CN100366737C - Production of curing lactase - Google Patents

Production of curing lactase Download PDF

Info

Publication number
CN100366737C
CN100366737C CNB2006100097568A CN200610009756A CN100366737C CN 100366737 C CN100366737 C CN 100366737C CN B2006100097568 A CNB2006100097568 A CN B2006100097568A CN 200610009756 A CN200610009756 A CN 200610009756A CN 100366737 C CN100366737 C CN 100366737C
Authority
CN
China
Prior art keywords
solution
lactase
enzyme
cell
preparation
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.)
Active
Application number
CNB2006100097568A
Other languages
Chinese (zh)
Other versions
CN1818061A (en
Inventor
肖雯娟
林枫翔
梁金钟
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.)
Harbin Meihua Biotechnology Co., Ltd.
Original Assignee
HARBIN MEIHUA BIOTECHNOLOGY 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 HARBIN MEIHUA BIOTECHNOLOGY CO Ltd filed Critical HARBIN MEIHUA BIOTECHNOLOGY CO Ltd
Priority to CNB2006100097568A priority Critical patent/CN100366737C/en
Publication of CN1818061A publication Critical patent/CN1818061A/en
Application granted granted Critical
Publication of CN100366737C publication Critical patent/CN100366737C/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Dairy Products (AREA)

Abstract

The present invention relates to a production method of immobilized lactase, which comprises the following steps of preparation of Kluyveromyces fragilis suspension, enzyme wall prebreaking treatment, freeze thawing and wall breaking, final wall breaking of a high-pressure refiner, preparation of immobilized vector solution, preparation of lactase immobilized vector solution, preparation of immobile liquid, immobilized treatment, etc. The present invention uses immobilized lactase to produce low-lactose milk. The present invention is characterized in that continuous treatment can be carried out, and immobilized enzymes can not lose along with liquid milk and can be recovered to be repeatedly used so that the production cost of lactose milk is reduced.

Description

Production of curing lactase
(1) technical field
What the present invention relates to is a kind of production method of microbial preparation, the production method of specifically a kind of microorganism cells broken wall and immobilized lactase.
(2) background technology
The enzyme that can reduce lactose among the human small intestine has Sumylact L (lactase) and beta-galactosidase enzymes, and (β-galactosidase), Sumylact L is positioned at the mucous membrane of small intestine brush border, and beta-galactosidase enzymes is positioned at lysosome, can not decompose the lactose in the enteric cavity.Lactase deficiencies is meant that the membrane bound enzyme of intestinal brush border chorionic cells is that lactase activity is low.Lactase deficiencies has three types: (1) congenital lactase deficiency: being meant the low or shortage of body lactase activity when being born, is on the body euchromosome due to the recessive gene, and this type is rarely found.(2) secondary lactase deficiency: be meant that the temporary lactase activity that causes the small intestine epithelium damage to cause owing to a variety of causes is low, as: diseases such as infectious diarrhea, immunoglobulin deficiency, celiac disease, regional ileitis, malnutrition, can after the organism disease rehabilitation, recover normal.(3) primary lactase deficiencies (claiming the adult type lactase deficiencies again): be modal a kind of, not by due to the influence of disease, mainly be to cause because lactase activity reduced gradually with the age, time of origin because of race with different from different places, behind weaning baby, just begin to take place, begin to occur during 20 years old left and right sides having.Population of China is many to be taken place in the time of 7~8 years old.It is generally acknowledged that lactase deficiencies is relevant with the different genetic gene mutations that cause of food habits that form from generation to generation.The lactase deficiencies incidence changes with country variant, different ethnic populations' variation.Europe crowd's 30% above lactase deficiencies, the asian population lactase deficiencies accounts for 75%~100%, the white American 12%, Black people 70%, Africa 90%~100%; Japan 100%, 3~13 years old children's lactase deficiencies incidence of China is 87%.
After lactose in the cow's milk entered small intestine, because the shortage of Sumylact L, lactose can not be broken down into glucose and semi-lactosi is absorbed, and is called lactose maldigestion and lactose malabsorption.After lactose enters colon, generated short chain organic acid such as acetic acid, propionic acid, butyric acid etc. and gas such as methane, H by fermentation using bacteria 2, CO 2Deng, the lactose fermentation process can cause borborygmus, stomachache, rectum gas and osmotic diarrhea, is called lactose intolerance when having these symptoms, serious lactose maldigestion or malabsorption are many to be taken place to a few hours after taking in a certain amount of lactose in 30 minutes.Lactose intolerance is bigger to infant's influence, semi-lactosi is the important substance of brain normal development, Sumylact L can not be decomposed into glucose with lactose and semi-lactosi is absorbed owing to lack, therefore, children's growth retardation, brain development also there is certain influence, and can be simultaneously with phenomenons such as vomitings, the adult is sometimes with the reaction of feeling sick.Have the people about 20% to have the lactose intolerance symptom among the lactase deficiencies person, and lactose intolerance symptom individual difference is very big.The lactose yield of what and severity of intolerance shape and the interior lactase activity of small intestine, absorption and whether to take in other based food simultaneously relevant, so produce low lactose milk and have crucial meaning.
But it is more expensive to produce the used Sumylact L price of low lactose milk, and this has just increased the production cost of liquid milk and milk powder, so low lactose milk is on the high side, and market sale is subjected to certain influence, if adopt immobilized lactase just can address this problem.Because immobilized lactase can not run off with milk liquid, can reclaim repeatedly and use, reduce production costs greatly.
(3) summary of the invention
The object of the present invention is to provide a kind of can the processing continuously, immobilized enzyme can not run off with liquid milk, can reclaim repeated use, reduces the production of curing lactase of the production cost of low lactose milk.
The object of the present invention is achieved like this:
1, the preparation of Kluyveromyces fragilis bacteria suspension:
To cultivate sophisticated Kluyveromyces fragilis cell through the 10000r/min high speed centrifugation, and obtain fresh active somatic cells, somatic cells with sterilized water washing 1-2 time, is mixed with the cell bacteria suspension with sterilized water then, cell concn is 5.0%-40.0%;
2, the pre-broken wall treatment of enzyme:
Get above-mentioned bacteria suspension 500mL, add proteolytic enzyme and beta-glucanase, proteolytic enzyme consumption 1.0-150.0u/g wet thallus, beta-glucan enzyme dosage 1.0-100u/g wet thallus, pH6.0-7.0,30 ℃-65 ℃ are incubated 1-6 hour;
3, freeze thawing broken wall
Cell suspension after enzyme is handled is taken out, places-20 ℃--quick freezing under 50 ℃ of temperature, it is thoroughly freezed, again the refrigerated cell is placed 40 ℃-75 ℃ to melt rapidly, obtain the frozen-thawed cell suspension;
4, the ultimate broken wall of high pressure homogenizer
Place liquid shear shredder assembly high pressure homogenizer to carry out the secondary broken wall cell suspension of freeze thawing, the temperature maintenance of ingress is at 20 ℃-45 ℃, the temperature in exit is not higher than 50 ℃, pressure maintains 30MPa-120MPa, obtain the active lactose enzyme solution of no cell structure, be called Ls solution;
5, preparation fixation support solution
Take by weighing 3.5g-20.0g polyvinyl alcohol (PVA), the 0.5g-10.0g sodium alginate adds 100mL distilled water, stirs 10 minutes, and static immersion 2-24 hour places under 121 ℃ of temperature and sterilized 20 minutes, is cooled to 10 ℃-35 ℃, and this solution is Ps solution;
6, preparation Sumylact L fixation support solution
Measure above-mentioned Ls solution and Ps solution, Ps: Ls is by 1: 1-1: 4, under aseptic condition, thoroughly stir, and this solution is called Ps-Ls solution;
7, preparation stationary liquid
Take by weighing boric acid 1.0-4.0g, calcium chloride 0.5-6.0g adds 100mL water, and heated and stirred is dissolved it, and then, 121 ℃ of temperature were sterilized 20 minutes, were cooled to 10 ℃-35 ℃, and this solution is boric acid-calcium chloride mixed solution;
8, immobilization
Ps-Ls solution is placed nodulizer; gently splash in boric acid-calcium chloride solution, the ratio of Ps-Ls solution and boric acid-calcium chloride solution is by 1: 1-1: 8, and the sclerosis through 2-8 hour; pull out and use the sterilized water washed twice, promptly make the immobilized lactase of solid globules shape.
9, other process for fixation
Immobilized lactase can be done glomeration, thread, column, strip, bulk, film like or the like with other process for fixation.
10, produce low lactose milk with immobilized lactase
Handle fresh cow milk or sterilization breast with immobilized lactase, the ratio of immobilized lactase and cow's milk is 10.0%-100%, the pH nature, and temperature 4-50 ℃, the reaction times is 0.5-5 hour, can produce low lactose liquid milk and low lactose powdered milk.
The present invention adopts immobilization technology, utilize chemistry or physical means with free microorganism cells or enzyme molecule, the area of space that is positioned to limit does not make cell or enzyme molecule leak, and substrate molecule can free in and out, and makes cell and enzyme keep active and repeatedly used a kind of basic fundamental.Immobilization technology comprises enzyme immobilization technology and immobilized cell technology, and process for fixation roughly can be divided into absorption method, covalent attachment method, crosslinking and entrapping method etc., wherein uses comparatively general with entrapping method.Entrapping method can be divided into gel embedding method and microcapsule method, exactly cell is wrapped in the small grid of gel or in the ultra-filtration membrane of semi-permeable membranes polymkeric substance, this method is simple to operate, and less to enzyme and cytoactive influence, the fixed cell carrier intensity of making is higher.Immobilized enzyme has the following advantages: 1. easily with immobilization enzyme-to-substrate, product separately; 2. can carry out batch reactions and dress post successive reaction in a long time; 3. can improve the stability of enzyme; 4. enzyme reaction process can in addition strict control; 5. do not have the residual of enzyme in the product solution, simplified extraction process; 6. be more suitable in multienzymatic reaction than water-soluble enzyme; 7. can increase the yield of product, improve the quality of product; 8. the service efficiency of enzyme improves, and cost reduces.But immobilized enzyme also has its weak point, can only be used for water soluble substrate, and is applicable to the small molecules substrate, and macromolecule substrate is not suitable for; Compare unsuitable multienzymatic reaction with intact cell; Intracellular enzyme must pass through separating of cell wall breaking and enzyme etc.
Produce low lactose milk with immobilized lactase, be characterized in and handle continuously that immobilized enzyme can not run off with liquid milk, can reclaim repeated use, reduce the production cost of low lactose milk.The present invention also relates to handle fresh cow milk, sterilization breast, produce low lactose liquid milk and low lactose powdered milk with immobilized lactase.
(4) embodiment
Get 5000mL and cultivate sophisticated Kluyveromyces fragilis cell fermentation liquid, through the 10000r/min high speed centrifugation, obtain fresh active somatic cells, somatic cells is washed 1-2 time with sterilized water, be mixed with the cell bacteria suspension with sterilized water then, cell concn is 5.0%-40.0%.
Get bacteria suspension 500mL, add proteolytic enzyme and beta-glucanase, proteolytic enzyme consumption 50.0u/g wet thallus, beta-glucan enzyme dosage 20u/g wet thallus, 6.5,42 ℃ of insulations of pH 1.5 hours.
Cell suspension after enzyme is handled is taken out, place quick freezing under-25 ℃ of temperature, it is thoroughly freezed, again the refrigerated cell is placed under 50 ℃ of temperature and melt rapidly, obtain the frozen-thawed cell suspension.
Cell suspension with freeze thawing places liquid shear shredder assembly high pressure homogenizer to carry out the secondary broken wall again, the temperature maintenance of ingress is about 20 ℃, and the temperature in exit is not higher than 50 ℃, and pressure maintains 70MPa, obtain the active lactose enzyme solution of no cell structure, be called Ls solution.
The preparation of immobilized lactase
Take by weighing 13.0g polyvinyl alcohol (PVA), the 5.0g sodium alginate adds 100mL distilled water, stirs 10 minutes, and static immersion 5 hours places under 121 ℃ of temperature and sterilized 20 minutes, is cooled to 35 ℃, and this solution is Ps solution.
Take by weighing boric acid 1.0-4.0g, calcium chloride 0.5-6.0g adds 100mL water, and heated and stirred is dissolved it, and then, 121 ℃ of temperature were sterilized 20 minutes, were cooled to 10 ℃-35 ℃, and this solution is boric acid-calcium chloride mixed solution.
Measure above-mentioned Ls solution and Ps solution, Ps: Ls thoroughly stirs under aseptic condition by 1: 2 mixed, and this solution is called Ps-Ls solution.
500mL places nodulizer with Ps-Ls solution, gently splashes in boric acid~calcium chloride solution, and constantly stirs, and prevents adhesion.The ratio of Ps-Ls solution and boric acid-calcium chloride solution was by 1: 4, and the sclerosis through 3 hours is pulled out and used the sterilized water washed twice, promptly makes the immobilized lactase of solid globules shape.If continuously fast with Ps: Ls solution injects boric acid-calcium chloride solution can obtain thread immobilized lactase.
Immobilized lactase is packed in the container, and then add fresh cow milk, the ratio of immobilized lactase and cow's milk is 50.0%, the pH nature, and 42 ℃ of temperature, the reaction times is 2 hours, can make low lactose liquid milk.

Claims (1)

1. production of curing lactase is characterized in that:
(1) preparation of Kluyveromyces fragilis bacteria suspension:
To cultivate sophisticated Kluyveromyces fragilis cell through the 10000r/min high speed centrifugation, and obtain fresh active somatic cells, somatic cells with sterilized water washing 1-2 time, is mixed with the cell bacteria suspension with sterilized water then, cell concn is 5.0%-40.0%;
(2) the pre-broken wall treatment of enzyme:
Get above-mentioned bacteria suspension 500mL, add proteolytic enzyme and beta-glucanase, proteolytic enzyme consumption 1.0-150.0u/g wet thallus, beta-glucan enzyme dosage 1.0-100u/g wet thallus, pH 6.0-7.0,30 ℃-65 ℃ are incubated 1-6 hour;
(3) freeze thawing broken wall
Cell suspension after enzyme is handled is taken out, places-20 ℃--quick freezing under 50 ℃ of temperature, it is thoroughly freezed, again the refrigerated cell is placed 40 ℃-75 ℃ to melt rapidly, obtain the frozen-thawed cell suspension;
(4) the ultimate broken wall of high pressure homogenizer
Place liquid shear shredder assembly high pressure homogenizer to carry out the secondary broken wall cell suspension of freeze thawing, the temperature maintenance of ingress is at 20 ℃-45 ℃, the temperature in exit is not higher than 50 ℃, pressure maintains 30MPa-120MPa, obtain the active lactose enzyme solution of no cell structure, be called Ls solution;
(5) preparation fixation support solution
Take by weighing 3.5g-20.0g polyvinyl alcohol (PVA), the 0.5g-10.0g sodium alginate adds 100mL distilled water, stirs 10 minutes, and static immersion 2-24 hour places under 121 ℃ of temperature and sterilized 20 minutes, is cooled to 10 ℃-35 ℃, and this solution is Ps solution;
(6) preparation Sumylact L fixation support solution
Measure above-mentioned Ls solution and Ps solution, Ps: Ls is by 1: 1-1: 4, under aseptic condition, thoroughly stir, and this solution is called Ps-Ls solution;
(7) preparation stationary liquid
Take by weighing boric acid 1.0-4.0g, calcium chloride 0.5-6.0g adds 100mL water, and heated and stirred is dissolved it, and then, 121 ℃ of temperature were sterilized 20 minutes, were cooled to 10 ℃-35 ℃, and this solution is boric acid-calcium chloride mixed solution;
(8) immobilization
Ps-Ls solution is placed shaper, gently splash in boric acid-calcium chloride solution, the ratio of Ps-Ls solution and boric acid-calcium chloride solution is by 1: 1-1: 8, and the sclerosis through 2-8 hour is pulled out and is used the sterilized water washed twice, promptly makes the solid immobilized lactase.
CNB2006100097568A 2006-03-01 2006-03-01 Production of curing lactase Active CN100366737C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2006100097568A CN100366737C (en) 2006-03-01 2006-03-01 Production of curing lactase

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2006100097568A CN100366737C (en) 2006-03-01 2006-03-01 Production of curing lactase

Publications (2)

Publication Number Publication Date
CN1818061A CN1818061A (en) 2006-08-16
CN100366737C true CN100366737C (en) 2008-02-06

Family

ID=36918260

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2006100097568A Active CN100366737C (en) 2006-03-01 2006-03-01 Production of curing lactase

Country Status (1)

Country Link
CN (1) CN100366737C (en)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009062132A2 (en) 2007-11-09 2009-05-14 California Institute Of Technology Immunomodulating compounds and related compositions and methods
US20110251156A1 (en) 2010-04-07 2011-10-13 Yue Shen Vehicle for delivering a compound to a mucous membrane and related compositions, methods and systems
JP6273200B2 (en) 2011-07-12 2018-01-31 ザ・ブリガーム・アンド・ウーメンズ・ホスピタル・インコーポレーテッド Lipid-containing PSA compositions, methods of isolation and methods of use
JP2016521284A (en) 2013-05-10 2016-07-21 カリフォルニア インスティチュート オブ テクノロジー Prevention and treatment of colorectal cancer with probiotics
CN103642785B (en) * 2013-11-25 2015-08-12 四川农业大学 A kind of immobilization 3-phenoxy benzoic acid degrading enzyme and preparation method thereof
WO2016201342A1 (en) 2015-06-10 2016-12-15 California Institute Of Technology Sepsis treatment and related compositions methods and systems
EP3337321A4 (en) 2015-08-19 2019-07-17 President and Fellows of Harvard College Lipidated psa compositions and methods
CN105969756A (en) * 2016-05-26 2016-09-28 南京农业大学 Immobilized Helianthus tuberosus L. fructan excision hydrolytic enzyme and preparation method thereof
WO2018014012A1 (en) 2016-07-15 2018-01-18 President And Fellows Of Harvard College Glycolipid compositions and methods of use
CN108064936A (en) * 2016-11-11 2018-05-25 内蒙古伊利实业集团股份有限公司 A kind of preparation method for the liquid diary product for reducing Mei Lade products
CN107252108B (en) * 2017-06-27 2021-01-29 福建农林大学 Lactase microcapsule and preparation method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1258452A (en) * 1998-12-25 2000-07-05 浙江医科大学 Method of producing low-lactose milk with solid thermophilic bacteria lactase
CN1724662A (en) * 2005-07-06 2006-01-25 江南大学 A kind of process for fixation of microbiological lactase and application thereof

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1258452A (en) * 1998-12-25 2000-07-05 浙江医科大学 Method of producing low-lactose milk with solid thermophilic bacteria lactase
CN1724662A (en) * 2005-07-06 2006-01-25 江南大学 A kind of process for fixation of microbiological lactase and application thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
微生物乳糖酶的特性和发展现状. 王敏等.河北农业大学学报,第26(增刊)卷. 2003 *

Also Published As

Publication number Publication date
CN1818061A (en) 2006-08-16

Similar Documents

Publication Publication Date Title
CN100366737C (en) Production of curing lactase
Husain β Galactosidases and their potential applications: a review
CN102199646B (en) Method for preparing collagen peptide with fish skin
CN104382941B (en) A kind of artificial bear gall powder and preparation method thereof
CN102550797B (en) Production method of sea cucumber peptide extract
CN101095458A (en) Method for preparation of spirulina polypeptide
CN101766251A (en) Method for extracting modified plasma protein powder and bioactive peptide for enriching blood from pig blood
Song et al. Optimization of lactulose synthesis from whey lactose by immobilized β-galactosidase and glucose isomerase
CN104846035B (en) A kind of method that sesbania enzyme process prepares galactomannan oligosaccharide
Driss et al. Production and in vitro evaluation of xylooligosaccharides generated from corncobs using immobilized Penicillium occitanis xylanase
CN106520747A (en) Novel immobilized enzyme preparation, and preparation method and application thereof
CN101509030A (en) Hydrolyzation of pig blood with complex enzyme method for producing blood peptide native
CN101805775A (en) Method for preparing collagen from deer sinew
Cregut et al. New insights in agar biorefinery with arylsulphatase activities
CN109468357A (en) A kind of preparation method of spleen aminopeptide
CN102228125B (en) Preparation method of algal active peptide
CN101791039B (en) Method for preparing high-F value pig blood oligopeptide
CN103444979A (en) Method for lowering albumen allergenicity by immobilized enzyme hydrolysis
CN111087486A (en) Novel continuous preparation method of resistant dextrin dietary fiber
Bodnár et al. Synthesis of Galacto-oligosaccharides in milk by using Bifidobacterium bifidum β-galactosidases (Saphera 2600L and Nola Fit 5500) immobilized on chitosan beads
CN107183177A (en) With technique of the waste beer yeast mud for ferment agent for sour milk
CN1916170A (en) Method for producing lactase of neutral liquid
Kumar et al. Continuous hydrolysis of raffinose family oligosaccharides in soymilk by fluidized bed reactor
CN101701226B (en) Method for producing phloretin by enzymatic hydrolysis method
CN103609833A (en) Processing method of potato protein peptide

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Production of curing lactase

Effective date of registration: 20120803

Granted publication date: 20080206

Pledgee: Harbin Enterprise Credit Guarantee Center

Pledgor: Harbin Meihua Biotechnology Co., Ltd.

Registration number: 2012990000424

PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20130620

Granted publication date: 20080206

Pledgee: Harbin Enterprise Credit Guarantee Center

Pledgor: Harbin Meihua Biotechnology Co., Ltd.

Registration number: 2012990000424

PLDC Enforcement, change and cancellation of contracts on pledge of patent right or utility model
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Production of curing lactase

Effective date of registration: 20130916

Granted publication date: 20080206

Pledgee: Harbin enterprise credit guarantee service center

Pledgor: Harbin Meihua Biotechnology Co., Ltd.

Registration number: 2013230000016

PLDC Enforcement, change and cancellation of contracts on pledge of patent right or utility model
ASS Succession or assignment of patent right

Owner name: LIN FENGXIANG

Free format text: FORMER OWNER: HARBIN MEIHUA BIOLOGIC TECHNOLOGY CO., LTD.

Effective date: 20150209

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 150018 HARBIN, HEILONGJIANG PROVINCE TO: 150070 HARBIN, HEILONGJIANG PROVINCE

TR01 Transfer of patent right

Effective date of registration: 20150209

Address after: 150070 Heilongjiang City, Harbin province Daoli District, Heyuan street, No. 18, deputy building A2, room 8, unit 1702, room 2

Patentee after: Lin Fengxiang

Address before: Aijian Binjiang international community 8-8, Shanghai street, Daoli District, Heilongjiang city of Harbin province 150018

Patentee before: Harbin Meihua Biotechnology Co., Ltd.

PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20150728

Granted publication date: 20080206

Pledgee: Harbin enterprise credit guarantee service center

Pledgor: Harbin Meihua Biotechnology Co., Ltd.

Registration number: 2013230000016

PLDC Enforcement, change and cancellation of contracts on pledge of patent right or utility model
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Production of curing lactase

Effective date of registration: 20150805

Granted publication date: 20080206

Pledgee: Harbin enterprise credit guarantee service center

Pledgor: Lin Fengxiang

Registration number: 2015230000019

PLDC Enforcement, change and cancellation of contracts on pledge of patent right or utility model
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20170224

Granted publication date: 20080206

Pledgee: Harbin enterprise credit guarantee service center

Pledgor: Lin Fengxiang

Registration number: 2015230000019

PLDC Enforcement, change and cancellation of contracts on pledge of patent right or utility model
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20170321

Address after: Daoli District Airport Road 150070 in Heilongjiang province Harbin City 2 kilometers Qunli Park 204 room

Patentee after: Harbin Meihua Biotechnology Co., Ltd.

Address before: 150070 Heilongjiang City, Harbin province Daoli District, Heyuan street, No. 18, deputy building A2, room 8, unit 1702, room 2

Patentee before: Lin Fengxiang