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 PDFInfo
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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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- ketogluconic
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- diketogluconic
- ketogulonic
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- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/40—Preparation of oxygen-containing organic compounds containing a carboxyl group including Peroxycarboxylic acids
- C12P7/58—Aldonic, 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)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US85295077A | 1977-11-18 | 1977-11-18 | |
US85295077 | 1977-11-18 |
Publications (3)
Publication Number | Publication Date |
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DK512978A DK512978A (en) | 1979-05-19 |
DK152679B true DK152679B (en) | 1988-04-11 |
DK152679C DK152679C (en) | 1988-08-22 |
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Application Number | Title | Priority Date | Filing Date |
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DK512978A DK152679C (en) | 1977-11-18 | 1978-11-17 | METHOD OF PREPARING 2,5-DICETOGLUCONIC ACID OR A MIXTURE OF 2-KETOGULONIC ACID AND 2-KETOGLUCONIC ACID |
Country Status (26)
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JP (1) | JPS54145283A (en) |
AR (1) | AR218348A1 (en) |
AT (1) | AT363887B (en) |
AU (1) | AU505434B1 (en) |
BE (1) | BE872095A (en) |
BR (1) | BR7807524A (en) |
CA (1) | CA1119981A (en) |
CH (1) | CH643592A5 (en) |
DD (1) | DD140459A5 (en) |
DE (1) | DE2849393C2 (en) |
DK (1) | DK152679C (en) |
ES (1) | ES475216A1 (en) |
FI (1) | FI782871A (en) |
FR (1) | FR2409304A1 (en) |
GB (1) | GB2008116B (en) |
HU (1) | HU175521B (en) |
IL (1) | IL55969A0 (en) |
IT (1) | IT1101715B (en) |
LU (1) | LU80536A1 (en) |
NL (1) | NL7811353A (en) |
NO (1) | NO783877L (en) |
PL (1) | PL118433B1 (en) |
PT (1) | PT68789A (en) |
RO (1) | RO75389A (en) |
SE (1) | SE7809345L (en) |
ZA (1) | ZA786487B (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
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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)
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 |
-
1978
- 1978-09-05 SE SE7809345A patent/SE7809345L/en unknown
- 1978-09-13 AU AU39819/78A patent/AU505434B1/en not_active Expired
- 1978-09-20 FI FI782871A patent/FI782871A/en not_active IP Right Cessation
- 1978-10-31 CH CH1121978A patent/CH643592A5/en not_active IP Right Cessation
- 1978-11-02 HU HU78PI647A patent/HU175521B/en unknown
- 1978-11-03 PL PL1978210683A patent/PL118433B1/en unknown
- 1978-11-03 DD DD78208866A patent/DD140459A5/en unknown
- 1978-11-03 RO RO7895585A patent/RO75389A/en unknown
- 1978-11-14 DE DE2849393A patent/DE2849393C2/en not_active Expired
- 1978-11-15 PT PT68789A patent/PT68789A/en unknown
- 1978-11-16 GB GB7844723A patent/GB2008116B/en not_active Expired
- 1978-11-16 LU LU80536A patent/LU80536A1/en unknown
- 1978-11-16 CA CA000316362A patent/CA1119981A/en not_active Expired
- 1978-11-16 IT IT29866/78A patent/IT1101715B/en active
- 1978-11-16 BR BR7807524A patent/BR7807524A/en unknown
- 1978-11-17 NO NO783877A patent/NO783877L/en unknown
- 1978-11-17 AR AR274472A patent/AR218348A1/en active
- 1978-11-17 IL IL55969A patent/IL55969A0/en unknown
- 1978-11-17 AT AT0823178A patent/AT363887B/en not_active IP Right Cessation
- 1978-11-17 DK DK512978A patent/DK152679C/en active
- 1978-11-17 NL NL7811353A patent/NL7811353A/en not_active Application Discontinuation
- 1978-11-17 JP JP14215078A patent/JPS54145283A/en active Granted
- 1978-11-17 FR FR7832491A patent/FR2409304A1/en not_active Withdrawn
- 1978-11-17 ZA ZA00786487A patent/ZA786487B/en unknown
- 1978-11-17 BE BE191792A patent/BE872095A/en unknown
- 1978-11-17 ES ES475216A patent/ES475216A1/en not_active Expired
Patent Citations (3)
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 |
Also Published As
Publication number | Publication date |
---|---|
ZA786487B (en) | 1979-10-31 |
DK512978A (en) | 1979-05-19 |
FI782871A (en) | 1979-05-19 |
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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