr e por kg, y más preferentemente entre alrededor del 50% y el 80% de L-Lisina. La fraccion de caldo de fermentacionde L-Lisina se obtiene mediante cualquier medio de separacion adecuado tal como ultrafiltracion o centrifugacion. Elprocedimiento tamb ién comprende un paso desecado que comprende cualquier medio de secado tal como un granulado de aspercion, secador de bandeja, secador de tambor, secador giratorio y secadorde tunel.
ARP980106270A 1997-12-16 1998-12-10 Procedimiento para producir un complemento de alimentacion de l-lisina granular con una cantidad ajustable de pureza de l-lisina AR013797A1 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/991,145 US5990350A (en) 1997-12-16 1997-12-16 Process for making granular L-lysine
US09/098,948 US6017555A (en) 1997-12-16 1998-06-17 Process for making L-lysine feed supplement

Publications (1)

Publication Number Publication Date
AR013797A1 true AR013797A1 (es) 2001-01-10

Family

ID=25536926

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP980106270A AR013797A1 (es) 1997-12-16 1998-12-10 Procedimiento para producir un complemento de alimentacion de l-lisina granular con una cantidad ajustable de pureza de l-lisina

Country Status (11)

Country Link
US (2) US5990350A (es)
EP (1) EP1424012B1 (es)
KR (1) KR19990063252A (es)
AR (1) AR013797A1 (es)
ES (1) ES2449225T3 (es)
GT (1) GT199800000A (es)
IN (1) IN187730B (es)
MY (1) MY116308A (es)
UY (1) UY25312A1 (es)
YU (1) YU58598A (es)
ZA (1) ZA9811450B (es)

Families Citing this family (61)

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DE102008001874A1 (de) 2008-05-20 2009-11-26 Evonik Degussa Gmbh Verfahren zur Herstellung von L-Aminosäuren
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BR112014027768A2 (pt) 2012-05-09 2017-06-27 Evonik Industries Ag aditivo de ração animal, contendo l-aminoácido, na forma de um granulado na base de caldo de fermentação e processo para produção
DE102012024435A1 (de) 2012-12-14 2014-07-10 Forschungszentrum Jülich GmbH Verfahren zur Identifizierung einer Zelle mit gegenüber ihrem Wildtyp erhöhten intrazellulären Konzentration eines bestimmten Metaboliten, wobei die Veränderung der Zelle durch Rekombi-neering erreicht wird, sowie ein Verfahren zur Herstellung einer gegenüber ihrem Wildtyp genetisch veränderten Produktionszelle mit optimierter Produktion eines bestimmten Metaboliten, ein Verfahren zur Herstellung dieses Metaboliten, sowie dafür geeignete Nukleinsäuren
EP2762571A1 (de) 2013-01-30 2014-08-06 Evonik Industries AG Mikroorganismus und Verfahren zur fermentativen Herstellung von Aminosäuren
ES2623161T3 (es) 2013-06-03 2017-07-10 Evonik Degussa Gmbh Procedimiento para la preparación de L-valina utilizando corinebacterias recombinantes que contienen el operón ilvBN inducible por propionato
ES2786108T3 (es) 2013-10-24 2020-10-08 Evonik Degussa Gmbh Aditivo para piensos para animales que contiene L-aminoácido
ES2781752T3 (es) 2013-10-24 2020-09-07 Evonik Operations Gmbh Aditivo para piensos para animales que contiene L-aminoácido
EP2932856B1 (en) * 2014-04-07 2017-08-23 Evonik Degussa GmbH Process for fluidized bed granulation of amino acid-containing fermentation broths
EP2940144A1 (de) 2014-04-30 2015-11-04 Evonik Degussa GmbH Verfahren zur Produktion von L-Lysin unter Verwendung eines alkaliphilen Bakteriums
ES2778037T3 (es) 2014-04-30 2020-08-07 Evonik Operations Gmbh Procedimiento para la producción de L-aminoácidos bajo empleo de una bacteria alcalífila
EP2940039A1 (de) 2014-04-30 2015-11-04 Evonik Degussa GmbH Verfahren zur Produktion von L-Aminosäuren in Corynebakterien unter Verwendung eines Glycin spaltenden Systems
DE102014208199A1 (de) 2014-04-30 2015-11-05 Evonik Degussa Gmbh Verfahren zur Produktion von L-Aminosäuren unter Verwendung eines alkaliphilen Bakteriums
BR102015008762B1 (pt) 2015-04-17 2021-06-08 Cj Do Brasil Industria E Comercio De Produtos Alimenticios Ltda. processo de fabricação de aditivo granulado alcalino para rações animais e aditivo granulado alcalino para rações animais
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JP2019519242A (ja) 2016-06-30 2019-07-11 ザイマージェン インコーポレイテッド 細菌ヘモグロビンライブラリーを生成するための方法およびその使用
JP2019519241A (ja) 2016-06-30 2019-07-11 ザイマージェン インコーポレイテッド グルコース透過酵素ライブラリーを生成するための方法およびその使用
CN110869504A (zh) 2017-06-07 2020-03-06 齐默尔根公司 来自谷氨酸棒状杆菌的启动子及其在调节辅助基因表达中的用途
EP3415622A1 (en) 2017-06-14 2018-12-19 Evonik Degussa GmbH Method for production of fine chemicals using a corynebacterium secreting modified alpha-1,6-glucosidases
EP3456833A1 (en) 2017-09-18 2019-03-20 Evonik Degussa GmbH Method for the fermentative production of l-amino acids
EP3467099A1 (en) 2017-10-05 2019-04-10 Evonik Degussa GmbH Method for the fermentative production of l-amino acids
EP3498853A1 (en) 2017-12-14 2019-06-19 Evonik Degussa GmbH Method for the fermentative production of l-lysine
KR102223797B1 (ko) * 2018-03-23 2021-03-12 씨제이제일제당 주식회사 L-아미노산을 포함하는 과립 및 이의 제조방법
EP3594355A1 (en) 2018-07-12 2020-01-15 Evonik Operations GmbH Method for the fermentative production of l-lysine
EP3599282B1 (en) 2018-07-24 2021-03-17 Evonik Operations GmbH Method for the fermentative production of l-lysine
RU2019128538A (ru) 2018-09-26 2021-03-11 Эвоник Оперейшенс ГмбХ Способ ферментативного получения l-лизина
EP3660158A1 (en) 2018-11-29 2020-06-03 Evonik Operations GmbH Method for the fermentative production of l-lysine
CN116249778A (zh) 2020-07-15 2023-06-09 赢创运营有限公司 编码氨基酸序列、编码氧化还原酶的多核苷酸
KR102567250B1 (ko) * 2020-12-07 2023-08-21 전주대학교 산학협력단 수비드 조리법에 의한 반려묘 츄르 제조방법
WO2023016890A1 (en) 2021-08-09 2023-02-16 Evonik Operations Gmbh Method for producing a recombinant bacterial collagen-like protein (clp)
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WO2023016895A1 (en) 2021-08-09 2023-02-16 Evonik Operations Gmbh Polynucleotide encoding a bacterial collagen-like protein
CN117999103A (zh) 2021-09-20 2024-05-07 赢创运营有限公司 非粘附性胶原蛋白样水凝胶
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Also Published As

Publication number Publication date
MY116308A (en) 2003-12-31
EP1424012B1 (en) 2013-12-11
ES2449225T3 (es) 2014-03-18
YU58598A (sh) 2000-10-30
EP1424012A3 (en) 2004-06-09
US5990350A (en) 1999-11-23
GT199800000A (es) 1999-11-02
ZA9811450B (en) 2000-03-08
IN187730B (es) 2002-06-15
EP1424012A2 (en) 2004-06-02
KR19990063252A (es) 1999-07-26
UY25312A1 (es) 1999-09-27
US6017555A (en) 2000-01-25

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