CN106380518B - The extraction process of Yolk immunoglobulin - Google Patents

The extraction process of Yolk immunoglobulin Download PDF

Info

Publication number
CN106380518B
CN106380518B CN201610781996.3A CN201610781996A CN106380518B CN 106380518 B CN106380518 B CN 106380518B CN 201610781996 A CN201610781996 A CN 201610781996A CN 106380518 B CN106380518 B CN 106380518B
Authority
CN
China
Prior art keywords
yolk
liquid
sodium chloride
extraction process
yolk immunoglobulin
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.)
Expired - Fee Related
Application number
CN201610781996.3A
Other languages
Chinese (zh)
Other versions
CN106380518A (en
Inventor
李增礼
徐燕
周乐春
王荣海
许培
宋礼华
董世建
倪晓燕
储成风
程婷
陈子镭
沈毅
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.)
ANHUI ANKE BIOTECHNOLOGY (GROUP) Co Ltd
Original Assignee
ANHUI ANKE BIOTECHNOLOGY (GROUP) 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 ANHUI ANKE BIOTECHNOLOGY (GROUP) Co Ltd filed Critical ANHUI ANKE BIOTECHNOLOGY (GROUP) Co Ltd
Priority to CN201610781996.3A priority Critical patent/CN106380518B/en
Publication of CN106380518A publication Critical patent/CN106380518A/en
Application granted granted Critical
Publication of CN106380518B publication Critical patent/CN106380518B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K16/00Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
    • C07K16/12Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from bacteria
    • C07K16/1203Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from bacteria from Gram-negative bacteria
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K16/00Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
    • C07K16/02Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies from eggs
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K2317/00Immunoglobulins specific features
    • C07K2317/10Immunoglobulins specific features characterized by their source of isolation or production
    • C07K2317/11Immunoglobulins specific features characterized by their source of isolation or production isolated from eggs

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Biophysics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Medicinal Chemistry (AREA)
  • Molecular Biology (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Immunology (AREA)
  • Peptides Or Proteins (AREA)
  • Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)

Abstract

The invention discloses a kind of extraction processes of Yolk immunoglobulin comprising following steps: a) prepared by antigen;B) laying hen is immune, collects egg;C) yolk of membrane removal clothing will be gone to stir evenly, is placed at -20 ± 3 DEG C and at least freezes 24-72h, quick-thawing, dilution is adjusted pH, stood overnight;D) centrifugal filtration is concentrated by ultrafiltration, is replaced with sodium chloride solution, ammonium sulfate precipitation, sodium chloride dissolution;E) dialysis, centrifugal filtration are to get Yolk immunoglobulin liquid.Compared with prior art, the present invention carries out the extraction purification of Yolk immunoglobulin using physical-chemical processes such as a series of centrifugation, filtering, precipitating, dialysis, it is not only easy to operate, and extraction cost is low, extraction process is easy to control, and extracted obtained Yolk immunoglobulin can be good at carrying out the treatment of periodontitis, effect is obvious, and extraction process disclosed by the invention can carry out large-scale industrial production.

Description

The extraction process of Yolk immunoglobulin
Technical field
The present invention relates to pharmaceutical technology fields, and in particular to a kind of extraction process of Yolk immunoglobulin.
Background technique
Three kinds of immunoglobulins, i.e. IgG, IgM and IgA are primarily present in carcass, wherein IgG is the principal immune ball egg of fowl It is white, since there are many differences for the characteristic and the IgG characteristic of mammal of fowl IgG, thus fowl IgG is usually referred to as IgY.Work as fowl Body is by can generate corresponding specific immunity antibody after the stimulation of specific antigen, and the IgY antibody that body generates can be from blood In be largely transported in yolk, the antibody being stored in yolk in this way is known as Yolk immunoglobulin.Yolk immunoglobulin is A kind of novel, efficient green preparation to diagnosis, prevents and treats disease caused by bacterium, virus with good effect.
Poultry egg (such as egg) can provide the source IgY, and yield is high, about containing 100~250mg's in one piece of egg IgY, and how efficiently to extract a large amount of Yolk immunoglobulin, this is most important for the extensive use of IgY. In the prior art, it is generally adopted for chicken yolk immune globulin and extraction method progress primary extraction is diluted with water, then in conjunction with salt Analysis with ion exchange in conjunction with, hydrophobic chromatography the methods of in conjunction with gel filtration, however separating effect is bad, is unsuitable on a large scale Production.
Periodontitis is common one of mouth disease, mainly includes at present that drug and operation are controlled for the treatment of periodontitis It treats, wherein be mainly preservative and antimicrobial sustained-release agent for treating the drug of periodontitis, but such drug is easy to produce bacterium Drug resistance and toxic side effect should not be used for a long time.Chinese patent discloses entitled " resisting porphyromonas gingivalis yolk immune globulin The patent of invention of the preparation method (application number 2010101359598) of white vaccine ", the patent are pointed out using porphyromonas gingivalis Immune Laying Hens, the processed manufactured preparation of the chicken yolk immune globulin extracted in this way can be used for the treatment of periodontitis, and effect Significantly.But the patent be during extracting Yolk immunoglobulin use kit it is expensive, specifically, one A kit is only capable of the yolk liquid of processing 200ml or so, therefore the production that can not carry out large-scale Yolk immunoglobulin is pure Change.It can be seen that being directed to efficient, the inexpensive extraction of chicken yolk immune globulin, in technical aspect, there is also many at present Bottleneck.In addition, carrying out the preparation of IgY in the patent using the laying hen without normal immunological, we have found in early stage research, When large-scale breeding, the laying hen without normal immunological is susceptible to suffer from various poultry diseases, and the death rate is high, and the death rate after four months is high Up to 90%, and the death rate of the immunized healthy laying hen after four months is only 1%.Therefore, method disclosed in the prior art is only It can be confined to laboratory, cannot achieve large-scale production.
Summary of the invention
The object of the present invention is to provide the extraction works of a kind of yield and purity is high and Yolk immunoglobulin at low cost Skill.
To achieve the above object, the technical solution adopted by the present invention is that: a kind of extraction process of Yolk immunoglobulin, The following steps are included:
A) prepared by antigen: the unicellular strain of porphyromonas is collected, culture obtains porphyromonas gingivalis body, then inactivate, 3-5 DEG C of overnight, PBS buffer solution washing, is later 1.0 × 10 by concentration11The inactivation thallus of CFU/ml and isometric Freund are helped Agent piping and druming is mixed into Water-In-Oil shape injection;
B) laying hen is immune: the healthy laying hen of 3-5 monthly age isolated rearing is selected, through pigeon breast portion subdermal muscle injecting immune 4 times, and prison It surveys Specific antibody titre variation tendency in record yolk: starting largely to collect chicken when antibody titer has obvious ascendant trend Egg;It is same to monitor Yolk antibody titre when finding that titre is begun to decline booster immunization 1 time, when Yolk antibody titre has obviously Stop collecting egg when decline, by the In Shade storage of egg;
C) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, is placed in -20 ± 3 DEG C Under at least freeze 24-72h, 8-10 times of volume purified water dilution stirring 5-6h is added, extremely with hydrochloric acid solution tune pH in quick-thawing 5.0-5.1 is stood overnight at 20-23 DEG C;
D) by yolk dilution centrifugal filtration, obtained filtrate is concentrated by ultrafiltration, and is replaced with sodium chloride solution and liquid is concentrated by ultrafiltration Twice, displacement gained concentrate ammonium sulfate precipitation, is redissolved using sodium chloride solution later;
E) by the dialysis of sodium chloride lysate, centrifugal filtration to get Yolk immunoglobulin liquid.
With the prior art using kit carry out Yolk immunoglobulin extraction compared with, the present invention using it is a series of from The physical-chemical processes such as the heart, filtering, precipitating, dialysis carry out the extraction purification of Yolk immunoglobulin, not only easy to operate, Er Qieti Take at low cost, extraction process is easy to control, and extracted obtained Yolk immunoglobulin can be good at carrying out periodontitis Treatment, effect are obvious;
In addition, unlike the prior art, we prepare IgY using the laying hen after being immunized, it can be to avoid because of large-scale breeding Caused by the high problem of the laying hen death rate;Meanwhile the present invention city Jun He in terms of titre, purity and yield IgY obtained IgY no significant difference on field, therefore extraction process disclosed by the invention can carry out large-scale industrial production.
Specific scheme is the cultural method of step a) Porphyromonas gingivalis body are as follows:
1) aseptically, the unicellular strain of porphyromonas is drawn in Columbia Blood Agar plate with four zoning collimation methods On, it is placed in 37 DEG C of anaerobic culture box and cultivates 3-5d to generating black colonies;
2) black colonies are inoculated in Anaerobic culturel 2-4d in 3.7% N of brain heart infusion fluid nutrient medium, tooth is collected by centrifugation Gum Porphyromonas thallus.
Specifically, step a) Porphyromonas gingivalis body is with 1% formalin-inactivated, 4 DEG C overnight, sterile PBS buffer It washes 3 times, later with concentration for 1.0 × 1011The inactivation thallus 1ml of CFU/ml is helped completely with equivalent incomplete Freund's adjuvant, Freund Agent blow and beat respectively be mixed into two kinds in requisition for Water-In-Oil shape injection.
Scheme as a further preference, the method for Immune Laying Hens is as follows in step b):
Healthy laying hen is first immunized 4 times, every chicken per injection 1.0ml, and first immunisation is with Freund's complete adjuvant and inactivation The injection that the injection that thallus mixes, rear 3 booster immunization incomplete Freund's adjuvants and inactivation thallus mix, it is immune every time Interval time is 8-10d, Specific antibody titre variation tendency in monitoring record yolk: when antibody titer has obvious ascendant trend When start largely to collect egg;When discovery titre begins to decline Shi Zaiyong incomplete Freund's adjuvant and inactivates the injection of thallus mixing It is agent booster immunization 1 time, same to monitor Yolk antibody titre, stop collecting egg when Yolk antibody titre decreased significantly, it will The laying hen of collection marks and stores in the cool.
Preferably, in step d) centrifugal filtration processing method are as follows: yolk dilution is centrifuged at 4 DEG C, is taken on clear liquid To get filtrate, the filler in Filter column is made of gauze layer arranged up and down and medical absorbent cotton layer for Filter column filtering.Application People, can be well by centrifugal clear liquid using the filler that gauze layer and medical absorbent cotton layer are constituted through a large amount of analysis and research discovery The granular insoluble matter of the middle overwhelming majority and lipid material removal, thus greatly reduce the purifying difficulty in later period, while effectively Ground improves the purity of Yolk immunoglobulin.
Further, step d) used molecular cut off that filtrate is concentrated by ultrafiltration 9-10 times for the ultrafiltration membrane of 100KD before this, Then liquid is concentrated by ultrafiltration twice with 0.9% sodium chloride solution equivalent displacement, displacement gained concentrate is spare.It is to use because before Purified water dilution dissolution yolk, and postorder needs to dissolve ammonium sulfate precipitation using sodium chloride, therefore chlorination is first used before precipitation Liquid displacement will be concentrated by ultrafiltration in sodium solution, so the dissolution system of target protein can be replaced as sodium chloride solution by purified water, from And facilitate precipitating, dissolution process, to remove impurity therein, realize the purpose of protein of interest.
Further, the concentrate that step d is obtained is by following precipitating and dissolution process: according to the ratio of 1ml:0.243g Ammonium sulfate is added into displacement concentrate in example, and 1h is sufficiently stirred, is stored at room temperature 2h, is centrifuged at 4 DEG C, supernatant is abandoned, with 0.9% Sodium chloride solution is completely dissolved precipitating;Preferred embodiment is displacement concentration liquid precipitate and dissolution process step cycle weight in step d Again twice, being completely dissolved precipitating with sodium chloride solution in certain step is also the redissolution of sediment.
Specifically, the sodium chloride solution that step e) is by sodium chloride lysate with temperature is 2-8 DEG C, concentration is 0.9% is saturating Then at 2-8 DEG C overnight analysis is centrifuged at 4 DEG C, gained clear liquid with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, Gained Yolk immunoglobulin liquid, which is placed at -20 DEG C, to be saved.
Preferably, step c) is that yolk after mixing evenly is placed at -20 ± 3 DEG C at least to freeze 48h, at this Under part, the yield and extraction efficiency of target product can be effectively ensured.
Detailed description of the invention
Fig. 1 is the overnight layering result figure of different yolk liquid.
Specific embodiment
Disclosed technical solution in order to further illustrate the present invention, 1-10 is illustrated by the following examples, Partial parameters in middle embodiment 5,7-10 are not within the scope of the present invention, it can be understood as are comparative examples:
Embodiment 1: the acquisition of egg
1) aseptically, the unicellular strain of porphyromonas (waiting supplementing in source) is drawn in brother's rival with four zoning collimation methods On sub- blood agar plate, it is placed in 37 DEG C of anaerobic culture box and cultivates 4d to generating black colonies;
2) black colonies are inoculated in Anaerobic culturel 3d in 3.7% N of brain heart infusion fluid nutrient medium, gum is collected by centrifugation Porphyromonas thallus;
3) by 1% formalin-inactivated of porphyromonas gingivalis body, 4 DEG C overnight, and sterile PBS buffer is washed 3 times, later with dense Degree is 1.0 × 1011The inactivation thallus 1ml and equivalent incomplete Freund's adjuvant, Freund's complete adjuvant of CFU/ml blows and beats mixing respectively At two kinds in requisition for Water-In-Oil shape injection.
4) healthy laying hen is first immunized 4 times, every chicken per injection 1.0ml, first immunisation be with Freund's complete adjuvant with go out The injection that the injection that viable bacteria body mixes, rear 3 booster immunization incomplete Freund's adjuvants and inactivation thallus mix, exempts from every time Epidemic disease interval time is 8-10d, Specific antibody titre variation tendency in monitoring record yolk: when antibody titer has obvious rise to become Start largely to collect egg when gesture;When discovery titre begins to decline Shi Zaiyong incomplete Freund's adjuvant and inactivates the note of thallus mixing It penetrates agent booster immunization 1 time, it is same to monitor Yolk antibody titre, stop collecting egg when Yolk antibody titre decreased significantly, The laying hen of collection is marked and is stored in the cool.
Embodiment 2: the extraction of livitin
1) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, is placed at -20 DEG C For 24 hours, 9 times of volume purified waters dilution stirring 5h are added in quick-thawing for freezing, with hydrochloric acid solution tune pH to 5.0-5.1, in 20-23 It is stood overnight at DEG C;
2) yolk dilution is centrifuged at 4 DEG C, takes on clear liquid Filter column filtering to get filtrate, the filler in Filter column It is to be made of gauze layer arranged up and down and medical absorbent cotton layer;
3) use molecular cut off be the ultrafiltration membrane of 100KD by filtrate be concentrated by ultrafiltration 9 times, then with 0.9% sodium chloride Liquid is concentrated by ultrafiltration twice in solution even displacement, and ammonium sulfate is added into displacement gained concentrate according to the ratio of 1ml:0.243g, 1h is sufficiently stirred, is stored at room temperature 2h, is centrifuged at 4 DEG C, abandons supernatant, is completely dissolved precipitating with 0.9% sodium chloride solution, sets It changes concentration liquid precipitate and dissolution process step cycle is repeated twice;
4) the sodium chloride solution dialysis that be 6 DEG C with temperature by sodium chloride lysate, concentration is 0.9%, is then stayed overnight for 4 DEG C, It is centrifuged at 4 DEG C, gained clear liquid is with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, gained Yolk immunoglobulin Liquid is placed at -20 DEG C and saves.
Embodiment 3: the extraction of livitin
1) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, is placed at -20 DEG C 48h is freezed, 9 times of volume purified waters dilution stirring 5h are added in quick-thawing, with hydrochloric acid solution tune pH to 5.0-5.1, in 20-23 It is stood overnight at DEG C;
2) yolk dilution is centrifuged at 4 DEG C, takes on clear liquid Filter column filtering to get filtrate, the filler in Filter column It is to be made of gauze layer arranged up and down and medical absorbent cotton layer;
3) use molecular cut off be the ultrafiltration membrane of 100KD by filtrate be concentrated by ultrafiltration 9 times, then with 0.9% sodium chloride Liquid is concentrated by ultrafiltration twice in solution even displacement, and ammonium sulfate is added into displacement gained concentrate according to the ratio of 1ml:0.243g, 1h is sufficiently stirred, is stored at room temperature 2h, is centrifuged at 4 DEG C, abandons supernatant, is completely dissolved precipitating with 0.9% sodium chloride solution, sets It changes concentration liquid precipitate and dissolution process step cycle is repeated twice;
4) the sodium chloride solution dialysis that be 6 DEG C with temperature by sodium chloride lysate, concentration is 0.9%, is then stayed overnight for 4 DEG C, It is centrifuged at 4 DEG C, gained clear liquid is with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, gained Yolk immunoglobulin Liquid is placed at -20 DEG C and saves.
Embodiment 4: the extraction of livitin
1) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, is placed at -20 DEG C 72h is freezed, 9 times of volume purified waters dilution stirring 5h are added in quick-thawing, with hydrochloric acid solution tune pH to 5.0-5.1, in 20-23 It is stood overnight at DEG C;
2) yolk dilution is centrifuged at 4 DEG C, takes on clear liquid Filter column filtering to get filtrate, the filler in Filter column It is to be made of gauze layer arranged up and down and medical absorbent cotton layer;
3) use molecular cut off be the ultrafiltration membrane of 100KD by filtrate be concentrated by ultrafiltration 9 times, then with 0.9% sodium chloride Liquid is concentrated by ultrafiltration twice in solution even displacement, and ammonium sulfate is added into displacement gained concentrate according to the ratio of 1ml:0.243g, 1h is sufficiently stirred, is stored at room temperature 2h, is centrifuged at 4 DEG C, abandons supernatant, is completely dissolved precipitating with 0.9% sodium chloride solution, sets It changes concentration liquid precipitate and dissolution process step cycle is repeated twice;
4) the sodium chloride solution dialysis that be 6 DEG C with temperature by sodium chloride lysate, concentration is 0.9%, is then stayed overnight for 4 DEG C, It is centrifuged at 4 DEG C, gained clear liquid is with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, gained Yolk immunoglobulin Liquid is placed at -20 DEG C and saves.
Embodiment 5 (comparative example): the extraction purification of livitin
1) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, is directly added into 9 times Volume purified water dilution stirring 5h is stood overnight at 20-23 DEG C with hydrochloric acid solution tune pH to 5.0-5.1;
2) yolk dilution is centrifuged at 4 DEG C, takes on clear liquid Filter column filtering to get filtrate, the filler in Filter column It is to be made of gauze layer arranged up and down and medical absorbent cotton layer;
3) use molecular cut off be the ultrafiltration membrane of 100KD by filtrate be concentrated by ultrafiltration 9 times, then with 0.9% sodium chloride Liquid is concentrated by ultrafiltration twice in solution even displacement, and ammonium sulfate is added into displacement gained concentrate according to the ratio of 1ml:0.243g, 1h is sufficiently stirred, is stored at room temperature 2h, is centrifuged at 4 DEG C, abandons supernatant, is completely dissolved precipitating with 0.9% sodium chloride solution, sets It changes concentration liquid precipitate and dissolution process step cycle is repeated twice;
4) the sodium chloride solution dialysis that be 2 DEG C with temperature by sodium chloride lysate, concentration is 0.9%, is then stayed overnight for 2 DEG C, It is centrifuged at 4 DEG C, gained clear liquid is with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, gained Yolk immunoglobulin Liquid is placed at -20 DEG C and saves.
Embodiment 6: the extraction purification of livitin
1) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, is placed at -20 DEG C 48h is freezed, 8 times of volume purified waters dilution stirring 5h are added in quick-thawing, with hydrochloric acid solution tune pH to 5.0-5.1, in 20-23 It is stood overnight at DEG C;
2) yolk dilution is centrifuged at 4 DEG C, takes on clear liquid Filter column filtering to get filtrate, the filler in Filter column It is to be made of gauze layer arranged up and down and medical absorbent cotton layer;
3) use molecular cut off be the ultrafiltration membrane of 100KD by filtrate be concentrated by ultrafiltration 10 times, then with 0.9% sodium chloride Liquid is concentrated by ultrafiltration twice in solution even displacement, and ammonium sulfate is added into displacement gained concentrate according to the ratio of 1ml:0.243g, 1h is sufficiently stirred, is stored at room temperature 2h, is centrifuged at 4 DEG C, abandons supernatant, is completely dissolved precipitating with 0.9% sodium chloride solution, sets It changes concentration liquid precipitate and dissolution process step cycle is repeated twice;
4) the sodium chloride solution dialysis that be 6 DEG C with temperature by sodium chloride lysate, concentration is 0.9%, is then stayed overnight for 4 DEG C, It is centrifuged at 4 DEG C, gained clear liquid is with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, gained Yolk immunoglobulin Liquid is placed at -20 DEG C and saves.
Embodiment 7 (comparative example): the extraction purification of livitin
1) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, is placed at -20 DEG C 48h is freezed, 9 times of volume purified waters dilution stirring 5h are added in quick-thawing, with hydrochloric acid solution tune pH to 5.0-5.1, at 3-5 DEG C Under stand overnight;
2) yolk dilution is centrifuged at 4 DEG C, takes on clear liquid Filter column filtering to get filtrate, the filler in Filter column It is to be made of gauze layer arranged up and down and medical absorbent cotton layer;
3) use molecular cut off be the ultrafiltration membrane of 100KD by filtrate be concentrated by ultrafiltration 9 times, then with 0.9% sodium chloride Liquid is concentrated by ultrafiltration twice in solution even displacement, and ammonium sulfate is added into displacement gained concentrate according to the ratio of 1ml:0.243g, 1h is sufficiently stirred, is stored at room temperature 2h, is centrifuged at 4 DEG C, abandons supernatant, is completely dissolved precipitating with 0.9% sodium chloride solution, sets It changes concentration liquid precipitate and dissolution process step cycle is repeated twice;
4) the sodium chloride solution dialysis that be 6 DEG C with temperature by sodium chloride lysate, concentration is 0.9%, is then stayed overnight for 4 DEG C, It is centrifuged at 4 DEG C, gained clear liquid is with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, gained Yolk immunoglobulin Liquid is placed at -20 DEG C and saves.
Embodiment 8 (comparative example): the extraction purification of livitin
1) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, is placed at -20 DEG C 48h is freezed, 9 times of volume purified waters dilution stirring 5h are added in quick-thawing, with hydrochloric acid solution tune pH to 5.0-5.1, in 29-31 It is stood overnight at DEG C;
2) yolk dilution is centrifuged at 4 DEG C, takes on clear liquid Filter column filtering to get filtrate, the filler in Filter column It is to be made of gauze layer arranged up and down and medical absorbent cotton layer;
3) use molecular cut off be the ultrafiltration membrane of 100KD by filtrate be concentrated by ultrafiltration 9 times, then with 0.9% sodium chloride Liquid is concentrated by ultrafiltration twice in solution even displacement, and ammonium sulfate is added into displacement gained concentrate according to the ratio of 1ml:0.243g, 1h is sufficiently stirred, is stored at room temperature 2h, is centrifuged at 4 DEG C, abandons supernatant, is completely dissolved precipitating with 0.9% sodium chloride solution, sets It changes concentration liquid precipitate and dissolution process step cycle is repeated twice;
4) the sodium chloride solution dialysis that be 6 DEG C with temperature by sodium chloride lysate, concentration is 0.9%, is then stayed overnight for 4 DEG C, It is centrifuged at 4 DEG C, gained clear liquid is with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, gained Yolk immunoglobulin Liquid is placed at -20 DEG C and saves.
Embodiment 9 (comparative example): the extraction purification of livitin
1) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, is placed at -20 DEG C 48h is freezed, 9 times of volume purified waters dilution stirring 5h are added in quick-thawing, with hydrochloric acid solution tune pH to 5.0-5.1, in 20-23 It is stood overnight at DEG C;
2) yolk dilution is centrifuged at 4 DEG C, takes on clear liquid Filter column filtering to get filtrate, the filler in Filter column It is to be made of active carbon;
3) use molecular cut off be the ultrafiltration membrane of 100KD by filtrate be concentrated by ultrafiltration 9 times, then with 0.9% sodium chloride Liquid is concentrated by ultrafiltration twice in solution even displacement, and ammonium sulfate is added into displacement gained concentrate according to the ratio of 1ml:0.243g, 1h is sufficiently stirred, is stored at room temperature 2h, is centrifuged at 4 DEG C, abandons supernatant, is completely dissolved precipitating with 0.9% sodium chloride solution, sets It changes concentration liquid precipitate and dissolution process step cycle is repeated twice;
4) the sodium chloride solution dialysis that be 6 DEG C with temperature by sodium chloride lysate, concentration is 0.9%, is then stayed overnight for 4 DEG C, It is centrifuged at 4 DEG C, gained clear liquid is with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, gained Yolk immunoglobulin Liquid is placed at -20 DEG C and saves.
Embodiment 10 (comparative example): the extraction purification of livitin
1) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, is placed at -20 DEG C 48h is freezed, 9 times of volume purified waters dilution stirring 5h are added in quick-thawing, with hydrochloric acid solution tune pH to 5.0-5.1, in 20-23 It is stood overnight at DEG C;
2) yolk dilution is centrifuged at 4 DEG C, takes on clear liquid Filter column filtering to get filtrate, the filler in Filter column It is to be made of diatomite;
3) use molecular cut off be the ultrafiltration membrane of 100KD by filtrate be concentrated by ultrafiltration 9 times, then with 0.9% sodium chloride Liquid is concentrated by ultrafiltration twice in solution even displacement, and ammonium sulfate is added into displacement gained concentrate according to the ratio of 1ml:0.243g, 1h is sufficiently stirred, is stored at room temperature 2h, is centrifuged at 4 DEG C, abandons supernatant, is completely dissolved precipitating with 0.9% sodium chloride solution, sets It changes concentration liquid precipitate and dissolution process step cycle is repeated twice;
4) the sodium chloride solution dialysis that be 6 DEG C with temperature by sodium chloride lysate, concentration is 0.9%, is then stayed overnight for 4 DEG C, It is centrifuged at 4 DEG C, gained clear liquid is with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, gained Yolk immunoglobulin Liquid is placed at -20 DEG C and saves.
As a result it detects:
Protein content survey is carried out to the Yolk immunoglobulin liquid that embodiment 2-5,7-10 is prepared using Lorry method Fixed, as the result is shown: 1, embodiment 2-5 testing result shows to prepare by the yolk of 200g striping clothing in terms of using embodiment 2-5 Obtained IgY total amount is respectively 497mg, 635mg, 651mg, 359mg, it can be seen that, before comprehensively considering optimal yolk liquid Reason mode are as follows: be put into after being freezed 48 hours under -20 DEG C of environment and take out spare, so may insure the yield and extraction efficiency of IgY; 2, the result after yolk liquid is stood overnight after tune acid in embodiment 3,7,8 is as shown in Figure 1, it can be seen from the figure that after adjusting acid The dwell temperature of yolk liquid influences very big, self sinking when yolk liquid dwell temperature is 20-23 DEG C on the layered effect of yolk liquid Layered effect is dropped significantly better than 3-5 DEG C and 29-31 DEG C;Different filtering column packings is respectively adopted to target liquid in embodiment 3,9,10 It is filtered, the results show that the clarity of the filtrate obtained after different filler filterings has apparent difference, wherein with Absorbent cotton and gauze are that the filtered filtrate clarity of Filter column of filler is best in embodiment 3, living with powdery in embodiment 9 Property charcoal be filler the filtered filtrate clarity of Filter column take second place, and in embodiment 10 diatomite be filler Filter column Filtered filtrate clarity is worst, the supernatant obtained after yolk diluent centrifugation, by being filling with absorbent cotton and gauze After the Filter column filtering of object, most granular insoluble matters and lipid material are successfully removed, and greatly reduce the later period Difficulty is purified, so can effectively improve the purity of Yolk antibody.

Claims (10)

1. a kind of extraction process of Yolk immunoglobulin comprising following steps:
A) prepared by antigen: collecting the unicellular strain of porphyromonas, culture obtains porphyromonas gingivalis body, then inactivation, 3-5 DEG C Overnight, concentration is later 1.0 × 10 by PBS buffer solution washing11The inactivation thallus and isometric Freund's adjuvant of CFU/ml is blown and beaten It is mixed into Water-In-Oil shape injection;
B) laying hen is immune: the healthy laying hen of 3-5 monthly age isolated rearing is selected, through pigeon breast portion subdermal muscle injecting immune 4 times, and monitoring note Specific antibody titre variation tendency in record yolk: start largely to collect egg when antibody titer has obvious ascendant trend;When It was found that booster immunization 1 time when titre is begun to decline, same to monitor Yolk antibody titre, when Yolk antibody titre decreased significantly Stop collecting egg, by the In Shade storage of egg;
C) by egg cleaning, disinfection, broken shell removes egg white and membrane of yolk clothing, yolk is stirred evenly, be placed in -20 ± 3 DEG C down toward 24-72h is freezed less, and 8-10 times of volume purified water dilution stirring 5-6h is added, with hydrochloric acid solution tune pH to 5.0- in quick-thawing 5.1, it is stood overnight at 20-23 DEG C;
D) by yolk dilution centrifugal filtration, obtained filtrate is concentrated by ultrafiltration, and is replaced with sodium chloride solution and liquid is concentrated by ultrafiltration twice, Displacement gained concentrate ammonium sulfate precipitation, is redissolved using sodium chloride solution later;
E) sodium chloride solution of liquid after above-mentioned redissolution is dialysed, centrifugal filtration is to get Yolk immunoglobulin liquid.
2. the extraction process of Yolk immunoglobulin according to claim 1, it is characterised in that: porphyromonas in step a) The cultural method of unit cell thallus are as follows:
1) aseptically, the unicellular strain of porphyromonas is drawn on Columbia Blood Agar plate with four zoning collimation methods, is set 3-5d is cultivated in 37 DEG C of anaerobic culture box to generating black colonies;
2) black colonies are inoculated in Anaerobic culturel 2-4d in 3.7% N of brain heart infusion fluid nutrient medium, gum porphin is collected by centrifugation Quinoline unit cell thallus.
3. the extraction process of Yolk immunoglobulin according to claim 2, it is characterised in that: porphyromonas in step a) Unit cell thallus is with 1% formalin-inactivated, and 4 DEG C overnight, and sterile PBS buffer is washed 3 times, later with concentration for 1.0 × 1011CFU/ml Inactivation thallus 1ml and equivalent incomplete Freund's adjuvant, Freund's complete adjuvant blow and beat respectively be mixed into two kinds in requisition for oil Wrap watery injection.
4. the extraction process of Yolk immunoglobulin according to claim 3, it is characterised in that: Immune Laying Hens in step b) Method it is as follows:
Healthy laying hen is first immunized 4 times, every chicken per injection 1.0ml, and first immunisation is with Freund's complete adjuvant and inactivation thallus The injection that the injection of mixing, rear 3 booster immunization incomplete Freund's adjuvants and inactivation thallus mix, each immunization interval Time is 8-10d, Specific antibody titre variation tendency in monitoring record yolk: is opened when antibody titer has obvious ascendant trend Begin a large amount of collection eggs;Add when discovery titre begins to decline Shi Zaiyong incomplete Freund's adjuvant with the injection that thallus mixes is inactivated It is strong 1 time immune, it is same to monitor Yolk antibody titre, stop collecting egg when Yolk antibody titre decreased significantly, will collect Laying hen mark and store in the cool.
5. the extraction process of Yolk immunoglobulin according to claim 4, it is characterised in that: centrifugal filtration in step d) Processing method are as follows: yolk dilution is centrifuged at 4 DEG C, takes on clear liquid Filter column filtering to get filtrate, filling out in Filter column Material is made of gauze layer arranged up and down and medical absorbent cotton layer.
6. the extraction process of Yolk immunoglobulin according to claim 5, it is characterised in that: step d) is used cut before this It stays the ultrafiltration membrane that molecular weight is 100KD that filtrate is concentrated by ultrafiltration 9-10 times, is then replaced with 0.9% sodium chloride solution equivalent super Twice, displacement gained concentrate is spare for filter concentration liquid.
7. the extraction process of Yolk immunoglobulin according to claim 6, it is characterised in that: the concentration that step d is obtained Liquid is by following precipitating and dissolution process: ammonium sulfate is added into displacement concentrate according to the ratio of 1ml:0.243g, sufficiently stirs 1h is mixed, 2h is stored at room temperature, is centrifuged at 4 DEG C, supernatant is abandoned, is completely dissolved precipitating with 0.9% sodium chloride solution.
8. the extraction process of Yolk immunoglobulin according to claim 7, it is characterised in that: replace concentration in step d Liquid precipitate and dissolution process step cycle are repeated twice.
9. the extraction process of Yolk immunoglobulin according to claim 6 or 7, it is characterised in that: step e) is by chlorine Change the sodium chloride solution dialysis that sodium lysate with temperature is 2-8 DEG C, concentration is 0.9%, then at 2-8 DEG C overnight, at 4 DEG C from The heart, for gained clear liquid with 0.22 μm of membrane filtration to get Yolk immunoglobulin liquid, gained Yolk immunoglobulin liquid is placed in -20 It is saved at DEG C.
10. the extraction process of Yolk immunoglobulin according to claim 9, it is characterised in that: step c) is will to stir Yolk after uniformly, which is placed at -20 ± 3 DEG C, at least freezes 48h.
CN201610781996.3A 2016-08-30 2016-08-30 The extraction process of Yolk immunoglobulin Expired - Fee Related CN106380518B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610781996.3A CN106380518B (en) 2016-08-30 2016-08-30 The extraction process of Yolk immunoglobulin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610781996.3A CN106380518B (en) 2016-08-30 2016-08-30 The extraction process of Yolk immunoglobulin

Publications (2)

Publication Number Publication Date
CN106380518A CN106380518A (en) 2017-02-08
CN106380518B true CN106380518B (en) 2019-07-12

Family

ID=57938586

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610781996.3A Expired - Fee Related CN106380518B (en) 2016-08-30 2016-08-30 The extraction process of Yolk immunoglobulin

Country Status (1)

Country Link
CN (1) CN106380518B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109613252A (en) * 2018-10-22 2019-04-12 新疆医科大学第附属医院 Echinococcus granulosus high immunity yolk antibody and test strips and preparation method and application
CN110128541A (en) * 2019-04-16 2019-08-16 广东工业大学 A kind of preparation method and application of Yolk antibody that preventing and treating chronic periodontitis
CN110240648A (en) * 2019-06-17 2019-09-17 长春西诺生物科技有限公司 Cat infectiousness nose conjunctivitis and feline panleukopenia bigeminy freeze-dried yolk antibody and preparation and application
CN112300275A (en) * 2020-02-19 2021-02-02 南京蛋球球生物医学技术合伙企业(有限合伙) Yolk antibody for inhibiting new coronavirus SARS-CoV-2 and its preparation method and application
CN111718410B (en) * 2020-06-05 2022-10-11 江南大学 Method for preparing yolk immunoglobulin
CN117164702B (en) * 2023-09-13 2024-05-10 江苏润洁生物科技有限公司 Preparation method and application of yolk globulin for clinical HPV infection

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101125886A (en) * 2007-07-27 2008-02-20 浙江大学 Method for extracting yolk immunoglobulin
CN101402673A (en) * 2008-11-06 2009-04-08 中国石油大学(华东) Method for extracting immunoglobulin of yolk
CN101791405A (en) * 2010-03-25 2010-08-04 安徽医科大学 Method for preparing yolk immunoglobulin vaccine for resisting porphyromonas gingivalis
CN101948538A (en) * 2010-10-19 2011-01-19 郑州后羿制药有限公司 Method for refining chicken egg yolk antibodies against Escherichia coli
CN103007278A (en) * 2012-10-18 2013-04-03 上海美加净日化有限公司 Anti-porphyromonas gingivalis and fusobacterium nucleatum compound specific IgY antibody, preparation method and toothpaste thereof
CN104117062A (en) * 2013-04-24 2014-10-29 杭州雅盛生物科技有限公司 Preparation method of composite IgY against periodontal disease pathogenic bacteria
CN104558164A (en) * 2013-10-12 2015-04-29 天津嘉瑞生物科技有限公司 Extraction method for avian coccidiosis yolk antibody
CN104725502A (en) * 2015-02-04 2015-06-24 陕西溯源农业发展有限公司 Preparation method of anti-small ruminant animal specificity IgY
CN105820242A (en) * 2015-01-05 2016-08-03 郑州牧业工程高等专科学校 Optimal extraction technology of infectious bursal diseased egg yolk immunoglobulin

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101125886A (en) * 2007-07-27 2008-02-20 浙江大学 Method for extracting yolk immunoglobulin
CN101402673A (en) * 2008-11-06 2009-04-08 中国石油大学(华东) Method for extracting immunoglobulin of yolk
CN101791405A (en) * 2010-03-25 2010-08-04 安徽医科大学 Method for preparing yolk immunoglobulin vaccine for resisting porphyromonas gingivalis
CN101948538A (en) * 2010-10-19 2011-01-19 郑州后羿制药有限公司 Method for refining chicken egg yolk antibodies against Escherichia coli
CN103007278A (en) * 2012-10-18 2013-04-03 上海美加净日化有限公司 Anti-porphyromonas gingivalis and fusobacterium nucleatum compound specific IgY antibody, preparation method and toothpaste thereof
CN104117062A (en) * 2013-04-24 2014-10-29 杭州雅盛生物科技有限公司 Preparation method of composite IgY against periodontal disease pathogenic bacteria
CN104558164A (en) * 2013-10-12 2015-04-29 天津嘉瑞生物科技有限公司 Extraction method for avian coccidiosis yolk antibody
CN105820242A (en) * 2015-01-05 2016-08-03 郑州牧业工程高等专科学校 Optimal extraction technology of infectious bursal diseased egg yolk immunoglobulin
CN104725502A (en) * 2015-02-04 2015-06-24 陕西溯源农业发展有限公司 Preparation method of anti-small ruminant animal specificity IgY

Also Published As

Publication number Publication date
CN106380518A (en) 2017-02-08

Similar Documents

Publication Publication Date Title
CN106380518B (en) The extraction process of Yolk immunoglobulin
CN105198988B (en) Anti- Vibrio splindidus Yolk antibody and preparation method thereof
SU625623A3 (en) Method of obtaining vaccine against respiratory diseases of animals and birds caused by mycoplasms
CN104099301B (en) Coxsackie virus A16 type virus strain, application, vaccine and preparation method thereof
CN104530232A (en) Preparation method of refined egg yolk antibody for duck viral hepatitis
CN101113176A (en) Method for preparing infectious chicken Fabricius bursa refined yolk cryodesiccation antibody
CN109097298A (en) A kind of method of enrichment culture method preparation phage bdellovibro preparation
CN106754754A (en) A kind of WZ plants of the 4 type strain of aviadenovirus I group and its application
CN103436583A (en) Method for producing therapeutic monoclonal antibody of canine distemper virus, product thereof and hybridoma cell
CN104606675B (en) A kind of multi-joint special yolk antibody of fowl and the preparation method of transfer factor
CN111500482A (en) Sheep A-type clostridium perfringens strain, inactivated vaccine thereof and vaccine preparation method
CN105198989A (en) Shewanella-smarisflavi-resistant egg yolk antibody and preparation method thereof
CN105582533A (en) Combined inactivated vaccine for avian influenza virus and fowl adenovirus
CN105664150A (en) Newcastle disease virus, avian influenza virus and avian adenovirus triple inactivated vaccine
CH504532A (en) Attenuated strain of feline enteritis virus - from cell cultures
CN106397586B (en) specific yolk antibody for resisting dermatophytes and preparation method and application thereof
CN104548088A (en) Method for preparing bivalent vaccine of newcastle disease virus La Sota strain and infectious bronchitis virus N-S multi-epitope protein
CN105585632A (en) Meat duck parvovirus refined yolk antibody
CN104017060B (en) Extraction method for escherichia coli pilus antigen used for preparing yolk antibody, and method for preparing yolk antibody
CN104069489B (en) Newcastle disease and infectious bursa of Fabricius bivalent inactivated vaccine and preparation method thereof
Sutherland THE SYDNEY FUNNEL–WEB SPIDER (ATRAX ROBUSTUS) 2. FRACTIONATION OF THE FEMALE VENOM INTO FIVE DISTINCT COMPONENTS
CN104984337A (en) Newcastle disease and avian flu antigen-antibody complex inactivated vaccine and preparation method
CN1268643C (en) Antibody against SARS-CoV IgY and its preparing method
CN106674346A (en) Specific yolk antibody for preventing mycoplasmosis of cattle, and preparation method and application thereof
CN104127869B (en) Multivalence B group meningitis cocci protein vaccine and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
CB03 Change of inventor or designer information

Inventor after: Li Zengli

Inventor after: Cheng Ting

Inventor after: Chen Zilei

Inventor after: Shen Yi

Inventor after: Xu Yan

Inventor after: Zhou Lechun

Inventor after: Wang Ronghai

Inventor after: Xu Pei

Inventor after: Song Lihua

Inventor after: Dong Shijian

Inventor after: Ni Xiaoyan

Inventor after: Chu Chengfeng

Inventor before: Song Lihua

Inventor before: Shen Yi

Inventor before: Chen Zilei

Inventor before: Wang Ronghai

Inventor before: Li Zengli

Inventor before: Zhou Lechun

Inventor before: Cheng Ting

Inventor before: Xu Pei

Inventor before: Ni Xiaoyan

Inventor before: Chu Chengfeng

Inventor before: Dong Shijian

COR Change of bibliographic data
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20190712

CF01 Termination of patent right due to non-payment of annual fee