NZ188211A - Isolation of polyribosyl ribitol phosphate(prp)from haemophilus influenzae type b;vaccine comprising prp and bordetellapertussis antigens - Google Patents

Isolation of polyribosyl ribitol phosphate(prp)from haemophilus influenzae type b;vaccine comprising prp and bordetellapertussis antigens

Info

Publication number
NZ188211A
NZ188211A NZ188211A NZ18821178A NZ188211A NZ 188211 A NZ188211 A NZ 188211A NZ 188211 A NZ188211 A NZ 188211A NZ 18821178 A NZ18821178 A NZ 18821178A NZ 188211 A NZ188211 A NZ 188211A
Authority
NZ
New Zealand
Prior art keywords
prp
haemophilus influenzae
influenzae type
strain
vaccine
Prior art date
Application number
NZ188211A
Inventor
J S-C Kuo
Original Assignee
American Cyanamid Co
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
Priority claimed from US05/846,466 external-priority patent/US4196192A/en
Priority claimed from US05/846,488 external-priority patent/US4220717A/en
Application filed by American Cyanamid Co filed Critical American Cyanamid Co
Publication of NZ188211A publication Critical patent/NZ188211A/en

Links

Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/70Carbohydrates; Sugars; Derivatives thereof
    • A61K31/715Polysaccharides, i.e. having more than five saccharide radicals attached to each other by glycosidic linkages; Derivatives thereof, e.g. ethers, esters
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K39/00Medicinal preparations containing antigens or antibodies
    • A61K39/02Bacterial antigens
    • A61K39/099Bordetella
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K39/00Medicinal preparations containing antigens or antibodies
    • A61K39/02Bacterial antigens
    • A61K39/102Pasteurellales, e.g. Actinobacillus, Pasteurella; Haemophilus
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K39/00Medicinal preparations containing antigens or antibodies
    • A61K2039/70Multivalent vaccine

Landscapes

  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Epidemiology (AREA)
  • Public Health (AREA)
  • Medicinal Chemistry (AREA)
  • Veterinary Medicine (AREA)
  • General Health & Medical Sciences (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Chemical & Material Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • Mycology (AREA)
  • Immunology (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Description

<div id="description" class="application article clearfix"> <p lang="en" class="printTableText">1 882 1 <br><br> Priority Datajs): . <br><br> Complete Specification Filed: <br><br> C-OTHII ; CiaflM 0*\ Afc.lvV5l\T3S: <br><br> Class: SEp.igffl <br><br> PubHcBiJon Data: <br><br> P.O. jc:&lt;Kc: . . ■ 1 ?^?-v <br><br> P. &amp; s. x-M <br><br> NEW ZEALAND PATENTS ACT, 1953 <br><br> vffi'f C. r* <br><br> No.: <br><br> Date: , - <br><br> COMPLETE SPECIFICATION <br><br> r&amp;r* fthlS <br><br> "HAEMOPHILUS INFLUENZAE^VACCINE" <br><br> XI / We, AMERICAN CYANAMID COMPANY, a corporation organized and existing under the laws o£ the State of Maine, United States of America, and having its executive offices at Wayne, New Jersey, United States of America, <br><br> hereby declare the invention for whichjfe/ we pray that a patent may be granted to XJg^us, and the method by which it is to be performed, to be particularly described in and by the following statement: - <br><br> - 1 - (followed by page la) <br><br> 188211 <br><br> This invention is in the field of vaccines for immunization against Haemophilus influenzae type b infections, such as meningitis. More specifically, this invention relates to: (1) a method for the isolation of antigenic polysaccharide 5 polyribosyl ribitol phosphate (PRP) from Haemophilus influenzae type b cultures; and, (2) a process for the preparation of a combined vaccine containing PRP and B. pertussis antigens. The PRP of this invention should also be effective when, used in conjunction with other non-pathogenic strains of bacteria, 10 such as E. coli, B. subtilis, S. aureus, B. punilus and L. <br><br> plantarum, to trigger an antibody response in warm-blooded animals. <br><br> The purified polyribosyl ribitol phosphate (PRP) from Haemophilus influenzae type b is being investigated as a pro-15 tective immunogen. However, an active antigenic response in young animals and infants has not been achieved. The prior art method for the purification employed ethanol and Cetavlon (hexadecyltrimethyl ammonium bromide). The contaminants, endotoxins, and pyrogenic substances were removed by the use 20 of cold phenol or chloroform and t-butanol which may result in the loss of the antigenic nature of this polysaccharide. <br><br> A new process for the isolation and purification of immunologically active PRP from Haemophilus influenzae type b has been established. <br><br> 25 The process to be described has distinct advantages over the prior art procedures in that all contaminants (nucleic acids, proteins and endotoxins) are removed to the minimum level by a treatment with hydroxylapatite. The PRP prepared by the process described here gives a higher molecular 30 weight polysaccharide than those reported previously. <br><br> la- <br><br> 188211 <br><br> 10 <br><br> More importantly, the PRP prepared by this new procedure is highly immunogenic in warm-blooded animals as opposed <br><br> % <br><br> to the PRP produced by prior art procedures. <br><br> A process for removal of contaminants (proteins, nucleic acids and endotoxins) in the polysaccharide PRP is performed by treating the partial purified polysaccharide with a phosphate containing adsorbent which does not absorb the polysaccharide under designated conditions. <br><br> The second objective of this invention is to provide a process for the preparation of a combined PRP and pertussis vaccine which is highly immunogenic in young animals. <br><br> DISCLOSURE <br><br> (I) Isolation and purification of polyribosyl ribitol phosphate, the capsular polysaccharide of Haemophilus -*-5 influenzae type b. <br><br> Organisms, Growth Medium and Culture <br><br> Two strains of Haemophilus influenzae type b are used. The Rab strain is obtained from Grace Leidy, Babies <br><br> Hospital, Columbia University, New York City, New York. The CK strain was isolated from a patient at Waterbury Hospital Waterbury, Conn. The organisms are passed through mice several times to insure their virulence. The organisms are isolated at autopsy from the brain tissue of mice, subcultured on either 3.7% (w/v) Brain Heart Infusion (BHI) (Difco Lab. , Detroit Mich.) medium or on 5% (w/v) BHI agar supplemented with 0.01% (w/v) nicotinamide adenine dinucleotide (NAD) (P-L Biochemicals, <br><br> Milwaukee, Wis.) and 1% (v/v) defibrinated horse blood (Animal Blood Center, Syracuse, N. Y.) and then distributed ^ in one ml portions in ampules, lyophilized and stored at -70°C. <br><br> 20 <br><br> 25 <br><br> - 2 <br><br> 188211 <br><br> 10 <br><br> Basal medium used for the growth of the organisms is 3.7% (w/v) (BHI). The basalrttedium is supplemented with 10 mg of NAD and 20 mg of hemin (Eastman Kodak, Rochester, N. Y.) per liter. One percent (v/v) defibrinated horse blood is added per 50 ml of seed culture. The supplements are freshly prepared and filtered through a 0.45i/\Nalgene filter unit Nalge Sybron Corp., Rochester, N. Y.) before use. For growth of the organism in a 14 liter fermentor, the medium is further supplemented with 0.5% by weight glucose. ' <br><br> To prepare a flask of seed organisms, one ml of frozen stock culture is thawed and transferred to 50 ml of the enriched BHI medium supplemented with defibrinated horse blood and NAD. The culture is grown for 8 hours at 37°C on a gyrotory shaker at 150 rpm. The organisms are added as a 1% by -.-.-sight inoculum to 500 ml portions of the enriched BHI broth in 2 liter flasks which are then incubated at 37°C with moderate shaking on a gyrotory shaker for 8 hours (for isolation of PRP) or 14 hours (as seed cultures). <br><br> The fermentation of each batch in a 14 liter fermentor is initiated by aseptically transferring 700 ml of the seed culture to 7 liters of the enriched BHI broth supplemented with hemin instead of defibrinated horse blood. The culture is continuously maintained at 37°+l°C, The tank is stirred at a rate of 150 rpm and an air flow of 0.25 liter of air per liter of mash per minute is maintained. During the growth 0.001% (w/v) of a silicone antifoam (FD-82, Hodag Chemical <br><br> Corp.) is added as needed. Cultures are grown to the limit <br><br> 9 <br><br> 30 logarithmic of growth (8 to 10 x 10 viable cells/ml), usu- <br><br> 15 <br><br> 20 <br><br> 25 <br><br> - 3 - <br><br> 188211 <br><br> ally about 8 hours and then growth is terminated by adding 0.4% (w/v) formaldehyde and standing overnight at 4 C. <br><br> Isolation of Polyribosyl Ribitol Phosphate (PRP) <br><br> Culture broth prepared as described above is centri-fuged at 27,000 x g for 30 minutes at 4°C. The cell free supernatant is collected and treated as follows: <br><br> Step 1, Ethanol Precipitation <br><br> To the culture supernatant is added sodium acetate <br><br> (final concentration 4% (w/v)). The solution is adjusted to pH 6.0-6.2 and 44 liters of formula 3A denatured alcohol are added slowly with vigorous stirring at 4°C. The mixture is adjusted to pH 6.8 with glacial acetic acid and then allowed to stand for 12 hours at 3°C. The resulting precipitate is collected by decantation and then cen-trifugation to afford crude PRP. <br><br> Step 2, Cetavlon(hexadecyItrimethyl ammonium bromide)Treatment <br><br> The precipitate from Step 1 is dissolved in pyro-gen-free distilled water and centrifuged to remove the residue. The clear brown solution is then slowly added to 100 ml of a 10% (w/v) aqueous solution of Cetavlon with mixing (final conc. 0.5% (w/v)). The mixture is stirred for one hour and then centrifuged. The precipitate of nucleic acids and PRP-Cetavlon complex is mixed with 2 liters of 0.3M sodium chloride. The cloudy solution is centrifuged to eliminate insoluble materials such as nucleic acid-Cetavlon salt. <br><br> The supernatant'is diluted with an equal volume of water causing the PRP-Cetavlon salt to precipitate. The mixture is stirred for one hour, the precipitate is collected by centrifugation and is then dissolved in 2 liters of 0.3M sodium chloride. , . <br><br> I <br><br> &amp; <br><br> 188211 <br><br> Step 3, Ethanol Precipitation <br><br> Cetavlon and the contaminants of nucleic acids and proteins are further removed by ethanol precipitation (at least 2 times). The PRP is precipitated as described in Step 1 while Cetavlon is dissolved in the alcoholic solution. The PRP is recovered by centrifugation, dissolved in 2 liters of pyrogen-free distilled water and then reprecipitated as described above. The final PRP precipitate is solubilized in 20mM sodium phosphate, pH 6.8. <br><br> Step 4, Hydroxylapatite Treatment <br><br> Contaminants (e.g. nucleic acids, proteins and endotoxins) in the partial purified PRP preparations are selectively removed by adsorption on a calcium phosphate containing adsorbent such as hydroxylapatite [3.Ca^(PO^)2.Ca(OH)- <br><br> This invention is based on the discovery that the polysaccharide PRP is not adsorbed by the calcium phosphate adsorbent containing phosphate buffer (20mM) having a pH of substantially 6.7-6.9; or a phosphate buffer (50 mM) having a pH of substantially 5.8; however, the contaminants (such as nucleic acids, proteins and endotoxins) are adsorbed under these conditions. The process of the present invention may be carried out in batch-wise or column operation. In batch process, the hydroxylapatite is added to the partially purified PRP preparation (in 20mM phosphate; pH 6.9). The mixture is mixed well at a temperature of substantially 1-4°C. and centrifuged to remove non-desired solids (adsorbent and the contaminants adsorbed by the adsorbent). The supernatant fluid is subjected to the foregoing procedure at least 2 more <br><br> 188211 <br><br> times. The resulting solution is filtered through millipore filters, dialyzed against pyrogen-free distilled water, and lyophilized. <br><br> In column operation, the partially purified PRP in 20mM phosphate buffer (pH of at least 5.8) is applied to a column containing the adsorbent hydroxylapatite which had been equilibrated with 20mM phosphate buffer, pH 5.8 and eluted with a stepwise gradient of sodium phosphate buffer (pH 5.3) from 20mM to lOOmM. Fractions are collected and assayed for pentose (for polyribosyl ribitol phosphate). Those fractions which are positive for pentose are dialyzed against pyrogen--free distilled water and lyophilized. <br><br> (II). A process for preparing a combination vaccine consisting of PRP from H. influenzae type b and B. pertussis antigens. <br><br> To prepare a PRP vaccine, lyophilized PRP (prepared as aforementioned) is dissolved at a concentration of 20 ng/ml in phosphate buffered saline (PBS) (0.113 g potassium diphosphate, 0.83 g disodium phosphate, and 8.5 g sodium chloride per liter, pH 7.0, containing 0.01% (w/v) thimerosal). The vaccine is sterile filtered through 0. 45y millipore filter units, dispensed into glass vials, and stored at 4°C. <br><br> A concentrated solution of the PRP is prepared by weighing predetermined amounts of the polysaccharide and dissolving it in phosphate buffered saline (0.113 g potassium diphosphate,, 0.83 g disodium phosphate, and 8.5 g sodium chloride per liter, pH 7.0, containing 0.01% (w/v) thimerosal). This concentrated solution of PRP is then mixed with an appropriate volume of fresh B. pertussis (strain 138) cell suspensions toorepare the <br><br> , - 1 APR1980 <br><br> 188211 <br><br> stock solution. The characteristics of B. pertussis (strain 138) are described in Bergey's Manual of Determinative Bacteriology, 8, Buchanan and Gibbons Editors, Wms and Wilkins, Maryland, U.S.A.} 1974,on page 283. This strain is available from the American Type Culture Collection, Maryland, U.S.A., deposit No. 103 80. The combined vaccine in this stock solution contains 200 pg of PRP and approximately 70 opacity units (op) of cells per ml. The stock solution is kept at 4°C for 90 days to allow for detoxification of pertussis antigens before the final product (vaccine) is prepared (which contains 10 yg of PRP and 3.5 op units of pertussis cells/0.5 ml dose). <br><br> DETAILED DISCLOSURE Example 1 <br><br> Hydroxylapatite (e.g. Bio. gel HTP, Bio-Rad Laboratories, Richmond, Calif.), 2.5 g is added to 250 ml partially purified PRP preparations (after Cetavlon and ethanol treatments) (containing approximately 1.0 mg PRP/ml) in 20mM sodium phosphate buffer, pH 6.9 and mixed at ice-cold water bath (1-4°C) for one hour. The mixture is centrifuged in the Sorvall RC2-B for 30 minutes at 16,000 x g.. The supernatant fluid is then passed through 0.65 y millipore filter and subjected to the foregoing procedure (each time treated with 2.5 g hydroxylapatite) 2 more times. The resulting solution is filtered through 0.65 y and 0.45 y millipore filters, dialyzed against pyrogen-free distilled water and lyophilized. The lyophilized product exhibits strong immunogenic activity (see below combined vaccine and animal experiment) and contains very low contaminants (such as nucleic acids, proteins and endotoxins) (see Table I below). Approximately 170 mg of the lyophilized PRP is obtained. The recovery of PRP by this process is approximately 70% of the starting polysaccharide. The PRP should be stored under suitable conditions, such as at 4°C in a desiccator over phosphorus pentoxide and silica gel. <br><br> - 7 - <br><br> 1 882 1 1 <br><br> Example 2 <br><br> A partially purified PRP (300 mg PRP) is dissolved in 100 ml of 20mM sodium phosphate buffer, pH 5.8 (i.e. 3 mg PRP/ml). This solution is applied to a column at ambient temperature (5.0 x 45 cm) of hydroxylapatite (approximately 250 ml bed volume which has been equilibrated with 20mM sodium phosphate buffer, pH 5.8 and eluted with a stepwise gradient of 20mM, 50mM, lOOmM sodium phosphate buffer, pH 5.8. The individual fractions (200 ml) eluted with 20mM and 50mM sodium phosphate buffer (pH 5.8), positive for pentose (pejitose determination by the orcinal method) are collected, dialyzed against pyrogen-free distilled water and lyophilized. Approximately 206 mg of the lyophilized product, PRP, is obtained. <br><br> The purity of the polysaccharide, PRP is assayed by estimating to what extent they are contaiminated with nucleic acids, proteins and endotoxins. Protein concentration is determined by the method of Lowry, et al^. in J. Biol. Chem. 193:265 (1951) with boving serum albumin as standard. Nucleic acid is measured gy the absorption of the PRP solution at 260nm. The absorbance of 50ug of nucleic acid in one ml of water in a cell of 1-cm light path is assumed to be equal to 1.0. Molecular size is estimated by means of Sepharose 4B or 2B gel filtration on columns 1.5 x 90 cm (Pharmacia-Fine Chemicals, Piscataway, N. J.). Partition coefficient (Kd) values are calculated from the elution pattern developed by the orcinal reaction (Herbert, et al., Methods in Microbiology, Vol. 5B, 285-291. <br><br> Table I <br><br> Physical-Chemical Characteristics of PRP Prefered <br><br> Assay <br><br> Endotoxin <br><br> Procedure <br><br> Mol. Size (Kd) <br><br> Pentose (%) <br><br> Nucleic Acid (%) <br><br> Protein (%) <br><br> Rabbit Pyrogen Testc <br><br> Limulus Lysate Test^ <br><br> Example 1 <br><br> oa <br><br> 36.0 <br><br> 0.8 <br><br> 0.7 <br><br> 10.0 <br><br> 1/400 <br><br> Example 2 <br><br> 0.44k <br><br> 33.8 <br><br> 0.3 <br><br> 0.7 <br><br> 10.0 <br><br> 1/1000 <br><br> a) Using both Sepharose 2B and 4B, molecular weight&gt; 2 x 10 <br><br> b) Using Sepharose 4B <br><br> c) vg PRP/kg rabbit body weight not yielding fever d) Reciprocal dilution of PRP (100 Ug PRP/ml) when compared to Bureau of Biologies El (endotoxin standard) <br><br> Example 1 utilises PRP derived from Haemophilus influenzae type b CK strain, available from the American Type Culture Collection, Maryland, U.S.A., deposit No. 31441. Example 2 utilises PRP derived from Haemophilus influenzae type b Rab strain available from Babies Hospital, Columbia University, New York, U.S.A. <br><br> 1 882 1 1 <br><br> Example 3 <br><br> A combination vaccine containing PRP from H. <br><br> influenzae type b and B. pertussis antigens is prepared as follows: 140 mg PRP (as prepared in Example 2) is dissolved in 350 ml sterile phosphate buffered saline (PBS) (0.113 g potassium diphosphate, 0.83 g disodium phosphate, and 8.5 g sodium chloride per liter, pH 7.0, containing 0.01% thimerosal), and filter through 0.45H millipore filter. This concentrated PRP solution (400-VJg/ml) is used to prepare a combination vaccine which consists of PRP and B. pertussis antigens. <br><br> To 150 ml of the concentrated PRP solution (400 £g/-ml) add 150 ml of fresh B. pertussis (strain 138) cell suspension in PBS, pH 7.0 (containing 149 opacity; op, unit cells/ml) to prepare the stock solution of the combined vaccine. This stock solution (300 ml) is kept at 4°C until the endotoxin level of the pertussis is decreased (at least 90 days). The sterility of the stock solution is tested with thioglycollate media (at <br><br> 32-33°C). The pH of the stock solution after 90 days incubation <br><br> + <br><br> is checked and adjusted to pH 7.0 -1. The final product (vaccine) used for animal experiments is prepared by diluting the stock combined solution with PBS and it contains 10 ^g of PRP and 3.5 op units of pertussis cells/0.5 ml (dose). <br><br> The results of the antibody response to this combined vaccine in young rats appears in Figures 1 and 2 as shown below. <br><br> - 10 - <br><br> 1 882 <br><br> Example 4 <br><br> The stock solution of PRP (400 jjg/ml) is prepared by dissolving 30 mg PRP (as prepared in Example 1) in 75 ml sterile phosphate buffered saline (PBS) and filtered through 0.45 amillipore filter. To 25 ml of this concentrated PRP is added an equal volume (i.e. 25 ml) of fresh B. pertussis (strain 138) cell suspension in PBS, pH 7.0 (containing 149 op units cells/ml) to prepare the stock solution of the combined vaccine. This stock solution (50 ml) is kept at 4°C for (at least) 90 days. The sterility of the stock solution is tested as aforementioned with thioglycollate media. The pH of the stock solution is pH 7.0+1. The final product (vaccine) used for animal experiments is prepared by diluting the stock combined solution with PBS, and it contains 10 Jig of PRP and 3.7 op units of pertussis cells/0.5 ml (dose). <br><br> Example 5 <br><br> The PRP stock solution (200 ug/ml in PBS (pH 7.0) is prepared as in Example 4. The pertussis stock solution (containing 75 op units/ml) is prepared by diluting 25 ml of fresh B. pertussis cell suspension (149 op units/ml) with an equal volume of PBS. Both stock solutions are incubated separately at 4°C for 90 days or slightly longer. The combined vaccine is made by taking 14 ml of PRP stock solution (200 Ug/ml), plus 14 ml (detoxified) stock solution of pertussis antigens (75 op units/ml) and diluting it with 112 nil PBS (final val. 140 ml). The final vaccine used for animal experiments contains 10 vg PRP and 3.7 op units pertussis/-0.5 ml (dose). <br><br> The results of the antibody response to this combined vaccine in young rats appears in Figure 3 and in Table II. <br><br> - 11 - <br><br> TABLE II <br><br> Immunogenicity of PRP-Pertussis Complex in Young Ratsa <br><br> Anti <br><br> -PRP Antibody Activity (cpm 3H-PRP Bound/50tJl Serum) <br><br> Dose (single or <br><br> Week Post- <br><br> -Injection <br><br> 3rd Week Post-injection (fold increase from <br><br> Vaccine multiple) <br><br> 0 <br><br> 1 <br><br> 2 <br><br> 3 <br><br> preimmunization) <br><br> Phosphate Buffered Saline <br><br> (M)b <br><br> 99° <br><br> 116 <br><br> 107 <br><br> 158 <br><br> 1.6 <br><br> Pertussis <br><br> (M) <br><br> 113 <br><br> 108 <br><br> 117 <br><br> 149 <br><br> 1.3 <br><br> PRP (K) (Example 1) <br><br> (M) <br><br> 110 <br><br> 136 <br><br> 148 <br><br> 142 <br><br> 1.3 <br><br> PRP (K) (3 mo) <br><br> + <br><br> Pertussis (3 no) (Example 5) PRP (K)+Pertussis (3 mo) (Example 4) <br><br> (S)d <br><br> 108 <br><br> 136 <br><br> 132 <br><br> 147 <br><br> 1.4 <br><br> (M) <br><br> (S) (M) <br><br> 101 <br><br> 93 119 <br><br> 135 <br><br> 146 154 <br><br> 1002 <br><br> 135 751 <br><br> 1771 <br><br> 140 1410 <br><br> 17.5 <br><br> 1.5 11.8 <br><br> a) 10 ug PRP or 3.5 op units pertussis/dose (0.5 ml). <br><br> b) Booster - 2nd and 3rd week respectively (multiple injection) <br><br> c) Average 10 rats. <br><br> d) Single injection. <br><br> I382U <br><br> wherein said polyribosyl ribitol phosphate is obtained from Haemophilus influenzae type b Rab strain. <br><br> wherein said Bordetella pertussis antigens are obtained from Bordetella pertussis strain 13 8 and said polyribosyl ribitol phosphate is obtained from Haemophilus influenzae type b Rab strain. <br><br> 15. A combined vaccine according to Claim 11&gt; wherein said young warm-blooded animal is a human child. <br><br> 16. A combined vaccine according to Claim 14^ wherein said young warm-blooded animal is a human child. <br><br> 14. A combined vaccine according to Claim 11 , <br><br> AMERICAN CYANAMID COMPANY <br><br> By t their authorised Agents., <br><br> Per <br><br> - 16 - <br><br> (8821J <br><br> 10. In the method of isolating and purifying immunologically active polyribosyl ribitol phosphate (PRP), the capsular polysaccharide of Haemophilus influenzae type b, by fermenting a strain of the organism Haemophilus influenzae type b under art recognized conditions, isolating the PRP by conventional ethanol precipitation, and further isolating the PRP as a hexadecyltrimethyl ammonium bromide complex by conventional procedures, the improvement comprising: <br><br> 20 mM sodium phosphate buffer at a pH of substantially 5.8 through hydroxylapatite /3Ca.j (PO^) ^ •Ca (OH) 2J' eluting with substantially 5.8, isolating fractions by analysis for PRP, dialyzing the PRP - containing fractions against pyrogen-free distilled water and then lyophilizing the product. <br><br> levels of anti-PRP (polyribosyl ribitol phosphate) and anti-pertussis antibody formation in young warm-blooded animals which consists of polyribosyl ribitol phosphate, <br><br> isolated from the capsular polysaccharide of Haemophilus influenzae type b and purified by adding hydroxylapatite in a substantially 20 mM phosphate buffer at a pH from substantially 6.7 to substantially 6.9, mixing at a temperature of substantially 1 to 4°C., centrifuging, and removing the supernatant and repeating the foregoing procedure at least 2 more times, filtering the supernatant through suitable filters, dialyzing against pyrogen-free distilled water, and then lyophilizing the product; and Bordetella pertussis antigens. <br><br> wherein said Bordetella pertussis antigens are obtained from Bordetella pertussis strain 138. <br><br> purifying the PRP by column chromatography in a <br><br> 20 mM and 50 mM sodium phosphate buffer at a pH of <br><br> 11. A combined vaccine that elicits effective <br><br> 12. A combined vaccine according to Claim 11 &gt; <br><br> 13. A combined vaccine according to Claim 11 <br><br> 15 <br><br> I 88*21I <br><br> 9. In the method of isolating and purifying immunologically active polyribosyl ribitol phosphate (PRP), the capsular polysaccharide of Haemophilus influenzae type b, by fermenting a strain of the organism Haemophilus influenzae type b under art recognized conditions, isolating the PRP by conventional ethanol precipitation, and further isolating the PRP as a hexadecyltrimethyl ammonium bromide complex by conventional procedures, the improvement comprising: <br><br> purifying the PRP by adding hydroxylapatite /3~ .Ca^ (P04) 2Ca- (OH) 2_7 in a 20 mM sodium phosphate buffer at a pH from substantially 6.7 to substantially 6.9, mixing at a temperature of substantially 1-4°C, centrifuging, removing the supernatant and repeating the foregoing procedure at least two more times, filtering the supernatant through suitable filters, dialyzing against pyrogen-free distilled water, and then lyophilizing the product. <br><br></p> </div>

Claims (8)

1882t 1 WHAT WE CLAIM IS:
1. A combined vaccine that elicits anti-PRP (polyribosyl ribitol phosphate) and antipertussis antibody formation in young warm-blooded animals which consists of polyribosyl ribitol phosphate, isolated and purified from the capsular polysaccharide of Haemophilus influenzae type b, and Bordetella pertussis antigens.
2. A combined vaccine according to Claim 1, wherein said Bordetella pertussis antigens are obtained from Bordetella pertussis strain 138.
3. A combined vaccine according to Claim 1, wherein said polyribosyl ribitol phosphate is obtained from Haemophilus influenzae type b Rab strain.
4. A combined vaccine according to Claim 1, wherein said polyribosyl ribitol phosphate is obtained from Haemophilus influenzae type b CK strain.
5. A combined vaccine according to Claim 1, wherein said Bordetella pertussis antigens are obtained from Bordetella pertussis strain 13 8 and said polyribosyl ribitol phosphate is obtained from Haemophilus influenzae type b Rab strain.
6. A combined vaccine according to Claim 1, wherein said Bordetella pertussis antigens are obtained from Bordetella pertussis strain 138 and said polyribosyl ribitol phosphate is obtained from Haemophilus influenzae type b CK strain.
7. A combined vaccine according to any one of Claims 1 to 4, wherein said young warm-blooded animal is a human child.
8. A combined vaccine according to Claim 5 or Claim 6, wherein said young warm-blooded animal is a human child.
NZ188211A 1977-10-28 1978-08-22 Isolation of polyribosyl ribitol phosphate(prp)from haemophilus influenzae type b;vaccine comprising prp and bordetellapertussis antigens NZ188211A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US05/846,466 US4196192A (en) 1977-10-28 1977-10-28 Combined Haemophilus influenzae type b and pertussis vaccine
US05/846,488 US4220717A (en) 1977-12-22 1977-12-22 Isolation and purification of polyribosyl ribitol phosphate from Haemophilus influenzae type b.

Publications (1)

Publication Number Publication Date
NZ188211A true NZ188211A (en) 1984-09-28

Family

ID=27126641

Family Applications (1)

Application Number Title Priority Date Filing Date
NZ188211A NZ188211A (en) 1977-10-28 1978-08-22 Isolation of polyribosyl ribitol phosphate(prp)from haemophilus influenzae type b;vaccine comprising prp and bordetellapertussis antigens

Country Status (25)

Country Link
JP (1) JPS5480408A (en)
AR (1) AR218932A1 (en)
AU (1) AU520902B2 (en)
BE (1) BE871586A (en)
CA (1) CA1117866A (en)
CH (1) CH649781A5 (en)
DD (1) DD140701A5 (en)
DE (1) DE2845745A1 (en)
DK (1) DK154327C (en)
ES (1) ES474611A1 (en)
FI (1) FI63674C (en)
FR (1) FR2407000B1 (en)
GB (1) GB2007244B (en)
GR (1) GR73991B (en)
HU (1) HU178166B (en)
IE (1) IE47474B1 (en)
IL (1) IL55433A (en)
IT (1) IT1107570B (en)
NL (1) NL7810753A (en)
NO (1) NO149611C (en)
NZ (1) NZ188211A (en)
PH (1) PH15882A (en)
PL (1) PL210545A1 (en)
SE (1) SE430753B (en)
YU (1) YU250878A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE889979A (en) * 1981-08-14 1982-02-15 Smith Kline Rit PROCESS FOR THE PREPARATION OF PURIFIED ANTIGENIC CAPSULAR BACTERIAL POLYSACCHARIDES, PRODUCTS OBTAINED AND THEIR USE
CA1209036A (en) * 1982-08-20 1986-08-05 Joseph S.C. Kuo Combined haemophilus influenzae and diphtheria, pertussis, tetanus vaccine
US4744982A (en) * 1982-08-24 1988-05-17 Hunter Kenneth W Human monoclonal antibody reactive with polyribosylribitol phosphate
ATE128628T1 (en) * 1990-08-13 1995-10-15 American Cyanamid Co FIBER HEMAGGLUTININ FROM BORDETELLA PERTUSSIS AS A CARRIER FOR CONJUGATE VACCINE.
SK18594A3 (en) * 1991-08-16 1994-08-10 Merck & Co Inc Method of production of capsular polysacharide without lipid and endotoxine

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3395219A (en) * 1964-12-11 1968-07-30 Merck & Co Inc Process for production of pertussis antigen
NO116869B (en) * 1965-01-19 1969-06-02 Merck & Co Inc
US3465078A (en) * 1965-10-21 1969-09-02 Sydney Z Spiesel Method of recovering antigens from bordetella pertussis cells
NL174267B (en) * 1969-05-20 Roussel Uclaf IMPROVEMENT OF THE PROCESS FOR THE PREPARATION OF A SOMATIC ANTIGEN ACCORDING TO DUTCH PATENT 169754 AND PROCESS FOR PREPARING A PHARMACEUTICAL PREPARATION.
US3636192A (en) * 1970-01-13 1972-01-18 Us Army Meningococcal polysaccharide vaccines
FR2253499B1 (en) * 1973-12-10 1977-11-04 Fabre Sa Pierre
DE2461439C3 (en) * 1974-12-24 1980-03-20 Behringwerke Ag, 3550 Marburg Process for the preparation of a protective antigen from Bordetella pertussis and agent containing the same
US3978209A (en) * 1975-03-24 1976-08-31 Merck & Co., Inc. Endotoxin free meningococcus polysaccharides

Also Published As

Publication number Publication date
NO149611B (en) 1984-02-13
NO149611C (en) 1984-05-23
GB2007244A (en) 1979-05-16
NO783635L (en) 1979-05-02
NL7810753A (en) 1979-05-02
AU520902B2 (en) 1982-03-04
FR2407000A1 (en) 1979-05-25
JPS6231694B2 (en) 1987-07-09
FI783269A (en) 1979-04-29
FR2407000B1 (en) 1983-01-21
IE47474B1 (en) 1984-03-21
JPS5480408A (en) 1979-06-27
IL55433A (en) 1982-09-30
HU178166B (en) 1982-03-28
BE871586A (en) 1979-04-27
AU4108178A (en) 1980-05-01
DE2845745C2 (en) 1987-10-01
DE2845745A1 (en) 1979-05-10
DK154327B (en) 1988-11-07
SE430753B (en) 1983-12-12
PL210545A1 (en) 1980-02-25
DK479578A (en) 1979-04-29
IE782146L (en) 1979-04-28
DK154327C (en) 1989-04-03
GB2007244B (en) 1982-03-31
GR73991B (en) 1984-06-06
CA1117866A (en) 1982-02-09
ES474611A1 (en) 1980-01-16
IT7851621A0 (en) 1978-10-24
YU250878A (en) 1983-12-31
IT1107570B (en) 1985-11-25
FI63674C (en) 1983-08-10
IL55433A0 (en) 1978-10-31
PH15882A (en) 1983-04-13
SE7811192L (en) 1979-04-29
AR218932A1 (en) 1980-07-15
FI63674B (en) 1983-04-29
DD140701A5 (en) 1980-03-26
CH649781A5 (en) 1985-06-14

Similar Documents

Publication Publication Date Title
US4220717A (en) Isolation and purification of polyribosyl ribitol phosphate from Haemophilus influenzae type b.
DE69736709T2 (en) MANY DTP POLIO VACCINES
US4196192A (en) Combined Haemophilus influenzae type b and pertussis vaccine
US4271147A (en) Process for the isolation of membrane proteins from Neisseria meningitidis and vaccines containing same
JP4589852B2 (en) Non-cellular pertussis vaccine and method for producing the same
JPH0231689A (en) Purification of pertussis toxin
Anderson et al. Isolation of the capsular polysaccharide from culture supernatant of Haemophilus influenzae type b
EP0527753A1 (en) Purification of a pertussis outer membrane protein.
EP0407037B1 (en) Process for removing bacterial endotoxin from gram-negative polysaccharides
JPH0662436B2 (en) Method for producing intravenous immunoglobulin preparation
US4402939A (en) Vaccinating glycopeptidic antigenic fraction with a very high level of immunogenicity, isolated from cultures of pathogenic germs, processes for isolating said fraction and vaccines containing said fraction
JPH03191789A (en) Purification of antigenic protein of 69000 dalton from pertussis bacteria
NZ188211A (en) Isolation of polyribosyl ribitol phosphate(prp)from haemophilus influenzae type b;vaccine comprising prp and bordetellapertussis antigens
HELTING et al. SEROTYPE DETERMINANT PROTEIN OF NEISSERIA MENINGITIDIS: Large Scale Preparation by Direct Detergent Treatment of the Bacterial Cells
US3208909A (en) Anaerobic process for production of a gel-adsorbed anthrax immunizing antigen
CA1137901A (en) Isolation of capsular polysaccharide of haemophilus influenzae
US5039610A (en) Process for removing bacterial endotoxin from gram-negative polysaccharides
KR810001317B1 (en) Process for preparing combined vaccine
WO2009016651A1 (en) Simplified means for obtaining prn from bordetella pertussis
JP4777599B2 (en) Method for producing human antithymocyte immunoglobulin
JP3747077B2 (en) Separation and acquisition method of pertussis-derived infection protective components
Lepow et al. Panel Discussion on Purification of Biologic Products: Problems Encountered in the Purification of Toxoids
WO2011043696A1 (en) Process for preparing an iga1 protease from a culture of n. меningiтidis serogroup a and polyvalent vaccine preparation for the prophylaxis of an infection caused by bacteria of n. меningiтidis serogroups а and в
JPS5872526A (en) Preparation of monoclonal hbs antibody
GB1570958A (en) Immunogenic product of tetanus toxin