CN101948820A - Acidic proteinase and preparation method thereof - Google Patents

Acidic proteinase and preparation method thereof Download PDF

Info

Publication number
CN101948820A
CN101948820A CN 201010265354 CN201010265354A CN101948820A CN 101948820 A CN101948820 A CN 101948820A CN 201010265354 CN201010265354 CN 201010265354 CN 201010265354 A CN201010265354 A CN 201010265354A CN 101948820 A CN101948820 A CN 101948820A
Authority
CN
China
Prior art keywords
aspergillus niger
fermentation
enzyme
preparation
raw material
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
CN 201010265354
Other languages
Chinese (zh)
Inventor
王兴吉
郭庆文
王春生
王克芬
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong Longkete Enzyme Preparation Co Ltd
Original Assignee
Shandong Longkete Enzyme Preparation Co Ltd
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
Application filed by Shandong Longkete Enzyme Preparation Co Ltd filed Critical Shandong Longkete Enzyme Preparation Co Ltd
Priority to CN 201010265354 priority Critical patent/CN101948820A/en
Publication of CN101948820A publication Critical patent/CN101948820A/en
Pending legal-status Critical Current

Links

Abstract

The invention relates to an acidic proteinase and a preparation method thereof and the acidic proteinase belongs to the microbial acidic proteinase. The invention is characterized in that 1) the enzymatic characteristics of the acidic proteinase are as follows: the optimum pH value is 2.5-3.5, the stable pH value is 2.5-6.0; the optimum temperature is 40-50 DEG C, the temperature stability range is 30-50 DEG C; and 2) the preparation method uses Aspergillus Niger which is stored in the China Center of Industrial Culture Collection (CICC) and has a preservation number of 2238, as the enzyme-producing strain and uses wheat bran as the raw material; the solid fermentation technology is adopted for preparation; the fermentation and enzyme-producing capability is not less than 47000u/g (dry yeast), the liquid enzyme yield is not less than 85% and the soid enzyme yield is not less than 80%, which all achieve the food grade sanitation standard. The invention provides the acidic proteinase and the preparation method thereof, wherein the utilization rate of the fermentation equipment is high, the byproduct of crop processing is used as the main raw material, the enzyme activity for fermentation is high, the extracting and purifying rate of enzyme is high and the production cost is low. The acidic proteinase of the invention is suitable to be used as the raw material or product additive of the products in the leather industry, the pharmaceutical industry, the brewing industry and the feed industry.

Description

Aspartic protease and preparation method thereof
Technical field
The present invention is a kind of aspartic protease and preparation method thereof.Belonging to the aspartic protease from microbial source, is the zymogenic bacteria kind with aspergillus niger (A.niger) particularly, adopts aspartic protease of solid fermentation process preparation and preparation method thereof.
Background technology
Aspartic protease can be in sour environment protein hydrolysate, be widely used in tanning industry, pharmaceutical sector, Brewing industry and fodder industry.Aspartic protease can obviously promote growing of young animal as a kind of novel fodder additives, reduces the stress effect that wean brings, and feeding effect highly significant is the boundless zymin of a class application prospect.
In the prior art, aspartic protease mainly adopts liquid-state fermentation technology, and the fermentation equipment utilization ratio is low, is carbon source with corn, soybean mainly, consumes a large amount of valuable grain resources; The fermenting enzyme vigor is low, enzyme extraction, purification yield are low; Cause the products production cost to rise.
A kind of fermentation equipment utilization ratio height is a main raw material with the grain processing by product, and fermenting enzyme vigor height, enzyme extraction purification yield height, aspartic protease that production cost is lower and preparation method thereof are that people expect.
Summary of the invention
The objective of the invention is to avoid above-mentioned weak point of the prior art, and provide a kind of fermentation equipment utilization ratio height, with the grain processing by product is main raw material, fermenting enzyme vigor height, enzyme extraction purification yield height, aspartic protease that production cost is lower and preparation method thereof.
Purpose of the present invention can reach by following measure:
Aspartic protease of the present invention is characterized in that:
A. enzymatic property: optimal pH 2.5-3.5, stablize pH2.5-6.0; Optimum temperature is 40 ℃-50 ℃, and the temperature stability scope is 30 ℃-50 ℃;
B. with aspergillus niger (Aspergillus niger), be preserved in CICC numbering 2238 and be the zymogenic bacteria kind, wheat bran is main raw material, adopts solid fermentation, immersion extraction, filtering and concentrating, dissolved purifying, ultrafiltration, the preparation of smart filtering technology, reaches following technical indicator:
1. enzymatic production ability: 〉=47000u/g (in dry medium),
2. soak extraction, ultrafiltration, smart filter, liquid enzymes yield 〉=85%, solid enzyme yield 〉=80% reaches the food grade hygienic standard.
The present inventor finds unexpectedly, by the cereal shell or not hulled grain participate in can making aspergillus niger (Aspergillus niger) as the solid fermentation main culture based raw material, the enzymatic productivity that is preserved in CICC numbering 2238 significantly improves.Wheat bran is as the by-product of whole meal flour processing industry, and the source is abundant.Selecting wheat bran for use is that main carbon source had both been saved valuable grain resource, has improved aspergillus niger (Aspergillus niger) again, is preserved in the enzymatic productivity of CICC numbering 2238.For productive rate and its production cost of reduction of improving aspartic protease of the present invention are made great contributions to.With aspergillus niger (Aspergillus niger), be preserved in CICC numbering 2238 and be the zymogenic bacteria kind, adopt the solid fermentation process method, improve the utilization ratio that feeds intake of fermentation equipment greatly, thereby improved the throughput of equipment.Soak the enforcement of extraction, ultrafiltration and concentration, dissolved purifying, ultrafiltration, smart filter, vacuum drying process, for the raising of enzyme extraction purification yield provides technical support.
Purpose of the present invention can also reach by following measure:
Aspartic protease of the present invention, it is characterized in that the aspergillus niger described in the b (Aspergillus niger), be preserved in CICC and number 2238 zymogenic bacteria kinds with cobalt 60 rays, the processing of excess ultraviolet mutagenesis, give and produce aspartic protease bacterial strain (Aspergillus niger), be preserved in CICC and number good characteristics such as 2238 stabilization characteristics of genetics are good, product enzyme speed is fast, product enzyme level height.The performance and the productive rate that improve aspartic protease of the present invention have been brought into play active effect.
Aspartic protease of the present invention is characterized in that moisture content in the solid fermentation raw material between 40%-50%, is an optimized technical scheme.
The preparation method of aspartic protease of the present invention is characterized in that comprising the steps:
A. liquid spawn is cultivated in advance: substratum 10-25 weight part, add water to 100 weight parts, and regulate pH to 4.6-5.0, sterilized 10-35 minute for 121 ℃, be cooled to 30 ℃-35 ℃, insert bacterial classification aspergillus niger (Aspergillus niger), be preserved in CICC numbering 2238, get the pre-nutrient solution of liquid spawn; 30 ℃-40 ℃ of controlled temperature, ventilation 45-60m 3/ h, pressure 0.05Mpa-0.08Mpa cultivated 28-32 hour, got liquid spawn, was equipped with solid state fermentation and used;
B. solid state fermentation: 120 ℃-123 ℃ of raw materials boiling 50-60 minute, be cooled to 30 ℃-35 ℃, insert the liquid spawn of dilution, stir evenly, make material initial water content 40-50%, ventilation: 50-60m 3/ h, culture cycle 5.0 days; Fermentation level 〉=47000u/g (in dry medium);
C. adopt and soak extraction, filtering and concentrating, dissolved purifying, ultrafiltration, smart filter, pH to 4.3 ± 0.1, liquid enzymes yield 〉=85%, solid enzyme yield 〉=80% reaches the food grade hygienic standard.
Aspartic protease of the present invention is used, and it is characterized in that being applicable to preparation raw material or product additive as tanning industry, pharmaceutical sector, Brewing industry and fodder industry product.
Technical scheme of the present invention has outstanding substantive distinguishing features and obvious improvement compared to existing technology, implements the back and produces following positively effect:
1. a kind of fermentation equipment utilization ratio height is provided, and is main raw material with the grain processing by product, fermenting enzyme vigor height, enzyme extraction purification yield height, aspartic protease that production cost is lower and preparation method thereof.
2. selecting wheat bran for use is that main raw material had both been saved valuable grain resource, has improved aspergillus niger (Aspergillus niger) again, is preserved in the enzymatic productivity of CICC numbering 2238.
3. with aspergillus niger (Aspergillus niger), be preserved in CICC numbering 2238 and be the zymogenic bacteria kind, adopt the solid fermentation process method, improved the utilization ratio that feeds intake of fermentation equipment greatly, thereby improved the throughput of equipment.
4. soak the enforcement of extraction, filtering and concentrating, dissolved purifying, ultrafiltration, smart filtering technology, for the raising of enzyme extraction purification yield provides technical support.
5. aspartic protease is applicable to preparation raw material or the product additive as tanning industry, pharmaceutical sector, Brewing industry and fodder industry product.For the user has won benefit.
Embodiment
The present invention is described in further detail below in conjunction with embodiment:
Embodiment 1
A. liquid spawn is cultivated in advance: with 100 kilograms in dextrin, and 10 kilograms of peptones, 5 kilograms of yeast extract pastes, 20 kilograms of corn steep liquors drop in the 1000L reactor, add water to 1000 kilograms of total charging capacitys, and regulate pH to 5.0; Be warming up to 121 ℃, insulated sterilizing 35 minutes.Be cooled to 30 ℃, insert aspergillus niger (Aspergillus niger), be preserved in CICC numbering 2238, get the pre-nutrient solution of liquid spawn; 30 ℃ of controlled temperature, ventilation 60m 3/ h, jar internal pressure 0.05Mpa-0.08Mpa, culture cycle 32 hours gets liquid spawn, is equipped with solid fermentation and uses;
B. solid fermentation: 3000 kilograms in wheat bran, under 121 ℃ of temperature, boiling 60 minutes; Be cooled to 35 ℃; Stir the liquid spawn of inserting down through water-reducible step a preparation, stir, the initial water content that makes fermentation raw material is at 40%-50%; At 35 ℃ of temperature, ventilation 60m 3/ h, fermentation culture 5.0 days, fermentation level: 〉=47000u/g (in dry medium);
C. adopt and soak extraction, ultrafiltration and concentration, dissolved purifying, ultrafiltration, smart filter, adjusting pH to 4.3 ± 0.1, the allotment can, liquid enzymes yield 〉=85% reaches the food grade hygienic standard.
Embodiment 2
A. liquid spawn is cultivated in advance: with 100 kilograms of starch, and 10 kilograms of peptones, 5 kilograms of yeast extract pastes, 20 kilograms of corn steep liquors, alpha-amylase 1000ml, 0.5 kilogram in calcium chloride drops in the 1000L reactor, adds water to 1000 kilograms of total charging capacitys, and regulates pH to 5.0; Be warming up to 121 ℃, insulated sterilizing 35 minutes.Be cooled to 30 ℃, insert aspergillus niger (Aspergillus niger), be preserved in CICC numbering 2238, get the pre-nutrient solution of liquid spawn; 30 ℃ of controlled temperature, ventilation 60m 3/ h, jar internal pressure 0.05Mpa-0.08Mpa, culture cycle 35 hours gets liquid spawn, is equipped with solid fermentation and uses;
B. solid fermentation: 3000 kilograms in wheat bran, under 123 ℃ of temperature, boiling 50 minutes; Be cooled to 35 ℃; Stir the liquid spawn of inserting down through water-reducible step a preparation, stir, the initial water content that makes fermentation raw material is 50%; At 30 ℃ of temperature, ventilation 50m 3/ h, fermentation culture 5.0 days, fermentation level: 〉=47000u/g (in dry medium);
C. adopt and soak extraction, filtering and concentrating, dissolved purifying, ultrafiltration, smart filter, regulate pH to 4.3 ± 0.1, the allotment can, liquid enzymes yield 〉=85% reaches the food grade hygienic standard.
Embodiment 3
A. liquid spawn is cultivated in advance: with 100 kilograms of malt syrups, and 10 kilograms of peptones, 5 kilograms of yeast extract pastes, 20 kilograms of corn steep liquors, 12 kilograms of soybean cake powder drop in the 1000L reactor, add water to 1000 kilograms of total charging capacitys, and regulate pH to 4.8; Be warming up to 121 ℃, insulated sterilizing 35 minutes.Be cooled to 30 ℃, insert aspergillus niger (Aspergillus niger), be preserved in CICC numbering 2238, get the pre-nutrient solution of liquid spawn; 30 ℃ of controlled temperature, ventilation 60m 3/ h, jar internal pressure 0.05Mpa-0.08Mpa, culture cycle 28 hours gets liquid spawn, is equipped with solid fermentation and uses;
B. solid fermentation: 3000 kilograms in wheat bran, under 123 ℃ of temperature, boiling 50 minutes; Be cooled to 32 ℃; Stir the liquid spawn of inserting down through water-reducible step a preparation, stir, the initial water content that makes fermentation raw material is 40%; At 32 ℃ of temperature, ventilation 50m 3/ h, fermentation culture 5.0 days, fermentation level: 〉=47000u/g (in dry medium);
C. adopt and soak extraction, filtering and concentrating, dissolved purifying, ultrafiltration, smart filter, adjusting pH to 4.3 ± 0.1, vacuum-drying, packing.Solid enzyme yield 〉=80% reaches the food grade hygienic standard.

Claims (5)

1. aspartic protease is characterized in that:
A. enzymatic property: optimal pH 2.5-3.5, stablize pH2.5-6.0; Optimum temperature is 40 ℃-50 ℃, and the temperature stability scope is 30 ℃-50 ℃;
B. with aspergillus niger (Aspergillus niger), be preserved in CICC numbering 2238 and be the zymogenic bacteria kind, wheat bran is main raw material, adopts solid fermentation, immersion extraction, filtering and concentrating, dissolved purifying, ultrafiltration, the preparation of smart filtering technology, reaches following technical indicator:
1. enzymatic production ability: 〉=47000u/g (in dry medium),
2. soak extraction, ultrafiltration, smart filter, liquid enzymes yield 〉=85%, solid enzyme yield 〉=80% reaches the food grade hygienic standard.
2. according to the aspartic protease of claim 1, it is characterized in that the aspergillus niger described in the b (Aspergillus niger), be preserved in CICC and number 2238 zymogenic bacteria kinds with cobalt 60 rays, the processing of excess ultraviolet mutagenesis, give and produce aspartic protease bacterial strain (Aspergillus niger), be preserved in CICC and number good characteristics such as 2238 stabilization characteristics of genetics are good, product enzyme speed is fast, product enzyme level height.
3. according to the aspartic protease of claim 1, it is characterized in that moisture content in the solid fermentation raw material is between 40%-50%.
4. the preparation method of the aspartic protease of a claim 1 is characterized in that comprising the steps:
A. liquid spawn is cultivated in advance: substratum 10-25 weight part, add water to 100 weight parts, and regulate pH to 4.6-5.0, sterilized 10-35 minute for 121 ℃, be cooled to 30 ℃-35 ℃, insert bacterial classification aspergillus niger (Aspergillus niger), be preserved in CICC numbering 2238, get the pre-nutrient solution of liquid spawn; 30 ℃-40 ℃ of controlled temperature, ventilation 45-60m 3/ h, pressure 0.05Mpa-0.08Mpa cultivated 28-32 hour, got liquid spawn, was equipped with solid state fermentation and used;
B. solid state fermentation: 120 ℃-123 ℃ of raw materials boiling 50-60 minute, be cooled to 30 ℃-35 ℃, insert the liquid spawn of dilution, stir evenly, make material initial water content 40%-50%, ventilation: 50-60m 3/ h, culture cycle 5.0 days; Fermentation level 〉=47000u/g (in dry medium);
C. adopt and soak extraction, filtering and concentrating, dissolved purifying, ultrafiltration, smart filter, pH to 4.3 ± 0.1, liquid enzymes yield 〉=85%, solid enzyme yield 〉=80% reaches the food grade hygienic standard.
5. the aspartic protease of claim 1 is used, and it is characterized in that being applicable to preparation raw material or product additive as tanning industry, pharmaceutical sector, Brewing industry and fodder industry product.
CN 201010265354 2009-08-27 2010-08-27 Acidic proteinase and preparation method thereof Pending CN101948820A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201010265354 CN101948820A (en) 2009-08-27 2010-08-27 Acidic proteinase and preparation method thereof

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CN200910017983.9 2009-08-27
CN200910017983A CN101638647A (en) 2009-08-27 2009-08-27 Acid protease and preparation method thereof
CN 201010265354 CN101948820A (en) 2009-08-27 2010-08-27 Acidic proteinase and preparation method thereof

Publications (1)

Publication Number Publication Date
CN101948820A true CN101948820A (en) 2011-01-19

Family

ID=41613827

Family Applications (2)

Application Number Title Priority Date Filing Date
CN200910017983A Pending CN101638647A (en) 2009-08-27 2009-08-27 Acid protease and preparation method thereof
CN 201010265354 Pending CN101948820A (en) 2009-08-27 2010-08-27 Acidic proteinase and preparation method thereof

Family Applications Before (1)

Application Number Title Priority Date Filing Date
CN200910017983A Pending CN101638647A (en) 2009-08-27 2009-08-27 Acid protease and preparation method thereof

Country Status (1)

Country Link
CN (2) CN101638647A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102994485A (en) * 2012-12-24 2013-03-27 湖南鸿鹰生物科技有限公司 Method for preparing acid proteinase
CN105199969A (en) * 2015-10-19 2015-12-30 山东隆科特酶制剂有限公司 Aspergillus niger strain capable of highly producing acidic protease and method for fermenting aspergillus niger strain liquid to produce enzymes
CN105316308A (en) * 2014-08-04 2016-02-10 湖南新鸿鹰生物工程有限公司 High-activity acid protease
CN112940943A (en) * 2019-12-11 2021-06-11 安琪酵母股份有限公司 Bacterial strain for producing acid protease by liquid fermentation and application

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101638647A (en) * 2009-08-27 2010-02-03 山东隆科特酶制剂有限公司 Acid protease and preparation method thereof
MD4186C1 (en) * 2012-02-20 2013-06-30 Институт Микробиологии И Биотехнологии Академии Наук Молдовы Strain of fungus Fusarium gibbosum - producer of acid and neutral proteases, xylanases and b-glucosidases
CN105950607A (en) * 2016-05-25 2016-09-21 浙江工业大学 Selecting method of acid proteinase high-yield strains obtained through induced mutation by 60Co-gamma rays
CN107384900B (en) * 2017-08-01 2019-08-27 中国农业科学院饲料研究所 The acid protease 6749 and its gene of a kind of originated from fungus and application

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101638647A (en) * 2009-08-27 2010-02-03 山东隆科特酶制剂有限公司 Acid protease and preparation method thereof
CN101671659A (en) * 2009-09-25 2010-03-17 山东隆科特酶制剂有限公司 Pectase and preparation method thereof

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101638647A (en) * 2009-08-27 2010-02-03 山东隆科特酶制剂有限公司 Acid protease and preparation method thereof
CN101671659A (en) * 2009-09-25 2010-03-17 山东隆科特酶制剂有限公司 Pectase and preparation method thereof

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
《中国调味品》 20090331 姚菁华等 酱油固态发酵生产中黑曲霉产酶条件的优化研究 第34卷, 第3期 2 *
《食品科学》 20031231 袁康培等 黑曲霉HU53 菌株产酸性蛋白酶的条件和酶学性质 第24卷, 第8期 2 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102994485A (en) * 2012-12-24 2013-03-27 湖南鸿鹰生物科技有限公司 Method for preparing acid proteinase
CN102994485B (en) * 2012-12-24 2016-08-24 湖南鸿鹰生物科技有限公司 A kind of method producing acid protease
CN105316308A (en) * 2014-08-04 2016-02-10 湖南新鸿鹰生物工程有限公司 High-activity acid protease
CN105199969A (en) * 2015-10-19 2015-12-30 山东隆科特酶制剂有限公司 Aspergillus niger strain capable of highly producing acidic protease and method for fermenting aspergillus niger strain liquid to produce enzymes
CN105199969B (en) * 2015-10-19 2019-05-14 山东隆科特酶制剂有限公司 The Aspergillus niger strain and its liquid fermentation enzyme producing method of one plant height production acid protease
CN112940943A (en) * 2019-12-11 2021-06-11 安琪酵母股份有限公司 Bacterial strain for producing acid protease by liquid fermentation and application

Also Published As

Publication number Publication date
CN101638647A (en) 2010-02-03

Similar Documents

Publication Publication Date Title
CN104996722B (en) A kind of method of the step combined ferment feed of multi-cultur es two
CN101948820A (en) Acidic proteinase and preparation method thereof
CN102934736B (en) Method for preparing sweet potato skin/ sweet potato powder dreg fermented feed
CN103609862B (en) Method for improving feeding nutritive value of sesame seed meal by combining enzymolysis method with fermentation method
CN103535511A (en) Method for producing feed with rich peptide and rich prebiotics by fermenting high-temperature soybean meal
CN101454438B (en) Nutritional supplement for alcoholic fermentation media
CN105950481B (en) One Aspergillus oryzae bacterial strain and its protease of generation are produced applied to yeast extract
CN104388514A (en) Method for preparing gamma-aminobutyric acid by virtue of fermentation of composite bacteria
CN111593036B (en) Preparation of enzyme preparation mainly containing acid protease, strain and application thereof
CN106922952B (en) Method for preparing polypeptide-rich protein feed additive by solid state fermentation of aspergillus oryzae
CN109198167A (en) Yeast for animal feeds hydrolysate and its preparation method and application
CN106417900A (en) Processing method and application of bean pulp for feed
JP6946277B2 (en) How to concentrate protein in flour
CN103355477A (en) Production method for feed through fermentation of soy sauce residues
CN106804875A (en) A kind of sweet potato residue fermented feed and preparation method and application
CN110747188B (en) Method for producing keratinase
RU2396007C1 (en) Method of complex processing grain raw material for alcohol and feed products enriched in lysine
CN101638645A (en) Method for producing xylanase by solid mechanical fermentation
CN106173187A (en) The preparation method of a kind of vegetable protein hydrolyzate containing prolease activity and application
CN110269248A (en) A kind of production method of natto brown rice enzyme powder
CN106666076B (en) Strain composition suitable for fermenting needle mushroom residues and brewer's grains and application thereof
CN114015579B (en) Aureobasidium pullulans capable of producing beta-glucan in high yield and application of aureobasidium pullulans
CN110747128B (en) Bacillus licheniformis strain capable of producing keratinase in high yield and application thereof
CN101671659A (en) Pectase and preparation method thereof
CN113966695A (en) Hypsizigus marmoreus culture medium and preparation method and application thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20110119