DK152679B - METHOD OF PREPARING 2,5-DICETOGLUCONIC ACID OR A MIXTURE OF 2-KETOGULONIC ACID AND 2-KETOGLUCONIC ACID - Google Patents

METHOD OF PREPARING 2,5-DICETOGLUCONIC ACID OR A MIXTURE OF 2-KETOGULONIC ACID AND 2-KETOGLUCONIC ACID Download PDF

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DK152679B
DK152679B DK512978AA DK512978A DK152679B DK 152679 B DK152679 B DK 152679B DK 512978A A DK512978A A DK 512978AA DK 512978 A DK512978 A DK 512978A DK 152679 B DK152679 B DK 152679B
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acid
ketogluconic
mixture
diketogluconic
ketogulonic
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DK512978AA
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DK152679C (en
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Donald Albert Kita
Karlene Elizabeth Hall
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Pfizer
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/40Preparation of oxygen-containing organic compounds containing a carboxyl group including Peroxycarboxylic acids
    • C12P7/58Aldonic, ketoaldonic or saccharic acids

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Description

DK 152679 BDK 152679 B

Opfindelsen angår en fremgangsmåde til fremstilling af 2,5-diketogluconsyre eller en blanding af 2-ketogulonsyre og 2-ketoglu-consyre ved dyrkning af en mikroorganisme af slægten Acetobacter i et medium indeholdende glucose i en koncentration fra 2,5 til 20%, efterfulgt af udvinding af den resulterende 2,5-diketogluconsyre fra mediet eller oparbejdning af dette ved selektiv reduktion til opnåelse af en blanding af 2-ketogulonsyre og 2-ketogluconsyre.The invention relates to a process for the preparation of 2,5-diketogluconic acid or a mixture of 2-ketogulonic acid and 2-ketogluconic acid by growing a microorganism of the genus Acetobacter in a medium containing glucose at a concentration of 2.5 to 20%, followed by by extracting the resulting 2,5-diketogluconic acid from the medium or working it up by selective reduction to obtain a mixture of 2-ketogulonic acid and 2-ketogluconic acid.

2,5-Diketogluconsyre er et egnet mellemprodukt ved fremstilling af vitamin C. Hidtil er 2,5-diketogluconsyre blevet fremstillet med en del forskellige bakterier såsom Acetobacter melanogenum, Acetobacter aurantium, Gluconoacetobacter rubiginosus, Gluconoaceto-bacter liquifaciens og Pseudomonas sesami. Anvendelse af disse mi2,5-Diketogluconic acid is a suitable intermediate in the production of vitamin C. To date, 2,5-diketogluconic acid has been produced with a variety of bacteria such as Acetobacter melanogenum, Acetobacter aurantium, Gluconoacetobacter rubiginosus, Gluconoaceto-bacter liquifaciens and Pseudomonas sesami. Use of these mi

2 DK 152679 B2 DK 152679 B

kroorganismer er imidlertid ikke helt ideel set ud fra et industrielt synspunkt, da der dannes store mængder brune eller gulbrune pigmenter som biprodukter ved dyrkningen, hvorved renheden af den dannede 2,5-diketogluconsyre formindskes.however, the organisms are not ideal from an industrial point of view, as large amounts of brown or yellow-brown pigments are formed as by-products in culture, thereby reducing the purity of the 2,5-diketogluconic acid formed.

USA patentskrift nr. 3.790.444 omhandler fremstilling af 2,5-diketogluconsyre uden ledsagende brunt pigment ved anvendelse af en ny art betegnet Acetobacter fragum. Herved kan opnås et udbytte på op til 87% (beregnet på glucose).U.S. Patent No. 3,790,444 discloses the preparation of 2,5-diketogluconic acid without accompanying brown pigment using a novel species called Acetobacter fragum. This yields a yield of up to 87% (based on glucose).

Det har vist sig, at Acetobacter cerinus danner 2,5-diketogluconsyre med stort udbytte ved dyrkning i et medium indeholdende glucose som hovedcarbonkilde. To af de afprøvede stammer, IFO 3263 og 3266, danner 2,5-diketogluconsyre i udbytter større end 95% (beregnet på glucose).It has been found that Acetobacter cerinus generates 2,5-diketogluconic acid in high yield by growing in a medium containing glucose as the main carbon source. Two of the strains tested, IFO 3263 and 3266, form 2,5-diketogluconic acid in yields greater than 95% (based on glucose).

Fremgangsmåden ifølge opfindelsen er ejendommelig ved det i krav 1*s kendetegnende del anførte.The process according to the invention is characterized by the characterizing part of claim 1 *.

2,5-Diketogluconsyre er, som nævnt, egnet som mellemprodukt ved fremstilling af ascorbinsyre. En vandig opløsning af 2,5-diketogluconsyre kan selektivt reduceres til opnåelse af en blanding af 2-ketogulonat og 2-ketogluconat, som kan omdannes til ascorbinsyre og erythrobinsyre.2,5-Diketogluconic acid is, as mentioned, suitable as an intermediate in the preparation of ascorbic acid. An aqueous solution of 2,5-diketogluconic acid can be selectively reduced to give a mixture of 2-ketogulonate and 2-ketogluconate which can be converted to ascorbic acid and erythrobic acid.

Ved fremgangsmåden ifølge opfindelsen kan anvendes let tilgængelige stammer af Acetobacter cerinus. Alle de nedenfor anførte offentligt deponerede stammer af Acetobacter cerinus har været prøvet og har vist sig at give ketosyrer i et udbytte på 50-95% eller mere (beregnet på glucose). Når Acetobacter cerinus IFO 3263 eller 3266 anvendes, er den dannede ketosyre udelukkende den ønskede 2,5-diketogluconsyre i udbytter større end 95%, beregnet på glucose. De tilgængelige, offentligt deponerede stammer af Acetobacter cerinus er følgende: IFO 3262 (ATCC 12303) 3263 3264 3265 3266 3267 ’ 3268 3269.In the method of the invention readily available strains of Acetobacter cerinus can be used. All of the publicly deposited strains of Acetobacter cerinus listed below have been tested and found to give keto acids in a yield of 50-95% or more (based on glucose). When Acetobacter cerinus IFO 3263 or 3266 is used, the keto acid formed is solely the desired 2,5-diketogluconic acid in yields greater than 95%, based on glucose. The publicly available strains of Acetobacter cerinus available are as follows: IFO 3262 (ATCC 12303) 3263 3264 3265 3266 3267 '3268 3269.

Disse mikroorganismer kræver ikke kostbare organiske nitrogenkilder såsom pepton eller kødekstrakt. Når der anvendes urin- 3These microorganisms do not require expensive organic nitrogen sources such as peptone or meat extract. When urine is used 3

DK 152679 BDK 152679 B

stof eller uorganiske nitrogenkilder såsom ammoniumsulfat, ammoniumnitrat eller ammoniumphosphat tilsættes nicotinsyre som en essentiel vækstfaktor.substance or inorganic nitrogen sources such as ammonium sulphate, ammonium nitrate or ammonium phosphate add nicotinic acid as an essential growth factor.

Glucosekoncentrationen i mediet varierer fortrinsvis mellem 10 og 12% til opnåelse af 2,5-diketogluconsyren mest økonomisk. Gæringstemperaturen er mellem 20 og 35°C, fortrinsvis mellem 25 og 30° C, mest foretrukket ca. 28°C. Den initiale pH-værdi for kulturmediet kan andrage fra 3,5 til 7,5, fortrinsvis fra 5 til 6. Under gæringens forløb holdes pH-værdien ved ca. 5,5 ved tilsætning af natriumhydroxidopløsning. Calciumcarbonat kan anvendes til pH-kontrol og sættes til den mængde medium, som anvendes til efterfyldning efter autoklavering, i en mængde på 30 g pr. 110 g glucose.The glucose concentration in the medium preferably varies between 10 and 12% to obtain the 2,5-diketogluconic acid most economically. The fermentation temperature is between 20 and 35 ° C, preferably between 25 and 30 ° C, most preferably approx. 28 ° C. The initial pH of the culture medium may be from 3.5 to 7.5, preferably from 5 to 6. During the course of fermentation, the pH is maintained at ca. 5.5 by adding sodium hydroxide solution. Calcium carbonate can be used for pH control and added to the amount of medium used for autoclaving backfill in an amount of 30 g / ml. 110 g glucose.

Efter inokulering omrøres gæringsmediet f.eks. med en mekanisk omrører med 1700 omdrejninger pr. minut og beluftes med fra 0,5 til 1 volumen luft pr. volumen dyrkningsmedium pr. minut.After inoculation, the fermentation medium is stirred e.g. with a mechanical stirrer at 1700 rpm. and is aerated with from 0.5 to 1 volume of air per minute. volume of culture medium per minute.

Ved anvendelse af Acetobacter cerinus IFO 3263 eller 3266 gennemføres gæringen indtil der er opnået et udbytte af 2,5 diketo-gluconsyre på mindst 90%, beregnet på glucose (36-40 timer).Using Acetobacter cerinus IFO 3263 or 3266, fermentation is carried out until a yield of 2.5 diketo-gluconic acid of at least 90%, calculated on glucose (36-40 hours) is obtained.

Det er ved papirchromatografi bestemt, at omdannelsen af glucose til 2,5-diketogluconsyre sker ad følgende veje:It is determined by paper chromatography that the conversion of glucose to 2,5-diketogluconic acid occurs in the following ways:

Glucose — > 2-ketogluconsyre-> 2,5-diketogluconsyre, og glucose-5-ketogluconsyre-* 2,5-diketogluconsyre.Glucose -> 2-ketogluconic acid-> 2,5-diketogluconic acid, and glucose-5-ketogluconic acid * 2,5-diketogluconic acid.

Der anvendes Whatman nr. 1 og nr. 2 papir og et opløsningsmiddelsystem af methylethylketon':acetone:myresyre:vand (80:6:2:12). Syrepletterne lokaliseres ved sprøjtning med 0,2% o-phenylendiamin i ethanolisk opløsning indeholdende 1% salpetersyre og opvarmning til ca. 70°C (5-ketogluconsyre giver blåt, 2-ketogluconsyre giver gult og 2,5-diketogluconsyre giver grønt). Højtryksvæskechromato-grafi kan også anvendes til identifikation.Whatman No. 1 and No. 2 paper and a solvent system of methyl ethyl ketone: acetone: formic acid: water are used (80: 6: 2: 12). The acid spots are localized by spraying with 0.2% o-phenylenediamine in ethanolic solution containing 1% nitric acid and heating to ca. 70 ° C (5-ketogluconic acid gives blue, 2-ketogluconic acid gives yellow and 2,5-diketogluconic acid gives green). High pressure liquid chromatography can also be used for identification.

2,5-Diketogluconsyre kan adskilles og udvindes fra den færdige gæringsvæske efter enhver sædvanlig metode, som det vil være kendt for fagmanden. Den filtrerede gæringsvæske kan oparbejdes f. eks. ved behandling med et borhydrid, og den resulterende blanding af 2-ketogluconsyre og 2-ketogulonsyre hydrolyseres til dannelse af ascorbinsyre og erythrobinsyre.2,5-Diketogluconic acid can be separated and recovered from the finished fermentation liquid by any conventional method as will be known to those skilled in the art. The filtered fermentation liquid can be worked up, for example, by treatment with a borohydride, and the resulting mixture of 2-ketogluconic acid and 2-ketogulonic acid is hydrolyzed to form ascorbic acid and erythrobic acid.

44

DK 152679 BDK 152679 B

Eksempel 1 Følgende vandige inokuleringsmedium blev fremstillet:Example 1 The following aqueous inoculation medium was prepared:

Bestanddel Gram/literIngredient Gram / liter

Glucose 25Glucose 25

Ma j s s tøbevand 5 KH2P04 0,5 K2HP04 0,5Ma j s s tap water 5 KH2PO4 0.5 K2HPO0 0.5

MgS04,7H20 0,2MgSO4.7H2O 0.2

CaCO^ 6,3 pH 6,2CaCO3 6.3 pH 6.2

En rystekolbe indeholdende en liter medium blev autoklaveret i 30 minutter ved 121°C. pH-værdien af det afkølede medium var 5,0. Celler af Acetobacter cerinus IFO 3263 fra en skråkultur af næringsagar (5 ml af en 20 ml steril vandig suspension) blev sat til kolben, som derpå blev rystet på et roterende rystebord ved ca. 28°C i ca. 24 timer.A shake flask containing one liter of medium was autoclaved for 30 minutes at 121 ° C. The pH of the cooled medium was 5.0. Cells of Acetobacter cerinus IFO 3263 from a slant culture of nutrient agar (5 ml of a 20 ml sterile aqueous suspension) were added to the flask which was then shaken on a rotary shaker table at ca. 28 ° C for approx. 24 hours.

En prøve af denne kultur, tilstrækkelig stor til at give et inoculum på 5 volumen/volumen%, blev sat til en 4 liters omrørt gæringsbeholder indeholdende 2 liter af nedenstående produktionsmedium:A sample of this culture, sufficiently large to give an inoculum of 5 v / v%, was added to a 4 liter stirred fermenter containing 2 liters of the following production medium:

Bestanddel Gram/literIngredient Gram / liter

Glucose 110Glucose 110

Majs støbevand 0,5 (NH4)2HP04 0,58 KH2P04 1,5Maize molding water 0.5 (NH4) 2HPO4 0.58 KH2PO4 1.5

MgS04,7H20 0,5MgSO4.7H2O 0.5

Urinstof 0,5Urea 0.5

CuS04,5H20 1 mgCuSO4.5H2O 1 mg

Nicotinsyre 300 γ pH 6,0 Gæringen blev udført ved en temperatur på ca. 28°C under omrøring ved 1700 omdrejninger pr. minut og beluftning med en mængde på 0,75 volumen gæringsvæske pr. minut. Efter en gæringsperiode på ca. 20 timer blev der tilsat sterilt glucose (55 gram/liter). pH-værdien blev holdt ved 5,5 ved tilsætning af natriumhydroxidopløsning. Gæringen blev fortsat til et udbytte af 2,5-diketogluconsyreNicotinic acid 300 γ pH 6.0 The fermentation was carried out at a temperature of approx. 28 ° C with stirring at 1700 rpm. per minute and aeration with an amount of 0.75 volume of fermentation liquid per minute. minute. After a fermentation period of approx. For 20 hours, sterile glucose (55 grams / liter) was added. The pH was kept at 5.5 by the addition of sodium hydroxide solution. The fermentation was continued to yield 2,5-diketogluconic acid

Claims (4)

1. Fremgangsmåde til fremstilling af 2,5-diketogluconsyre, eller en blanding af 2-ketogulonsyre og 2-ketogluconsyre ved dyrkning af en mikroorganisme af slægten Acetobacter i et medium indeholdende glucose i en koncentration fra 2,5 til 20%, efterfulgt af udvinding af den resulterende 2,5-diketogluconsyre fra mediet eller oparbejdning af dette ved selektiv reduktion til opnåelse af en blanding af 2-ketogulonsyre og 2-ketogluconsyre, kendetegnet ved, at der som mikroorganisme, anvendes en sådan hørende til Acetobacter cerinus.A process for preparing 2,5-diketogluconic acid, or a mixture of 2-ketogulonic acid and 2-ketogluconic acid, by culturing a microorganism of the genus Acetobacter in a medium containing glucose at a concentration of 2.5 to 20%, followed by extraction of the resulting 2,5-diketogluconic acid from the medium or working it up by selective reduction to give a mixture of 2-ketogulonic acid and 2-ketogluconic acid, characterized in that such as a microorganism, one belonging to Acetobacter cerinus is used. 2. Fremgangsmåde ifølge krav 1, kendetegnet ved, at gæringstemperaturen er fra 20 til 35°C, den indledende pH-værdi fra 3,5 til 7,5, og pH-værdien under gæringen holdes ved 5,5.Process according to claim 1, characterized in that the fermentation temperature is from 20 to 35 ° C, the initial pH is from 3.5 to 7.5 and the pH during fermentation is kept at 5.5. 3. Fremgangsmåde ifølge krav 1 eller 2, kendetegne t ved, at nævnte Acetobacter cerinus er af stammen IFO 3263.Method according to claim 1 or 2, characterized in that said Acetobacter cerinus is of the strain IFO 3263. 4. Fremgangsmåde ifølge krav 1 eller 2, kendetegnet ved, at nævnte Acetobacter cerinus er af stammen IFO 3266.Method according to claim 1 or 2, characterized in that said Acetobacter cerinus is of the strain IFO 3266.
DK512978A 1977-11-18 1978-11-17 METHOD OF PREPARING 2,5-DICETOGLUCONIC ACID OR A MIXTURE OF 2-KETOGULONIC ACID AND 2-KETOGLUCONIC ACID DK152679C (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4316960A (en) * 1979-09-28 1982-02-23 Pfizer Inc. Preparation of 2,5-diketogluconic acid
JPS6365970A (en) * 1987-08-25 1988-03-24 Kyushu Hitachi Maxell Ltd Motor-driven sprayer
FR2820973B1 (en) 2001-02-19 2003-05-23 Oreal COMPOSITION COMPRISING VITAMIN C PREPARED DURING APPLICATION, USE OF ENZYMES FOR THE FORMATION OF VITAMIN C FOR TOPICAL USE AND COSMETIC PROCESSING METHOD

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3234105A (en) * 1962-09-20 1966-02-08 Takeda Chemical Industries Ltd Method for producing 2-keto-lgulonic acid
US3790444A (en) * 1971-03-09 1974-02-05 Daiichi Seiyaku Co Process for preparing diketogluconic acid
US3998697A (en) * 1974-09-20 1976-12-21 Shionogi & Co., Ltd. Process for preparing 2-keto-L-gulonic acid

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3234105A (en) * 1962-09-20 1966-02-08 Takeda Chemical Industries Ltd Method for producing 2-keto-lgulonic acid
US3790444A (en) * 1971-03-09 1974-02-05 Daiichi Seiyaku Co Process for preparing diketogluconic acid
US3998697A (en) * 1974-09-20 1976-12-21 Shionogi & Co., Ltd. Process for preparing 2-keto-L-gulonic acid

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DK512978A (en) 1979-05-19
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DD140459A5 (en) 1980-03-05
ATA823178A (en) 1981-02-15
IT1101715B (en) 1985-10-07
PL210683A1 (en) 1979-06-18
BR7807524A (en) 1979-07-24
AU505434B1 (en) 1979-11-22
BE872095A (en) 1979-05-17
NO783877L (en) 1979-05-21
NL7811353A (en) 1979-05-22
IT7829866A0 (en) 1978-11-16
ES475216A1 (en) 1979-04-16
DK152679C (en) 1988-08-22
JPS579357B2 (en) 1982-02-20
PL118433B1 (en) 1981-10-31
CA1119981A (en) 1982-03-16
FR2409304A1 (en) 1979-06-15
RO75389A (en) 1980-11-30
PT68789A (en) 1978-12-01
SE7809345L (en) 1979-05-19
IL55969A0 (en) 1979-01-31
HU175521B (en) 1980-08-28
GB2008116B (en) 1982-03-17
CH643592A5 (en) 1984-06-15
AT363887B (en) 1981-09-10
DE2849393C2 (en) 1983-05-05
GB2008116A (en) 1979-05-31
JPS54145283A (en) 1979-11-13
DE2849393A1 (en) 1979-05-23
AR218348A1 (en) 1980-05-30
LU80536A1 (en) 1980-06-05

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