专利摘要:
A pertussis toxoid is produced by removing endotoxin from a culture supernatant of a Bordetella pertussis phase I strain or a concentrate thereof and flocculating pertussis exotoxin in the resultant fluid by permitting formaldehyde to act upon the fluid in the substantial absence of basic amino acid. The thus-obtained pertussis toxoid is low in toxicity and has a high immunizing potency.
公开号:SU1297712A3
申请号:SU813235495
申请日:1981-01-23
公开日:1987-03-15
发明作者:Сиукуда Юкио;Ватанабе Хидео;Мацуяма Сигео
申请人:Такеда Кемикал Индастриз,Лтд. (Фирма);
IPC主号:
专利说明:

This invention relates to biotechtology and is concerned with the preparation of biologically active substances.
The aim of the invention is to reduce the toxicity of the target product by modifying the method of isolation and detoxification.
The method is illustrated by a simple example.
Example 1, and Tohamafaz111 1 Bordetella pertussis, is inoculated on Burde-Gangu medium prepared from potatoes, peptone, sodium chloride, agar and bovine blood, and incubated at 35 ° C for two days. Then translucent round colonies are selected, the activity of K-agglutinating serum is determined, and the culture is selected as a seed. The production medium is obtained by autoclaving a Cohe-Wheeler liquid medium containing: soluble starch 225 g, sodium chloride 375 g, disubstituted potassium phosphate 75 g, magnesium chloride hexahydrate 750 ml (8% w / v,% liquid), calcium chloride 75 ml ( 2 w / v,% liquid), copper sulfate pentahydrate 112.5 ml (0.1 w / v% liquid), sodium glutamate 30 g, nicotinamide 4.5 g, casamic acid 1800 g, cystine hydrochloride 4.5 g, Tris buffer 12.5 l. The components of the medium are diluted with distilled water to 150 liters, adjusted to pH 7.0-7.2 and sterilized, then glutathione (recovered 50 ml (| w / v% liquid) and Fe5047H 50 ml (l Fluid at 121 ° C for 60 minutes, followed by rapid cooling to approximately 40 ° C. The medium is stored at 37 ° C,
The inoculum culture is introduced into the nutrient medium to a final concentration of 200-300 ppm, cells / ml, mixed thoroughly, seeded at 0.2 l in the Rowks’s bottle and placed in a thermostat at 37 ° C. The maximum number of cells is obtained on the 5th day. liquids from bottles are combined, centrifuged, and 20.2 w / v, ammonium sulfate is added to the supernatant. After thorough mixing, the mixture is kept at 4 ° C. After 7 days, the supernatant is drained and the precipitate is collected and centrifuged at 8000 rpm for 10 minutes.
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the sedimentary liquid is discarded, 1/10 volume of the mixture W of sodium chloride solution and (), 05 M phosphate buffer (pH 8.0) is added to the precipitate and the mixture is thoroughly mixed. The mixture is again maintained at 40 ° C for 7 days, after which it is again centrifuged and the supernatant is collected (extract 1),
Extract 1 contains fibrin, a leukocytosis promoter factor (PSL), gmintaminimmunizing factor (HIF) and endotoxin, there are no microbial cells. Extract 1 is re-concentrated, an equal volume of a saturated ammonium sulphate solution (pH is adjusted with ammonia) is added to it and the mixture is kept at 4 ° C for 7 days. The ammonium sulfate fraction is centrifuged at 10,000 rpm for 20 minutes, the precipitate is separated and 1/300 of the volume of the liquid mixture Ш of sodium chloride solution and 0.05 M phosphate buffer (pH 8, o) is added. After thoroughly mixing, the mixture is placed in A dialysis tube with a semipermeable membrane to remove ammonium sulfate and dialysis are carried out against a 1M solution of sodium chloride (pH 8.0). The dialyzed concentrate is then centrifuged at a sucrose density gradient.
The pre-sterilized 1700 ml centrifuge rotor and the sealed unit are rotated at a low speed; 1300 ml 5-30 w / v% sugar-free solutions are fed using a gradient pump. Then 100 ml of a dialyzed concentrate are fed and the coating medium is introduced (0.5 M sodium chloride solution, pH 8.0). The rotor is rotated at RMQ 89400 and for 18.5 hours.
After centrifugation, 34 w / v% sugar cane solution is fed at low speed and the liquid from the rotor is collected in fractions of 50-100 ml. The collection of fractions is started from the low density side of sucrose, and fractions with high hemagglutinating activity (at least 20 units / ml, preferably at least 500 units / ml) and depleted in endotoxin are obtained. The presence of endotoxin is determined in a test in rabbits. Each sample of the fraction was kept at 100 ° C for 3 minutes and diluted to
312
20 hematsinigrupsch units / ml of saline. The skipped sample is administered intravenously to rabbits at a dose of 1 ml / kg live weight. Fractions that do not cause heat in rabbits for 3 hours are collected and pooled as the desired product (exotoxin).
The collected fractions containing the exotoxin were diluted with M / 250 phosphate buffer pH 7.0 to a protein content of 50 mg / ml. Gelatin, tween-80 and thimerosol are added to a final concentration of 0.02% w / v, 0.05% v / v and 0.01% w / v, respectively, to the mixture without which - Formalin is added to the basic amino acid to a concentration of 0.2% v / v in a thermostat at 39 ° C and, after thorough mixing, the mixture is further incubated in the same thermostat. After 2 days, formalin is added to a concentration of 0.3 v / v% and, after thorough mixing, the mixture is further incubated at the same temperature.
After 2 days, the addition of formalin was repeated to a concentration of 0.4 v / v% and, after stirring, the incubation was continued for 5 days.
You can handle a mixture of 0.1 v / v% formalin by incubating at 42 ° C for 14 days or 0.6 v / v formalin by incubating for 14 days.
The resulting toxoid flocculent suspension is dialyzed with 0.01 v / v / v of formalin-saline, identical to the coating medium. Dialysis is carried out in a membrane dialysis tube at a 12.5-fold ratio of the volumes of the internal and dialysis solution for 2 days, while the dialysis solution is constantly stirred. After two days, this solution was replaced with a fresh solution and the dialysis was repeated. The dialyzed toxoid toxoid flocculent suspension is subjected to various tests applied to the cocklet vaccine raw material.
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Next, the suspension of toxoid flakes is subjected to ultrasonic treatment (frequency 20-50 kHz, 5 min) and filtered through a coarse filter.
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400 mesh, resulting in a liquid pertussis toxoid.
The experience of treating the liquid containing exotoxin with formalin with the addition of 0.05 M L-lysine was monitored and then the treatment was carried out as described above.
Experimental and control liquids separately treated by the method of Levin. Each liquid was diluted with M / 250 phosphate buffer pH 7.0 to a protein content of 20 µg / ml or less, and aluminum chloride was added to a concentration of 0.18 w / v. The mixture is thoroughly mixed, the pH is adjusted to 7.0 with hydrochloric acid or sodium hydroxide and the precipitated precipitate is separated.
vaccine, 1
The experiments showed the following: BLP should not exceed the equivalent of 0.5 LUE (leukocytosis of the promoter unit) / ml; The HIF should not exceed the equivalent of 0.8 GSE (histamine-sensitizing units) / ml; Efficacy of mummy is acceptable when it is 8 MU (infection three weeks after immunization) per ml.
The average efficacy of 14 consecutive batches is 13.5 IU / ml. In the control (with the addition of L-lysine), a series of 23 batches shows complete acceptability of the vaccine in only 23%,
Example 2. Liquid pertussis toxoid obtained in Example 1, diphtheria liquid toxoid and tetanus toxoid are precipitated in accordance with Example 1 and purified polyvaccine against pertussis — diphtheria – tetanum is obtained.
The composition of the vaccine: pertussis toxoid - protein content of about 15 mg / ml, diphtheria toxoid - approximately 30s 1 / ml; tetanus toxoid - approximately 5 °, / ml; aluminum — about 0.2 mg / ml; thimerosol 0.01 wt./about.%.
Polyvaccine has the following basic properties: the concentration of hydrogen ions is 7.0; Pyrolysis for rabbits (50-fold dilution and intravenous administration at a rate of 1 ml / kg live weight) is negative; weight loss does not exceed the permissible norm; leukocytosis promotion activity in mice no more than the equivalent of 0.5 LU / ml; histamine sensitization activity no more than equivalent 0.8 efficiency
512
pertussis toxoid is equivalent to 8 IU / ml, diphtheria toxoid is 45 IU / mp, and tetanus toxoid is 30 IU / ml.
Vaccination is carried out as follows.
Children 3-48 months of age, subcutaneously injected 0.5 ml of each vaccine three times with an interval of 2-8 weeks. After 12-18 months, after the last injection, another 0.5 ml of the vaccine was injected subcutaneously.
权利要求:
Claims (1)
[1]
Invention Formula
The method of obtaining toxoid Vogo- detella pertussis by cultivating bacteria in the first phase in the diet. Editor L. Veselovska Order 799/64
Compiled by G. Smirnova Tehred M. Khodanych
Corrector L
Circulation 596 Subscription
VNISH1I USSR State Committee
for inventions and discoveries 113035, Moscow, Zh-35, Raushsk nab., 4/5
Production and printing company, Uzhgorod, Projecto st., 4
26
a medium with subsequent separation of biomass, release of the toxin from the culture liquid and its detoxification, characterized in that, in order to reduce the toxicity of the target product, a mixture of toxins is precipitated from the culture liquid after separation of the mycelium, the precipitate is diluted with a buffer solution with sodium chloride, the resulting concentrate, if necessary, is additionally concentrated by treatment with ammonium sulfate and dialysis, exotoxin is isolated, treated with a formaldehyde solution in a ratio of 1: 0.1-0.6 v / v / v and the obtained target product is subjected to ultrasonic treatment at a frequency of 10-50 kHz.
Proofreader L. Pat Ai
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同族专利:
公开号 | 公开日
NO159667B|1988-10-17|
NO810014L|1982-03-15|
DK155915B|1989-06-05|
ES8202058A1|1982-02-01|
EP0047802B1|1984-10-10|
JPS5750925A|1982-03-25|
EP0047802A2|1982-03-24|
DE3069433D1|1984-11-15|
DK155915C|1989-10-23|
US4455297A|1984-06-19|
KR830004851A|1983-07-20|
DK9281A|1982-03-13|
KR840001512B1|1984-09-29|
GB2083358A|1982-03-24|
HU185404B|1985-02-28|
CA1152001A|1983-08-16|
JPS64928B2|1989-01-10|
ES499112A0|1982-02-01|
NO159667C|1989-02-01|
EP0047802A3|1982-12-29|
引用文献:
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法律状态:
优先权:
申请号 | 申请日 | 专利标题
JP55127825A|JPS64928B2|1980-09-12|1980-09-12|
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