专利摘要:
A new beta -galactosidase is now provided which is highly effective to digest lactose and stable at acidic pH values and thermally stable. The beta -galactosidase is produced by Penicillium multicolor in high yield and is isolated from the culture medium of this microorganism in an inexpensive and easy way.
公开号:SU952111A3
申请号:SU792724401
申请日:1979-02-05
公开日:1982-08-15
发明作者:Мива Тан;Кобаяси Рейсуке;Такита Киеси
申请人:Кумиаи Кемикал Индастри К.О. Лтд (Фирма);
IPC主号:
专利说明:

(5) METHOD FOR OBTAINING P) -GALACTOSIDASE
one
The invention relates to the microbiological industry, in particular to methods for producing the enzyme p) -galactosidase.
.-- five
A known method of production. (I-ralactosidase by cultivating the strain, the producer of Aspergillus og2aе FERM-F-1680 on a nutrient medium containing bran as a source of nitrogen and other nutrients, followed by isolation and purification of the enzyme. The resulting preparation hydrolyzes lactose, O-un-nitrophenyl-p-O-galactopyranoside and phenyl-ts -pD-galactopyranoside fl.
Enzyme activity is low.
The closest to the present invention is a method for producing p-galactosidase, which involves the cultivation of a strain of the genus Repici Ill urn producing it on a nutrient medium containing assimilated carbon and nitrogen sources with or without mineral salts
under aerobic conditions at a pH of 3, for 16-120 h, followed by separation of the enzyme from the culture fluid by solvent extraction, precipitation, purification, filtration, etc. 2
The resulting enzyme has a sufficiently high activity, but is not thermally stable and should be stored in the cold.
The purpose of the invention is to increase the durability and activity of the target product.
The goal is achieved by the fact that according to the method of producing | 3-galactosidase, which involves the cultivation of a strain-producing microorganism from the genus PeniciIlium on a nutrient medium containing assimilated carbon and nitrogen sources with or without mineral salts, followed by release of the enzyme from the culture fluid , PeniciMium multicolor KU-0-312 strain identified as FtRM-5 375 or ATCC 20539 is used as a producing microorganism, and bran is used as a source of nitrogen. The essence of the method consists in the use of the PeniciHium multicolor KU-0-312 strain to obtain the p-galacto-zidase enzyme. This strain was deposited with the Japan Depository Institute of Industrial Science and Technology Japan Kiago Chiba Depositary Institute. There are approximately 25 Nvar under the number FERM-P 375 as well as c. American Collections of type cultures under the number of ATCC 20539. Morphological. Properties inherent in the strain Peniciliium multicolor KU-0-312. Macroscopic observations (after incubation for 10 days on Capes agar medium). With the growth of Peniciliium multicolor, colonies with a diameter of 30 mm are formed. The surface is radially wrinkled with a dense velvety layer of conidia from deep blue-green to grayish-green in color, periphery in width of 1-2 mm from orange to yellow. Reverse srona from yellow to brown. Microscopic observation (after incubation for 10 days on Czapek's agar medium). Monomouting bunches. The conidophores are straight and vertical, without branching, 2-3 m wide, with extension towards the end. Sterigma: from 6 to It sterigm in a pack. Conidium spherical or oval shape with a diameter of 2-3 microns. The surface is smooth. When using the proposed method, the strain Peniciliium multico-lo can be cultivated in a liquid or solid nutrient medium using known methods under anaerobic conditions. The culture medium contains one or more natural nutrients, namely wheat bran, rice bran, defatted soy flour, cotton seed flour, as the main components. The cuprate medium may also contain lactose, starch, glucose, apaPinose, and xylose as a source of carbonaceous and ammonium sulfate, nitrate sodium carbonate, peptone, malt, and yeast extract as a nitrogen source. Inorganic salts may be included in the culture medium, for example, phosphates and magnesium and calcium salts. It is usually advisable to cultivate Peniciliium multicolor at 10-35 ° C, preferably 25-33 ° C, in an environment with a pH of -9, preferably 5-7, for 1-8 days, although the cultivation conditions may vary depending on the cultivation method. Production of new / 3-galactosidase according to the proposed method reaches a maximum after 2-6 days of incubation. When cultured in solid media, new β-galactosidase can be obtained with an activity of about 1000 units per gram of solid culture medium. When cultivated in a liquid medium, an enzyme with an activity of about 150 units per 1 ml of liquid medium can be obtained. To extract p-galactosidase according to the invention from Peniciliium multicolor culture medium, where the enzyme is formed and accumulates, the liquid culture medium is freed from solids by filtration or centrifugation and the resulting filtrate is then concentrated by distillation under reduced pressure or passed through a dialysis membrane and then subjected to salinization with ammonium sulfate or a precipitation process with acetone and / or ethanol to obtain a crude powder / galactosidase. The solid culture medium is treated with water (for the extraction of the enzyme) and the resulting aqueous extract is treated in the same way as the mentioned filtrate. The culture medium itself, the filtrate and the aqueous extract can be used as crude [L-galactosidase. For further purification, crude β-galactosidase can be processed by a known enzyme purification method, for example, by ion exchange, gel filtration, dialysis, adsorption and protein precipitation. When a concentrated filtrate or aqueous extract containing p-galactosidase is mixed with acetone to contain its weight, almost all | 5-galactosidase can be precipitated in the form of a powder, which after drying is detected
for example, high galactosidase activity on the order of 3, 8 units / m. 3.8 units / mg of the Poroshkova p-yag actosidase usually does not require further purification if administered orally to lactose-free patients as powders, granules or tablets in a mixture with a pharmaceutically acceptable carrier, for example starch, can be dissolved in milk and any dose taken by the patient.
The activity of p-galactosidase was evaluated according to the usual test method as follows.
Mix 1 ml of the substrate solution containing mg / ml o-nitrophenyl- | -0-galactopyranoside in water, 2 ml of 0.2 M buffered maquilvan solution (pH 1.5) AND (1 ml of enzyme solution, the mixture is heated at 3-7s for 15 minutes to induce an enzymatic reaction. After this, the reaction
the mixture is mixed with 1 ml of an aqueous 1 M sodium carbonate solution for stopping the reaction. To determine the content of o-nitrophenyl formed, the reaction mixture was subjected to colorimetric analysis at 420 µm, using a reference curve for the colorimetric analysis of o-nitrophenol. When an enzyme can produce 1 µmol of o-nitrophenol in 1 min, it is considered that this enzyme has 1 unit of activity.
To confirm the advantages of the enzymatic properties of p-galactosidase obtained according to the proposed method, they are compared with the properties of the known p-galactosidase from RepiciIlium citrinum, which is representative of galactosidase produced by other RepiciIlium 2 species. The results of this comparison are presented in the table.
Substrate (glycosides) Lactose
o-nitriphenyl | -0-galactonyranoside p-Nitrophenyl-0-galactonyranoside
Molecular weight
(gel method)
PH optimum
Active pH (the limits in which the enzyme is active)
Optimum temperature, C
The temperature is active (temperature limits in which the enzyme is active),
Stability at pH (pH limit in which the enzyme is stable when kept for 2 hours at A s)
Thermal stability (residual (ggalactosidase activity after a stop of 15 minutes at pH 6),%, at temperature, C
60
Relative
100
22i (
186
About
120,000
4.5
3.5-8 50
Less than 60
3.5-8.0
2.5-8.0
50 .
100
65
70
75
The effect of metallic ions with a concentration of 10
Iron () Copper () Mercury (Nd)
Example 1. A solid culture medium consisting of 10 g of wheat bran, 10 g of defatted soy flour and 20 ml of water is loaded into a 500 ml conical flask and sterilized by autoclaving at 15 min and then infected with an oblique culture of Penici11ium multicolor KU-0-132 . The contaminated medium is then incubated in sterile air at 28 ° C. for k-days and then mixed with 200 ml of aqueous y-galactosidase extract in the aqueous phase. The mixture is filtered to remove solids. The resulting filtrate, i.e. aqueous extract, detects p-galactosidase activity of 228 units / ml.
Example 2. A liquid culture medium (100 ml) containing 3 rice bran, 1 flour of cotton seeds, 0.25t, potassium hydrogen phosphate and 0.15% potassium phosphate (pH 6.2) is loaded into a 500 ml flask and heat sterilized in autoclave, sterilization is not nearly inhibited
Almost inhibited
Almost INGIBITATED
The medium is inoculated with an oblique culture of Penicipium multicolor KU-0-132 and cultured with agitation at 28 ° C for 3 days on an agitating table. The incubated medium is filtered. The resulting filtrate detects j-galactosidase activity at 140.
Example 3aJ A solid culture medium consisting of a uniform mixture of 1.5 kg of defatted soy flour, 1.5 kg of cotton seed flour and 3 liters of water is placed as a layer in a large tank and sterilized by heating in an autoclave.
Sterilized medium is contaminated with 150 g of a seed culture of Penici11ium multicolor KU-0-132, obtained by incubating an oblique culture of this microorganism in bran medium (a mixture of wheat bran and water in a 1: 1 ratio by weight). Then the infected medium is quietly incubated at 5 days and incubated
权利要求:
Claims (1)
[1]
Claim
A method for producing p-galactosidase, which involves culturing a peniciIlium strain of the microorganism producing it on a nutrient medium containing assimilable carbon and nitrogen sources with or without mineral salts, under aerobic conditions, followed by isolation of the enzyme from the culture fluid, characterized in that, in order to increase the resistance and the activity of the target product, Penici11iurn multicolor KU-O-312, identified as FERM-P4375 or ATCC 20539, is used as the producing microorganism, and as source a ota - bran.
类似技术:
公开号 | 公开日 | 专利标题
WO2000058491A1|2000-10-05|Novel substances kf-1040t4a, kf-1040t4b, kf-1040t5a and kf-1040t5b and process for producing the same
JP2993767B2|1999-12-27|FO-1289A substance and method for producing the same
IE893482L|1990-04-28|The glycosidase inhibitor salbostatin, process for its¹preparation, and its use
US3649455A|1972-03-14|Production of lipase
US4283494A|1981-08-11|Microbial lipase, process for its preparation and microbiologically pure culture therefor
SU952111A3|1982-08-15|Process for producing beta-galactozeidaze
US3597325A|1971-08-03|Production of 3-|-4-chloro-pyrrole
US20040253694A1|2004-12-16|Process for the preparation of gallic acid by co-culture
US20080227164A1|2008-09-18|Process For Producing Mycophenolic Acid Using Penicillium Arenicola Bicc 7673
CN106047713A|2016-10-26|Talaromyces pinophilum strain Li-93 and application thereof
US3980520A|1976-09-14|Process for the production of l-malic acid by microbiological fermentation and means suitable for carrying out the same
SU539538A3|1976-12-15|Method for producing metabolite 2776
GB2086394A|1982-05-12|B-galctosidase inhibitor designated gt-2558 and derivatives thereof and microorganism for use in their preparation
DE3116856C2|1989-08-17|
CN109456898A|2019-03-12|A kind of the fermentation preparation and its application of chaetomium globosum dextranase
US3808102A|1974-04-30|Process for preparing alpha amylase
CN108410749A|2018-08-17|The method that marine low temperature | gamma-lactam enzyme asymmetric hydrolysis prepares | gamma-lactam
JP2710834B2|1998-02-10|FO-608A substance and method for producing the same
US4007090A|1977-02-08|Novel fermentation process for the preparation of Sulfomycin
US11279961B2|2022-03-22|Aspergillus oryzae BLCY-006 strain and application thereof in preparation of galactooligosaccharide
US2886490A|1959-05-12|Process of producing cobalamines by fermenting culture media with nocardia rugosa
CA3121566C|2022-03-01|Aspergillus oryzae blcy-006 strain and application thereof in preparation of galactooligosaccharides
CA1334741C|1995-03-14|Method for production of a growth factor for bifidobacterium sp
CN111073830B|2021-07-23|Lactobacillus casei with high yield of gamma-glutamyltranspeptidase and application thereof in production of L-theanine
US3898133A|1975-08-05|Process of preparing an enzyme with lipolytic activity
同族专利:
公开号 | 公开日
DE2904225C2|1985-11-14|
US4229539A|1980-10-21|
JPS54105290A|1979-08-18|
IT1165933B|1987-04-29|
GB2014154A|1979-08-22|
GB2014154B|1982-06-03|
FR2422680B1|1983-02-04|
JPS5915626B2|1984-04-10|
AU524893B2|1982-10-07|
DE2904225A1|1979-08-09|
FR2422680A1|1979-11-09|
AU4387879A|1979-08-16|
CH641837A5|1984-03-15|
NL7900762A|1979-08-08|
IT7909337D0|1979-02-05|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题

IL85581A|1987-05-21|1992-05-25|Technicon Instr|Substrate for beta-galactosidase comprising derivatives of 4-nitrophenyl-beta-d-galactopyranoside and beta-galactosidase immunoassay containing said substrate|
AT131869T|1990-03-16|1996-01-15|Suntory Ltd|HEAT-RESISTANT BETA-GALACTOSYL TRANSFERASE, THEIR PRODUCTION PROCESS AND THEIR USE|
US5234828A|1990-03-16|1993-08-10|Suntory Limited|Process for producing novel heat-resistant β-galactosyltransferase|
US5744345A|1992-10-05|1998-04-28|Takara Shuzo Co., Ltd.|Hyperthermostable β-galactosidase gene, enzyme encoded thereby, and process for production|
US6428786B1|1993-09-28|2002-08-06|Mcneil-Ppc, Inc.|Composition and method for lactose hydrolysis|
US6057139A|1995-06-29|2000-05-02|Mcneil-Ppc, Inc.|Preblend of microcrystalline cellulose and lactase for making tablets|
AT357153T|2001-09-27|2007-04-15|Amano Enzyme Inc|PROCESS FOR PRODUCING BREW LEAF OR BREWERY EXTRACT WITH IMPROVED TASTE|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
JP53012102A|JPS5915626B2|1978-02-06|1978-02-06|
[返回顶部]