DD249712A1 - PROCESS FOR PREPARING LIPASE - Google Patents
PROCESS FOR PREPARING LIPASE Download PDFInfo
- Publication number
- DD249712A1 DD249712A1 DD29106886A DD29106886A DD249712A1 DD 249712 A1 DD249712 A1 DD 249712A1 DD 29106886 A DD29106886 A DD 29106886A DD 29106886 A DD29106886 A DD 29106886A DD 249712 A1 DD249712 A1 DD 249712A1
- Authority
- DD
- German Democratic Republic
- Prior art keywords
- lipase
- enzyme
- culture supernatant
- cultivation
- strain
- Prior art date
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- Enzymes And Modification Thereof (AREA)
Abstract
Das Ziel der Erfindung besteht darin, ein Verfahren anzugeben, das ein Enzym hoher spezifischer Aktivitaet und Anreicherung liefert. Die Aufgabe wird darin gesehen, durch Zuechtung eines Bakterienstammes auf einem bisher nicht verwendeten Kultursubstrat das gewuenschte Enzym herzustellen. Das Wesen der Erfindung besteht darin, den Stamm Acinetobacter calcoaceticus auf wasserloeslichen Fettsaeureestern als einziger C-Quelle zu zuechten, bei deren Abbau Fettsaeuren entstehen.The object of the invention is to provide a method which provides an enzyme of high specific activity and enrichment. The object is seen to produce the desired enzyme by culturing a bacterial strain on a previously unused culture substrate. The essence of the invention consists in cultivating the Acinetobacter calcoaceticus strain on fatty acid esters of water-soluble fatty acids as the sole source of C, fatty acids being produced during their degradation.
Description
Ausführungsbeispielembodiment
Acinetobacter calcoaceticus (69V) wird bei 3O0C in Submerskultur in einem flüssigen Minimalmedium gezüchtet. Das Medium enthält pro Liter: 6,97K2HPO4,1,5g NaH2PO4, 0,2g MgSO4- 7H2O, 7,5mg FeSO4 · 7H2O, 0,75mg MnSO4 · 4H2O, 0,75mg ZnSO4- 7H2O, 0,15mg CuSO4- 5H2O, 0,15mg CoCI2 · 6H2O und 0,15mg Borsäure. Als Impfsuspension dient eine Abschwemmung von Bouillon-Agar. Als C-Quelle wie Polyoxyethylen-sorbitan-monooleat in einer Konzentration von 10 ml/l als einziger Kohlenstoffquelle und NH4Cl (3g/l) als N-Quelle verwendet.Acinetobacter calcoaceticus (69V) is grown at 3O 0 C in submerged culture in a liquid minimal medium. The medium contains per liter: 6.97K 2 HPO 4 , 1.5g NaH 2 PO 4 , 0.2g MgSO 4 - 7H 2 O, 7.5mg FeSO 4 .7H 2 O, 0.75mg MnSO 4 .4H 2 O , 0.75 mg of ZnSO 4 - 7H 2 O, 0.15 mg of CuSO 4 - 5H 2 O, 0.15 mg of CoCl 2 · 6H 2 O and 0.15 mg of boric acid. As a vaccine suspension is a flush of bouillon agar. Used as the C source such as polyoxyethylene sorbitan monooleate at a concentration of 10 ml / l as the sole carbon source and NH 4 Cl ( 3 g / l) as the N source.
Nach einer Wachstumszeit von 12h werden die Bakterien durch Zentrifugation (2000 x g, 20min) separiert und derzellfreie Kulturüberstand gewonnen. Zu diesem Kulturüberstand wird NaCI zu einer Konzentration von 1 mol/l zugegeben und die Lösung bei 4°C auf eine Octyl-Sepharose-Säule aufgetragen. Die Lipaseaktivität verbleibt am Trägermaterial. Nacheinander wird der Träger mit 1 mol/l Natriumchloridlösung (in 50mmol/l Phosphatpuffer, pH7,5)xl gewaschen, bis kein Protein im Eluat nachweisbar ist. Das Enzym wird anschließend mit Triton X-100 (5g/l in 50mmol/l Phosphatpuffer, pH7,5) vom Träger gelöst. Das gewonnene Enzym ist diskelektrophor'etisch rein. Die Isolierung der Lipase ist in Tabelle 2 dargestellt, x) und Phosphatpuffer, pH7,5After a growth time of 12 h, the bacteria are separated by centrifugation (2000 × g, 20 min) and the cell-free culture supernatant is obtained. NaCI is added to this culture supernatant to a concentration of 1 mol / l and the solution is applied at 4 ° C. to an octyl-Sepharose column. The lipase activity remains on the carrier material. Successively, the carrier is washed with 1 mol / l sodium chloride solution (in 50 mmol / l phosphate buffer, pH 7.5) xl until no protein is detectable in the eluate. The enzyme is then dissolved with Triton X-100 (5 g / l in 50 mmol / l phosphate buffer, pH 7.5) from the carrier. The recovered enzyme is discrete electrophoretically pure. The isolation of the lipase is shown in Table 2, x) and phosphate buffer, pH 7.5
Volumenaktivität, Proteinkonzentration und spezifische Aktivität der Lipse im Kulturüberstand von Acinetobacter calcoaceticus nach Wachstum auf verschiedenen KultursubstratenVolume activity, protein concentration and specific activity of the lipids in the culture supernatant of Acinetobacter calcoaceticus after growth on different culture substrates
KultursubstratCulture substrate
Volumenaktivität (μιηοΙ/Γηίη/ΓηΙ)Volume activity (μιηοΙ / Γηίη / ΓηΙ)
Protein (mg/1)Protein (mg / l)
spezifische Aktivität (^mol/min/mg Protein)specific activity (^ mol / min / mg protein)
Bouillonbouillon
Polyoxyethylen-polyoxyethylene
sobitan-mono-sorbitan mono-
lauratlaurat
Polyoxyethylen-polyoxyethylene
sorbitan-mono-sorbitan mono-
palmitatpalmitate
Polyoxyethylen-polyoxyethylene
sorbitan-mono-sorbitan mono-
0,30.3
6,56.5
6,06.0
26,626.6
9,59.5
0,250.25
0,250.25
0,340.34
0,030.03
Reinigung der Lipase (Kultursubstrat: Polyoxyethylen-sorbitanmonooleat) von Acinetobacter calcoaceticusPurification of the lipase (culture substrate: polyoxyethylene sorbitan monooleate) of Acinetobacter calcoaceticus
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DD29106886A DD249712B1 (en) | 1986-06-06 | 1986-06-06 | PROCESS FOR PREPARING LIPASE |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DD29106886A DD249712B1 (en) | 1986-06-06 | 1986-06-06 | PROCESS FOR PREPARING LIPASE |
Publications (2)
Publication Number | Publication Date |
---|---|
DD249712A1 true DD249712A1 (en) | 1987-09-16 |
DD249712B1 DD249712B1 (en) | 1988-12-14 |
Family
ID=5579747
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DD29106886A DD249712B1 (en) | 1986-06-06 | 1986-06-06 | PROCESS FOR PREPARING LIPASE |
Country Status (1)
Country | Link |
---|---|
DD (1) | DD249712B1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4933287A (en) * | 1985-08-09 | 1990-06-12 | Gist-Brocades N.V. | Novel lipolytic enzymes and their use in detergent compositions |
WO2009037488A2 (en) * | 2007-09-21 | 2009-03-26 | Statoilhydro Asa | Biodiesel |
-
1986
- 1986-06-06 DD DD29106886A patent/DD249712B1/en not_active IP Right Cessation
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4933287A (en) * | 1985-08-09 | 1990-06-12 | Gist-Brocades N.V. | Novel lipolytic enzymes and their use in detergent compositions |
WO2009037488A2 (en) * | 2007-09-21 | 2009-03-26 | Statoilhydro Asa | Biodiesel |
WO2009037488A3 (en) * | 2007-09-21 | 2009-08-06 | Statoilhydro Asa | Biodiesel |
EA017338B1 (en) * | 2007-09-21 | 2012-11-30 | Статоил Аса | Biodiesel |
Also Published As
Publication number | Publication date |
---|---|
DD249712B1 (en) | 1988-12-14 |
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