JPH05502157A - Enzymatic production and recovery of group B Streptococcus type 3 capsular oligosaccharides - Google Patents
Enzymatic production and recovery of group B Streptococcus type 3 capsular oligosaccharidesInfo
- Publication number
- JPH05502157A JPH05502157A JP2514324A JP51432490A JPH05502157A JP H05502157 A JPH05502157 A JP H05502157A JP 2514324 A JP2514324 A JP 2514324A JP 51432490 A JP51432490 A JP 51432490A JP H05502157 A JPH05502157 A JP H05502157A
- Authority
- JP
- Japan
- Prior art keywords
- endo
- galactosidase
- iii
- gbs
- polysaccharide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920001542 oligosaccharide Polymers 0.000 title claims description 10
- 150000002482 oligosaccharides Chemical class 0.000 title claims description 10
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 241000193990 Streptococcus sp. 'group B' Species 0.000 title claims description 6
- 238000011084 recovery Methods 0.000 title claims description 5
- 230000002255 enzymatic effect Effects 0.000 title description 3
- 150000004676 glycans Chemical class 0.000 claims description 41
- 229920001282 polysaccharide Polymers 0.000 claims description 32
- 239000005017 polysaccharide Substances 0.000 claims description 32
- 108010011519 keratan-sulfate endo-1,4-beta-galactosidase Proteins 0.000 claims description 29
- 238000000034 method Methods 0.000 claims description 21
- 239000002775 capsule Substances 0.000 claims description 18
- 239000012634 fragment Substances 0.000 claims description 18
- 108090000790 Enzymes Proteins 0.000 claims description 15
- 102000004190 Enzymes Human genes 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 15
- 239000008346 aqueous phase Substances 0.000 claims description 13
- 239000012071 phase Substances 0.000 claims description 11
- 150000004804 polysaccharides Polymers 0.000 claims description 9
- 230000001580 bacterial effect Effects 0.000 claims description 7
- 239000000758 substrate Substances 0.000 claims description 7
- 241000894006 Bacteria Species 0.000 claims description 6
- 239000008103 glucose Substances 0.000 claims description 6
- 241000588919 Citrobacter freundii Species 0.000 claims description 5
- 230000029087 digestion Effects 0.000 claims description 5
- 241001136276 Sphingobacterium multivorum Species 0.000 claims description 2
- 241000194017 Streptococcus Species 0.000 claims description 2
- 239000002250 absorbent Substances 0.000 claims description 2
- 230000002745 absorbent Effects 0.000 claims description 2
- 238000004925 denaturation Methods 0.000 claims description 2
- 230000036425 denaturation Effects 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- 238000002360 preparation method Methods 0.000 claims description 2
- 230000004044 response Effects 0.000 claims description 2
- 241000606124 Bacteroides fragilis Species 0.000 claims 1
- 206010011416 Croup infectious Diseases 0.000 claims 1
- 102100025342 Voltage-dependent N-type calcium channel subunit alpha-1B Human genes 0.000 claims 1
- 101710088658 Voltage-dependent N-type calcium channel subunit alpha-1B Proteins 0.000 claims 1
- 201000010549 croup Diseases 0.000 claims 1
- 238000004064 recycling Methods 0.000 claims 1
- 238000011146 sterile filtration Methods 0.000 claims 1
- 235000018102 proteins Nutrition 0.000 description 12
- 102000004169 proteins and genes Human genes 0.000 description 12
- 108090000623 proteins and genes Proteins 0.000 description 12
- 102000015728 Mucins Human genes 0.000 description 7
- 108010063954 Mucins Proteins 0.000 description 7
- 150000003214 pyranose derivatives Chemical group 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 5
- 229920001817 Agar Polymers 0.000 description 4
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 4
- 239000008272 agar Substances 0.000 description 4
- 238000010168 coupling process Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000002609 medium Substances 0.000 description 4
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 229960005486 vaccine Drugs 0.000 description 3
- WQZGKKKJIJFFOK-SVZMEOIVSA-N (+)-Galactose Chemical compound OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@H]1O WQZGKKKJIJFFOK-SVZMEOIVSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 108010059712 Pronase Proteins 0.000 description 2
- 229960000583 acetic acid Drugs 0.000 description 2
- 239000000427 antigen Substances 0.000 description 2
- 102000036639 antigens Human genes 0.000 description 2
- 108091007433 antigens Proteins 0.000 description 2
- 239000000872 buffer Substances 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000000502 dialysis Methods 0.000 description 2
- DMBHHRLKUKUOEG-UHFFFAOYSA-N diphenylamine Chemical compound C=1C=CC=CC=1NC1=CC=CC=C1 DMBHHRLKUKUOEG-UHFFFAOYSA-N 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- 239000001963 growth medium Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229940051875 mucins Drugs 0.000 description 2
- MBLBDJOUHNCFQT-UHFFFAOYSA-N n-(3,4,5,6-tetrahydroxy-1-oxohexan-2-yl)acetamide Chemical compound CC(=O)NC(C=O)C(O)C(O)C(O)CO MBLBDJOUHNCFQT-UHFFFAOYSA-N 0.000 description 2
- 239000008223 sterile water Substances 0.000 description 2
- 210000002784 stomach Anatomy 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 108091003079 Bovine Serum Albumin Proteins 0.000 description 1
- 238000009631 Broth culture Methods 0.000 description 1
- 102000014914 Carrier Proteins Human genes 0.000 description 1
- 108010078791 Carrier Proteins Proteins 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 241000605056 Cytophaga Species 0.000 description 1
- 229920002307 Dextran Polymers 0.000 description 1
- 108010053187 Diphtheria Toxin Proteins 0.000 description 1
- 102000016607 Diphtheria Toxin Human genes 0.000 description 1
- 241000589565 Flavobacterium Species 0.000 description 1
- 102000009338 Gastric Mucins Human genes 0.000 description 1
- 108010009066 Gastric Mucins Proteins 0.000 description 1
- 102000006395 Globulins Human genes 0.000 description 1
- 108010044091 Globulins Proteins 0.000 description 1
- 102000011782 Keratins Human genes 0.000 description 1
- 108010076876 Keratins Proteins 0.000 description 1
- PQMWYJDJHJQZDE-UHFFFAOYSA-M Methantheline bromide Chemical compound [Br-].C1=CC=C2C(C(=O)OCC[N+](C)(CC)CC)C3=CC=CC=C3OC2=C1 PQMWYJDJHJQZDE-UHFFFAOYSA-M 0.000 description 1
- 125000003047 N-acetyl group Chemical group 0.000 description 1
- OVRNDRQMDRJTHS-RTRLPJTCSA-N N-acetyl-D-glucosamine Chemical group CC(=O)N[C@H]1C(O)O[C@H](CO)[C@@H](O)[C@@H]1O OVRNDRQMDRJTHS-RTRLPJTCSA-N 0.000 description 1
- 229920005654 Sephadex Polymers 0.000 description 1
- 239000012507 Sephadex™ Substances 0.000 description 1
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 206010043376 Tetanus Diseases 0.000 description 1
- 108010055044 Tetanus Toxin Proteins 0.000 description 1
- 239000007983 Tris buffer Substances 0.000 description 1
- 238000005903 acid hydrolysis reaction Methods 0.000 description 1
- 230000005875 antibody response Effects 0.000 description 1
- 125000001488 beta-D-galactosyl group Chemical group C1([C@H](O)[C@@H](O)[C@@H](O)[C@H](O1)CO)* 0.000 description 1
- 102000005936 beta-Galactosidase Human genes 0.000 description 1
- 108010005774 beta-Galactosidase Proteins 0.000 description 1
- SQVRNKJHWKZAKO-UHFFFAOYSA-N beta-N-Acetyl-D-neuraminic acid Natural products CC(=O)NC1C(O)CC(O)(C(O)=O)OC1C(O)C(O)CO SQVRNKJHWKZAKO-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229940098773 bovine serum albumin Drugs 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 230000010261 cell growth Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 1
- 230000001268 conjugating effect Effects 0.000 description 1
- 230000021615 conjugation Effects 0.000 description 1
- 239000012228 culture supernatant Substances 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000001079 digestive effect Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 229930182830 galactose Natural products 0.000 description 1
- FJEKYHHLGZLYAT-FKUIBCNASA-N galp Chemical compound C([C@@H](C(=O)N[C@@H](CC(C)C)C(=O)N1CCC[C@H]1C(=O)N[C@@H](CCC(N)=O)C(=O)N[C@@H](CCSC)C(=O)NCC(=O)N[C@@H](CC(O)=O)C(=O)N[C@@H](CCC(N)=O)C(=O)N[C@@H](CC(O)=O)C(=O)NCC(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H](CCC(O)=O)C(=O)N[C@H](C(=O)N[C@@H](C)C(=O)N[C@@H](CC(C)C)C(=O)N[C@@H](CCC(O)=O)C(=O)N[C@H](C(=O)N[C@@H](CC(C)C)C(=O)N[C@@H](CC(O)=O)C(=O)N[C@@H](CC(C)C)C(=O)N[C@@H](CC=1C2=CC=CC=C2NC=1)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H](C)C(=O)N[C@@H]([C@@H](C)CC)C(=O)N[C@@H](CC(O)=O)C(=O)NCC(=O)N[C@@H](CC(C)C)C(=O)N1[C@@H](CCC1)C(=O)N[C@@H](CC=1C=CC(O)=CC=1)C(=O)N[C@@H](CO)C(=O)N[C@@H](CC=1N=CNC=1)C(=O)N1[C@@H](CCC1)C(=O)N1[C@@H](CCC1)C(=O)N[C@@H](CCC(N)=O)C(=O)N1[C@@H](CCC1)C(=O)N[C@@H](CO)C(O)=O)[C@@H](C)CC)[C@@H](C)O)NC(=O)[C@H](CC(C)C)NC(=O)[C@@H](NC(=O)[C@H]1N(CCC1)C(=O)CNC(=O)[C@H](CC(C)C)NC(=O)[C@H](CC(C)C)NC(=O)[C@H](CC=1C=CC(O)=CC=1)NC(=O)CNC(=O)[C@H](C)NC(=O)[C@H](CO)NC(=O)[C@H](CC(N)=O)NC(=O)[C@H](CC(C)C)NC(=O)[C@@H](NC(=O)[C@H](CC=1C2=CC=CC=C2NC=1)NC(=O)CNC(=O)CNC(=O)[C@H](CCCNC(N)=N)NC(=O)CNC(=O)[C@H](CCCNC(N)=N)NC(=O)[C@H](CC=1N=CNC=1)NC(=O)[C@H](C)NC(=O)[C@H]1N(CCC1)C(=O)[C@H](C)N)[C@@H](C)O)C(C)C)C1=CNC=N1 FJEKYHHLGZLYAT-FKUIBCNASA-N 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 238000002523 gelfiltration Methods 0.000 description 1
- 239000012362 glacial acetic acid Substances 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 230000002163 immunogen Effects 0.000 description 1
- 230000005847 immunogenicity Effects 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000002198 insoluble material Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 235000015277 pork Nutrition 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 235000004252 protein component Nutrition 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- SQVRNKJHWKZAKO-OQPLDHBCSA-N sialic acid Chemical compound CC(=O)N[C@@H]1[C@@H](O)C[C@@](O)(C(O)=O)OC1[C@H](O)[C@H](O)CO SQVRNKJHWKZAKO-OQPLDHBCSA-N 0.000 description 1
- 125000005629 sialic acid group Chemical group 0.000 description 1
- 239000001632 sodium acetate Substances 0.000 description 1
- 235000017281 sodium acetate Nutrition 0.000 description 1
- 239000007974 sodium acetate buffer Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000003595 spectral effect Effects 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 description 1
- 238000002255 vaccination Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/14—Preparation of compounds containing saccharide radicals produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase, e.g. by cellulase, hemicellulase
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/24—Hydrolases (3) acting on glycosyl compounds (3.2)
- C12N9/2402—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
- C12N9/2468—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1) acting on beta-galactose-glycoside bonds, e.g. carrageenases (3.2.1.83; 3.2.1.157); beta-agarase (3.2.1.81)
- C12N9/2471—Beta-galactosidase (3.2.1.23), i.e. exo-(1-->4)-beta-D-galactanase
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12Y—ENZYMES
- C12Y302/00—Hydrolases acting on glycosyl compounds, i.e. glycosylases (3.2)
- C12Y302/01—Glycosidases, i.e. enzymes hydrolysing O- and S-glycosyl compounds (3.2.1)
- C12Y302/01023—Beta-galactosidase (3.2.1.23), i.e. exo-(1-->4)-beta-D-galactanase
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- Microbiology (AREA)
- Biotechnology (AREA)
- Biomedical Technology (AREA)
- Molecular Biology (AREA)
- Medicinal Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Safety Valves (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 グループB連鎖球菌NI型莢膜オリゴ塘の酵素学的産生及び回収 I1立1遣 た資金によりなされたものであり、政府は本発明にある種の権利を持っている。[Detailed description of the invention] Enzymatic production and recovery of group B Streptococcus type NI capsular oligosaccharides I1 standing 1 ken The government has certain rights in the invention.
本発明の一般的分野は、グループB連鎖球菌(5treptococcus ) III型(CBS−III)多糖莢膜(pc)に有用な抗体を産生させるため の抗原及びこれらの抗原を得るための方法である。The general field of the invention is Group B Streptococcus To produce antibodies useful for type III (CBS-III) polysaccharide capsule (PC) antigens and methods for obtaining these antigens.
CBS−III多塘莢膜がG B S −III遣鎖球菌の培養物から回収でき ること、それがG B S −III感染症を防ぐ抗体反応を生じさせ得ること が知られている4例えば、カスパー氏の米国特許第4207414号及び同43 67223号並びに再発行特許第31672号は、連鎖球菌を特定の条件で培養 することによりG B S −rrlに対して特異的な大きい(0,8〜6XI O’ダルトン)精製された多糖抗体の回収を特徴としている。多糖莢膜は十分に 特徴づけられており、D−N−アセチルグルコサミン(ピラノース形)がβ1− 3結合によりD−ガラクトース(ピラノース形)に連結し、後者がさらにβ1− 4結合によりD−グルコース(ピラノース形に)連結してなる主鎖を形成するよ うに配列された数百個の繰り返し単位からなる。グルコースは、βt−s結合に より次の繰り返し単位中のD−N−アセチルグルコサミン残基に連結されている 。各繰り返し単位は、1−4結合により主鎖のD−N−アセチルグルコサミンに 結合された側鎖を有する。この側mは、第1図に示すように主鎖に結合したD− ガクドースに2〜3結合により結合した末端シアリン酸残基かうなる。第1図は この繰り返し単位を示す、第1図において、GlcNAcpはN−アセチルグル コサミン(ピラノース形)を表わし、GaLpはガラクトース(ピラノース形) を表わし、Glcpはグルコース(ピラノース形)を表わし、α−D−NANA はシアリン酸を表わす。CBS-III multilayer capsules can be recovered from cultures of GBS-III streptococci. and that it can generate an antibody response that protects against GBS-III infection. For example, Kasper U.S. Pat. No. 4,207,414 and 43 No. 67223 and Reissue Patent No. 31672 involve culturing streptococci under specific conditions. By doing so, a large (0,8~6XI O'Dalton) is characterized by the recovery of purified polysaccharide antibodies. polysaccharide capsule is sufficient It has been characterized that D-N-acetylglucosamine (pyranose form) is 3 bonds to D-galactose (pyranose form), and the latter is further linked to β1- D-glucose (in the form of pyranose) is linked by 4 bonds to form a main chain. It consists of hundreds of repeating units arranged in a uniform pattern. Glucose connects to the βt-s bond is linked to a D-N-acetylglucosamine residue in the next repeating unit. . Each repeating unit connects to D-N-acetylglucosamine in the main chain through 1-4 bonds. with attached side chains. This side m is D- attached to the main chain as shown in Figure 1. It consists of a terminal sialic acid residue bound to Gakudose through 2-3 bonds. Figure 1 is In Figure 1, which shows this repeating unit, GlcNAcp is an N-acetyl group. Cosamine (pyranose form), GaLp represents galactose (pyranose form) , Glcp represents glucose (pyranose form), α-D-NANA represents sialic acid.
l見立11 我々は、G B S −III多糖莢膜の繰り返し単位を無傷で保持する多糖断 片(第1図を参照)が免疫学的に有用であり、そしてG B S −III多塘 莢膜から径免疫学的に産生させることができることを見出した。我々は、用語「 多糖莢膜」を、一般に数百個の繰り返し単位を含有する天然産G B S −I II多糖莢膜を説明するために使用する。また、我々は、′用語「多糖断片」又 は「オリゴ塘」を、本発明に従って産生されたG B S −III多糖莢膜の 断片(好ましくは1〜150個の単位、最も好ましくは50個以下の単位)を説 明するために使用する。l Mitate 11 We present a polysaccharide fragment that retains the repeating unit of the GBS-III polysaccharide capsule intact. fragment (see Figure 1) is immunologically useful and It has been found that the diameter can be immunologically produced from the capsule. We use the term “ The polysaccharide capsule is a naturally occurring GBS-I that generally contains several hundred repeating units. II is used to describe the polysaccharide capsule. We also use the term “polysaccharide fragment” or ``oligotang'' of GBS-III polysaccharide capsule produced according to the present invention. fragments (preferably 1 to 150 units, most preferably 50 units or less) Used to clarify.
本発明の一局面は、グループB連鎖球菌(5treptococcus ) I II型(CBS−III)多糖莢M(PC)を選択的に消化して無傷でCBS− rrlPc繰り返し単位からなる多糖莢膜の断片を生じさせる方法を特徴とする 。この方法は、GBS−IIIPCを用意し、そのGBS−111PC主鎖中の ガラクトースーグルコースグゾコシド結合(第1図の矢印を参照)に特異的であ り且つその他のCBS−IIIPCグリコシド結合を実質上加水分解しない細菌 エンド−β−ガラクトシダーゼと該GBS−IrIPCを反応させることにより そのGBS−111PCを消化させ、次いで得られた断片を回収することからな る1本発明の第一の局面の好ましい具体例においては、多糖断片はCBS−II IPCよりも実質的に小さい0例えば、それらは、150個以下(最も好ましく は50個以下)の繰返し単位を含有する。また、それらは大きい多糖成分から分 離される。また好ましくは、エンド−β−ガラクトシダーゼは、酵素基質(例え ば分解ムチン)に露出させることにより酵素を生成させるように誘発できる細菌 から得ることができるものである。シトロバクチル・フロインシイ(Citro bacter freundii)は酵素を作るように誘発させることができ、 このような細菌は特に好ましい細菌源である。さらに好ましくは、CBS−II IPCの消化は、多糖莢膜をエンド−β−ガラクトシダーゼの無菌のろ過された 製剤と酵素の変性温度よりも低い温度(例えば37℃以下)で少なくとも10時 間で且つ5日以内にわたってインキュベートすることに書フて達成される。One aspect of the invention is that group B Streptococcus I Type II (CBS-III) polysaccharide capsule M (PC) is selectively digested to intact CBS- Features a method for producing a fragment of a polysaccharide capsule consisting of rrlPc repeating units . In this method, GBS-IIIPC is prepared, and the main chain of GBS-111PC is specific for the galactose-glucose gluzocoside bond (see arrow in Figure 1). and other CBS-IIIPC glycosidic bonds that do not substantially hydrolyze By reacting endo-β-galactosidase with the GBS-IrIPC There is no need to digest the GBS-111PC and then collect the resulting fragments. In a preferred embodiment of the first aspect of the invention, the polysaccharide fragment is CBS-II For example, they are substantially less than 150 (most preferably contains up to 50 repeating units). In addition, they can be separated from large polysaccharide components. be separated. Also preferably, the endo-β-galactosidase contains an enzyme substrate (e.g. bacteria that can be induced to produce enzymes by exposure to degradable mucins It is something that can be obtained from Citrobacterium froinsii (Citro) bacter freundii) can be induced to make enzymes, Such bacteria are particularly preferred bacterial sources. More preferably, CBS-II Digestion of IPC was carried out using endo-β-galactosidase sterile filtered polysaccharide capsules. At least 10 hours at a temperature below the denaturation temperature of the formulation and enzyme (e.g. below 37°C) This is accomplished by incubating for up to 5 days.
本発明の第一の局面は、G B S −III多糖莢膜の断片を使用して抗G B S −III抗体を生じさせる免疫原性複合体を形成させるのを可能にさせ る(例えば能動的又は受動的ワクチン接種において)。特に、蛋白成分に対する 複合体化は免疫原性を改善又は発生させるのに望ましい、このような複合体の多 糖成分としてこれらの断片を使用することは有益なことである。なぜならば、な かんずく、カップリング方法が天然産の多糖莢膜全体に蛋白をカップリングさせ るよりも多糖の断片に蛋白をカップリングさせる方がより信頼できるからであり 、またこのような断片はカップリング方法をより良く制御し且つ得られる複合体 の収率を向上させるからである。A first aspect of the invention provides anti-G allow the formation of immunogenic complexes that give rise to BSS-III antibodies. (e.g. in active or passive vaccination). Especially for protein components. Conjugation is desirable to improve or generate immunogenicity of multiple such conjugates. It is advantageous to use these fragments as sugar components. Because, Specifically, the coupling method couples the protein to the entire naturally occurring polysaccharide capsule. This is because coupling proteins to polysaccharide fragments is more reliable than coupling proteins to polysaccharide fragments. , such fragments also allow for better control of the coupling method and the resulting conjugate. This is because it improves the yield of.
本発明の第二の局面は、一般に、GBS−i’1lPc主鎖中のガラクトース− グルコースグリコシド結合に対して特異的であり且つその他のGBS−TIIP Cグリコシド結合を実質上加水分解しないエンド−β−ガラクトシダーゼを製造 する方法を特徴とする。この方法は、i)液状水性相、ii)水不溶性であり且 つその境界面において該液状水性相と接している第二の相及び11】)該水性相 と第二の相との間の境界面において一般に該液状水性相中に配置された細菌細胞 を含む多相培地を使用する。エンド−β−ガラクトシダーゼは、液状水性相から 回収される。A second aspect of the invention generally relates to galactose- GBS-TIIP specific for glucose glycosidic bonds and other Production of endo-β-galactosidase that does not substantially hydrolyze C-glycosidic bonds It features a method of The method comprises: i) a liquid aqueous phase; ii) a water-insoluble and a second phase in contact with the liquid aqueous phase at its interface; and 11]) the aqueous phase; bacterial cells generally disposed in the liquid aqueous phase at the interface between the liquid aqueous phase and the second phase; Use a multiphase medium containing Endo-β-galactosidase is extracted from the liquid aqueous phase. It will be collected.
本発明の第二の局面の好ましい具体例においては、エンド−β−ガラクトシダー ゼは、微生物(例えばシトロバクチル・フロインシイ)であってその酵素の生成 が化学的に分解されたムチン(例えば酸化及び酸加水分解により)のような酵素 のための基質の存在に応じて誘発されるものから得ることができるものである。In a preferred embodiment of the second aspect of the invention, endo-β-galactosidase enzymes are microorganisms (e.g. Citrobacterium froinsii) that produce enzymes. enzymes such as mucins that have been chemically degraded (e.g. by oxidation and acid hydrolysis) This is what can be obtained from those that are induced in response to the presence of a substrate for.
酵素基質は、好ましくは第二の相中に含められる。また、好ましくは、第二の相 は、水性吸収性重合体又は水性ゲルである。The enzyme substrate is preferably included in the second phase. Also preferably, the second phase is an aqueous absorbent polymer or an aqueous gel.
本発明の第二の局面は、高い細胞密度と高収率の酵素の回収を可能にする。The second aspect of the invention allows for high cell densities and high yields of enzyme recovery.
本発明の第三の局面は、G B S −III多塘莢膜の無傷の繰返し単位を含 む実質的に単離されたG B S −[1多塘莢膜断片を特徴としている。「実 質的に単離された」とは、G B S −III多塘莢膜及びその他の反応成分 から有効に分離されていることを意味する。但し、少量のこれらの又はその他の 異物が存在できる可能性を排除するものではない、好ましくは、断片は、1〜1 50(最も好ましくは1〜50)個のGBS−IIIPC繰返し単位からなる。A third aspect of the invention comprises an intact repeating unit of GBS-III multilayer capsule. The present invention is characterized by substantially isolated GBS-[1 multicapsule fragments comprising: "fruit ``Qualitatively isolated'' means GBS-III polycapsules and other reaction components. means that it is effectively separated from the However, small amounts of these or other Preferably, the fragments are between 1 and 1, without excluding the possibility that foreign bodies may be present. Consisting of 50 (most preferably 1 to 50) GBS-III PC repeat units.
本発明のその他の特徴及び利点は、以下の妬ましい具体例の説明及び請求項から 明らかとなろう。Other features and advantages of the invention will be apparent from the following description of exemplary embodiments and from the claims. It will become clear.
好JL長」二A工生旦ユII I 第1図は、G B S −III多糖莢膜の繰返し単位の式である。Good JL Chief” 2A Engineer Dan Yu II I FIG. 1 is the formula of the repeating unit of the GBS-III polysaccharide capsule.
第2図は、培養装置の図である。FIG. 2 is a diagram of the culture apparatus.
GBSニュ匡11J1ユI」 本発明において出発物質として使用するのに好適な実質的に単離されたG B S −III莢膜多塘を得る方法は一般的には周知である。特に、カスパー氏の 米国再発行特許第31672号は、連鎖球菌の培養及びG B S −+rl莢 1@多糖の取得を開示している。GBS New 11J1 Yu I” Substantially isolated G B suitable for use as a starting material in the present invention Methods for obtaining S-III capsular membranes are generally well known. Especially Mr. Kasper's U.S. Reissue Patent No. 31,672 describes the cultivation of streptococci and 1@Discloses the acquisition of polysaccharides.
エンド−−ガラクトシダーゼの ′ 本発明で使用されるエンド−β−ガラクトシダーゼは、主鎖中の繰返し単位1個 当たりただ一つの箇所においてG B S −III多糖莢膜を特異的に解裂さ せ、側鎖を無傷で残し且つ完全な莢膜多糖単位の繰返しを含むオリゴ塘を生じさ せるものでなければならない。Endo-galactosidase ′ The endo-β-galactosidase used in the present invention has one repeating unit in the main chain. specifically cleaved the GBS-III polysaccharide capsule at only one location to produce an oligomer that leaves the side chains intact and contains a complete repeat of the capsular polysaccharide unit. It must be something that can be done.
好適なエンド−β−ガラクトシダーゼの好ましい細菌源は、シトロバクチル・フ ロインシイ(Citrobacter freundii) (以前の名称はニ ジエリチア・フロインシイ(Esherichia freundii )であ って、これは、中用氏他の1”J、Biol、Chem、J 255:5955 −5959 (1980)、北御門氏他の「日本水産学会誌」旦Jpn、Soc 、Sci、Fish、 ]36 ;592−596 (1970)及び北御門氏 他の「日本水産学会誌J 36 : 592 (1970)に報告されているよ うにして得ることができる。また、シトロバクチル・フロインシイはこれらの著 者から入手することもできる。A preferred bacterial source of suitable endo-β-galactosidase is Citrobacterium Citrobacter freundii (formerly known as Citrobacter freundii) It is Escherichia freundii. So, this is Mr. Nakayo et al.'s 1"J, Biol, Chem, J 255:5955 -5959 (1980), “Journal of the Japanese Fisheries Society” by Mr. Kitamikado et al., DanJpn, Soc. , Sci, Fish, ] 36; 592-596 (1970) and Kitamikado. It is reported in another article, ``Journal of the Japanese Society of Fisheries Science, J 36: 592 (1970). You can get it like this. In addition, Citrobacterium froinsii was described by these authors. It can also be obtained from.
これらの細胞は、特に多量のエンド−β−ガラクトシダーゼを生成させるように 二相培地中で多糖誘発物質と共に増殖される0本発明を限定するわけではないが 、本発明で使用できる特定の増殖培地の一つは25%(W/V)のハートインフ ュージョンブロス(ジフコ社)、02%(w / v )のスミスの分解豚胃ム チン及び2゜5%(w / v )の精製寒天からなるものである。These cells are specifically designed to produce large amounts of endo-β-galactosidase. Although not limiting the invention, , one particular growth medium that can be used in the present invention is 25% (w/v) heart influenza. Fusion Broth (Difco), 02% (w/v) Smith's Decomposed Pork Stomach Chin and 2.5% (w/v) purified agar.
豚胃ムチン(シグマケミカル社)は、例えば前掲の福田氏(1981)及びスロ ミアニー氏他のrJ、Bi。Porcine gastric mucin (Sigma Chemical Co., Ltd.) is described, for example, by Fukuda (1981) and Slott, cited above. Mr. Miani et al. rJ, Bi.
1、 Chem、 コ 247 、 5062−5070 (1972)に記載 の一般的技術により製造することができる。1, described in Chem, Co. 247, 5062-5070 (1972) It can be manufactured by the general technique of.
まず、粗製ムチン(500g)を水(2リツトル)に溶解し、phを1%NaO Hにより8.0に調節する。プロナーゼ(0,2g)を添加し、トルエン中で3 7℃で1日間インキュベートする6ブロナーゼによる消化を24時間毎に0.2 gのプロナーゼを添加して3日間続ける。次いで、pHを氷酢酸により4.0に 調節し、不溶性物質を遠心分離により除去する。上澄み液に3容の95%エタノ ールを添加する。沈殿したムチンを集め、乾燥する。First, crude mucin (500 g) was dissolved in water (2 liters), and the pH was adjusted to 1% NaO Adjust to 8.0 with H. Add pronase (0.2 g) and Incubate for 1 day at 7 °C. Digest with 6 Bronase every 24 hours. g of pronase and continue for 3 days. The pH was then adjusted to 4.0 with glacial acetic acid. Condition and remove insoluble material by centrifugation. Add 3 volumes of 95% ethanol to the supernatant liquid. Add mol. The precipitated mucin is collected and dried.
上記の増殖培地(1200ml)を4リツトルのエルレンマイヤーフラスコに入 れ、オートクレーブ処理し、固化させる。無菌のd Hx O(300m l )を液体上層として添加し、30℃で終夜平衡化させる。水性土石にムチンを含 有するハートインフュージョンブロス中で30℃で2日間増殖させた2mlのシ トロバクチル・フロインシイの細胞を接種する。3日目に細胞と培地を含有する 液相を取り出し、300m1の無菌水で置き換える。さらに3日間インキュベー トした後、第二の収穫物を得る。Add the above growth medium (1200 ml) to a 4 liter Erlenmeyer flask. Then autoclave and solidify. Sterile dHxO (300ml ) is added as a liquid top layer and equilibrated at 30° C. overnight. Mucin is included in aqueous soil and stone. 2 ml cultures grown for 2 days at 30°C in heart infusion broth with Inoculate with Trobacterium freundschii cells. Contain cells and medium on day 3 The liquid phase is removed and replaced with 300 ml of sterile water. Incubate for another 3 days After harvesting, you will get a second crop.
前記の系において、寒天を主体とした固相は、細胞の増殖のための栄養物及び酵 素の生成を誘発させるための基質(スミスの分解豚胃ムチン)を含有する。液状 水性相は無菌水である。In the above system, the solid phase mainly composed of agar contains nutrients and enzymes for cell growth. Contains a substrate (Smith's degraded porcine stomach mucin) to induce the production of mucin. liquid The aqueous phase is sterile water.
第2図は、二相培養を達成するための器具を概略的に示す、フラスコEは、適切 な空気の供給を行うために綿とガーゼのパッドを含む、ブロス培地又は水拡散物 の液層(H,O)を層Bとして示す、固体寒天培地は[Cとして示す、凹みDは 寒天基剤を保持し、振盪機上でインキュベートするときのその崩壊を防止する。Figure 2 schematically shows the equipment for achieving a two-phase culture, flask E is suitable for Broth medium or water diffuser, including cotton and gauze pads to provide adequate air supply The liquid layer (H, O) of is shown as layer B, the solid agar medium is shown as [C, the depression D Retain the agar base and prevent its collapse when incubating on a shaker.
30℃で24時間後に、上記の系で増殖された細胞ははバッチ式又はブロス式培 養により一般に達成されるよりもはるかに高い。After 24 hours at 30°C, cells grown in the above system are grown in batch or broth culture. much higher than that typically achieved by nutrition.
エンド−−ガラクトシダーゼの。 ・ 。Endo--galactosidase.・ .
エンド−β−ガラクトシダーゼを、一般にリー氏他により rMsthods in、EnzymologyJ1ユ、61.0−625 (1982)に記載の ようにして前記の液状水性相から単離する。培養液を遠心分離(16,300X G、45分、4℃)により浄化し、蛋白を4℃で(NH,)z SO,を75% の飽和まで添加することにより沈殿させる。沈殿を遠心分!11(18,300 XG、15分、4℃)により集め、蒸留水中に懸濁させ、透析管(スペクトルボ ール1、スペクトル・メジカル・インダストリーズ社、ロスアンジェルス、CA )に入れ、4℃でdH20に対して透析する。50mMの酢酸ナトリウム緩衝液 pH5,5に対する透析に続いて、蛋白を同じ緩衝液で平衡化させたQAE−セ ファデックスA−50’(ファルマシアLKB社、スエーデン)カラム(2,6 x25cm)上に置く、カラム画分をエンド−β−ガラクトシダーゼ活性につい て試験する。酵素活性は、20μmのカラム画分をグループB鎖球菌からの60 μgの精製されたIII型多塘と37℃で終夜インキュベートすることによって 実証される1次の日に、消化混合物を減容させて乾固させ、5μmのdHao中 に懸濁させ、薄1クロマトグラフィー(TLC’)プレートに適用する。試料を 2:1:1の容量比の1−ブタノール:酢酸・水よりなる溶媒中で分離する。炭 水化物をジフェニルアミンのスプレィを使用して目視できるようする。エンド− β−ガラクトシダーゼ活性をTLC上でIII型多糖の単一の繰返し五糖類の存 在により検出する。エンド−β−ガラクトシダーゼ活性を含むカラム画分はプー ルしておき、多量のIII型多糖を消化するのに使用した。汚染性のノイラミニ ダーゼは、物質をセファデックスG−100のカラムに通じることによりQAE −セファデックスで精製されたエンド−β−ガラクトシダーゼから分離する。Endo-β-galactosidase is generally described by Lee et al. In, Enzymology J1, 61.0-625 (1982). from the liquid aqueous phase. Centrifuge the culture solution (16,300X G, 45 min, 4°C) and purified the protein at 4°C with (NH,) SO, 75% Precipitate by adding to saturation. Centrifuge the precipitate! 11 (18,300 XG, 15 min, 4°C), suspended in distilled water, and placed in a dialysis tube (spectral bottle). Rule 1, Spectrum Medical Industries, Inc., Los Angeles, CA. ) and dialyzed against dH20 at 4°C. 50mM sodium acetate buffer Following dialysis against pH 5.5, the protein was incubated with QAE-separate equilibrated in the same buffer. Fadex A-50' (Pharmacia LKB, Sweden) column (2,6 x 25 cm) and column fractions were analyzed for endo-β-galactosidase activity. Test. Enzyme activity was determined by comparing the 20 μm column fraction to 60 μm from group B streptococci. By incubating with μg of purified type III Tatsu at 37°C overnight. On the first day of demonstration, the digestion mixture was reduced in volume to dryness and dissolved in 5 μm dHao. and apply to thin 1 chromatography (TLC') plates. sample Separation is carried out in a solvent consisting of 1-butanol:acetic acid/water in a volume ratio of 2:1:1. charcoal Make the hydrate visible using diphenylamine spray. End- β-galactosidase activity was determined on TLC by the presence of a single repeating pentasaccharide of type III polysaccharide. Detected by presence. Column fractions containing endo-β-galactosidase activity are pooled. It was used to digest a large amount of type III polysaccharide. Pollution Noiramini QAE is produced by passing the substance through a column of Sephadex G-100. - Separated from Sephadex-purified endo-β-galactosidase.
乙土工亙二亙ニ ゲループB連鎖球菌の天然III型莢膜多糖を前記(ジェニングス氏他のrCa n、J、Biochem、]58.1.12−120(1980))のようにし て培養上澄み液から精製する。 III型多糖(120m、 g )を5〜10 m lのdHzo中に懸濁させ、0.45μmシリンジフィルター(Mi I l exHA、ミリボア社)を使用して無菌状態で、10m1の無菌消化用緩 衝液(50mMの酢酸ナトリウム、10mMのCaC1z −pH5,5)及び 50mMのdH20を入れた容器内にろ過する。また、酵素製剤を、予め状態調 節した(1mg/m1の牛血清アルブミンのdHa○溶液1 m 1. 、次い でd Hz O3m lをフィルターに通す)0.45μmシリンジフィルター を使用して無菌状態でろ過し、多糖に添加する。多糖の最終濃度はLmg/ml である。消化を37℃で2〜5日間行なわせる。消化を、TLCを使用して毎日 モニターし、単一の反復多糖のバンドの密度が天然のバンドの密度と同じである と思われたときに停止する。消化物を凍結乾燥し、2mlのd H* Oに懸濁 させる。消化物に4℃で(NH−)x SO4を75%(W/ v )の飽和度 まで添加することにより2時間蛋白を沈殿させる。 trr型莢膜オリゴ塘及び 多糖を含有する上澄み液を遠心分離により浄化させ、次いで10m1のトリス緩 衝液pH7,0で平衡化したG−75(1,6X80cm)ゲルろ過カラムに入 れる6画分をモニターしくAm。81111)+塩の溶出よりも前に床の容積ピ ーク前に最初に溶出するA2゜6□のピークに相当するカラム画分についてTL Cを達成して単一の多糖繰り返し単位(lru)及び五糖類又は2繰り返し単位 (2r u)の正確な位置を確認する。早い方の画分に溶出したオリゴ塘の分子 寸法をIruオリゴ糖、2ruオリゴ糖及びデキストラン照準試料の溶出容積に 基ず<K、、の計算によって算定する。Otsudo Kogyo 2nd Station The natural type III capsular polysaccharide of Geloop B Streptococcus was used as described above (rCa n, J. Biochem,] 58.1.12-120 (1980)). Purify from the culture supernatant. Type III polysaccharide (120m, g) 5-10 Suspended in ml of dHzo and filtered with a 0.45 μm syringe filter (MiI 10 ml of sterile digestive fluid under aseptic conditions using buffer solution (50mM sodium acetate, 10mM CaC1z - pH 5,5) and Filter into a container containing 50mM dH20. In addition, condition the enzyme preparation in advance. (1 mg/ml of bovine serum albumin in dHa○ solution 1 ml), then Pass d Hz O3ml through the filter) 0.45μm syringe filter Filter aseptically using a filter and add to the polysaccharide. The final concentration of polysaccharide is Lmg/ml It is. Digestion is allowed to occur for 2-5 days at 37°C. Digestion daily using TLC Monitor and ensure that the density of the single repeating polysaccharide band is the same as the density of the native band. Stop when you think so. Lyophilize the digest and suspend in 2 ml of dH*O let Add (NH-)x SO4 to the digestate at 4°C to a saturation of 75% (W/v). Precipitate the protein by adding up to 2 hours. trr-type capsular oligosaccharide and The supernatant containing polysaccharides was clarified by centrifugation and then poured into 10 ml Tris buffer. Pour into a G-75 (1.6 x 80 cm) gel filtration column equilibrated with buffer pH 7.0. Am to monitor the 6 fractions. 81111) + Bed volumetric peak prior to salt elution. TL for the column fraction corresponding to the A2゜6□ peak that elutes first before A single polysaccharide repeat unit (lru) and a pentasaccharide or two repeat units Check the exact location of (2r u). Oligotang molecules eluted in early fractions Dimensions to elution volumes of Iru oligosaccharides, 2ru oligosaccharides, and dextran aiming samples. It is calculated by calculating the basis <K.
得られた多糖断片は、蛋白に結合して保護抗体を誘発させる免疫原を作り出させ ることができる。複合体の蛋白部分は、不活性キャリアー蛋白であるか、或いは CBS −III蛋白又は破傷風若しくはジフテリアトキシン(CRIM)のよ うな他の細菌からのトキソイド蛋白の如き他の保護を提供する蛋白であってよい 、多糖断片を蛋白に複合体化させるための技術は知られている6例えば、ジェニ ング氏の米国特許第4356120号又はマルバーグ氏の米国特許第46956 24号を参照された得られた複合体は、標準的な方法に従って受動的又は能動的 ワクチンとしてえ使用することができる0例えば、前記のように製造された複合 体は、ジェニング氏の米国特許に記載の技術に従って回収し、通常の塩水溶液に 懸濁させ、カスパー氏の米国再発行特許第31672号に記載のように、ワクチ ンとして注射することができる。また、このカスパー氏の再発行特許第3167 2号に記載のようにグロブリン画分を使用して受動的ワクチン摂取を達成するこ とができる。The resulting polysaccharide fragments create immunogens that bind to proteins and induce protective antibodies. can be done. The protein portion of the complex is an inert carrier protein or CBS-III protein or tetanus or diphtheria toxin (CRIM) may be proteins that provide other protection such as toxoid proteins from other bacteria such as , techniques for conjugating polysaccharide fragments to proteins are known6. Ng U.S. Pat. No. 4,356,120 or Malberg U.S. Pat. No. 46,956. The resulting conjugate, see No. 24, can be passively or actively processed according to standard methods. For example, the conjugate produced as described above can be used as a vaccine. The bodies were recovered according to the technique described in Jenning's US patent and placed in a normal saline solution. Vaccine suspension as described in Kasper U.S. Reissue Patent No. 31,672. It can be injected as an injection. Also, Mr. Kasper's reissued patent No. 3167 Achieving passive vaccine uptake using globulin fractions as described in No. 2 I can do it.
上記の説明は本発明を例示するためのものであって、本発明を制限するものでは ない。その他の具体例も請求項の記載の範囲内にある0例えば、好適なエンド− 〇−ガラクトシダーゼを、大阪布の発酵研究所(IFO)にI FONo 14 087として寄託されたサイトファガ・ケラトリチ力(Cytophaga k eratolytica) (以前の名称フラボバクテリウム・ケラトリチカス (Flavobacteriumkeratolyticus) )から得るこ とができるが、これらの細菌による酵素の生成は(シトロバクチル・フロインシ イからの生成と異なって)誘発を要求しない、そのエンド−β−ガラクトシダー ゼを回収するための好適・な一般的操作は、北御門氏他のrJ、Biol、Ch em、J256;3906−3909 (1981)及び中沢氏他のrJ、Bi ol、Chem、 J 250 : 912−917(1975)に開示されて いる。シトロバクチル・フロインシイのエンド−β−ガラクトシダーゼのその他 の誘発剤は硫酸ケラチン又は他の好適な酵素気質を包含する。The above description is for the purpose of illustrating the present invention and is not intended to limit the present invention. do not have. Other embodiments are also within the scope of the claims. 〇-Galactosidase was sent to Osaka Fabric Fermentation Research Institute (IFO) IFO No. 14 Cytophaga keratricii deposited as 087 eratolytica) (formerly known as Flavobacterium ceratolytica) (Flavobacterium keratolyticus)) However, the production of enzymes by these bacteria The endo-β-galactosidase does not require induction (unlike its production from A). A suitable general procedure for recovering the enzyme is described by Kitamikado et al., rJ, Biol, Ch. em, J256; 3906-3909 (1981) and Nakazawa et al. rJ, Bi ol, Chem, J 250: 912-917 (1975). There is. Other aspects of endo-β-galactosidase of Citrobacter freundii inducing agents include keratin sulfate or other suitable enzymatic agents.
β−D−Galp 国際調査報告β-D-Galp international search report
Claims (15)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US40867089A | 1989-09-18 | 1989-09-18 | |
US408,670 | 1989-09-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05502157A true JPH05502157A (en) | 1993-04-22 |
Family
ID=23617253
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2514324A Pending JPH05502157A (en) | 1989-09-18 | 1990-09-14 | Enzymatic production and recovery of group B Streptococcus type 3 capsular oligosaccharides |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0493521A4 (en) |
JP (1) | JPH05502157A (en) |
AU (1) | AU6538490A (en) |
CA (1) | CA2066036A1 (en) |
WO (1) | WO1991004335A1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6284884B1 (en) | 1995-06-07 | 2001-09-04 | North American Vaccine, Inc. | Antigenic group B streptococcus type II and type III polysaccharide fragments having a 2,5-anhydro-D-mannose terminal structure and conjugate vaccine thereof |
US7060483B1 (en) * | 1999-10-22 | 2006-06-13 | Seikagaku Corporation | DNA encoding endo-β-galactosidase |
AU2001287422A1 (en) * | 2000-08-22 | 2002-03-04 | National Research Council Of Canada | Synthesis of complex carbohydrates |
WO2017175082A1 (en) * | 2016-04-05 | 2017-10-12 | Gsk Vaccines S.R.L. | Immunogenic compositions |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0302887B1 (en) * | 1986-04-16 | 1994-06-22 | The Brigham And Women's Hospital, Inc. | Bacterial antigens, antibodies, vaccines, and methods of manufacture |
-
1990
- 1990-09-14 WO PCT/US1990/005244 patent/WO1991004335A1/en not_active Application Discontinuation
- 1990-09-14 EP EP19900915363 patent/EP0493521A4/en not_active Withdrawn
- 1990-09-14 JP JP2514324A patent/JPH05502157A/en active Pending
- 1990-09-14 CA CA002066036A patent/CA2066036A1/en not_active Abandoned
- 1990-09-14 AU AU65384/90A patent/AU6538490A/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
WO1991004335A1 (en) | 1991-04-04 |
CA2066036A1 (en) | 1991-03-19 |
EP0493521A1 (en) | 1992-07-08 |
AU6538490A (en) | 1991-04-18 |
EP0493521A4 (en) | 1993-05-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Aplin et al. | Preparation, Properties, and Applications of Carbohydrate Conjugates of Proteins and Lipid | |
Paoletti et al. | An oligosaccharide-tetanus toxoid conjugate vaccine against type III group B Streptococcus. | |
Scudder et al. | Isolation and characterization of an endo-β-galactosidase from Bacteroides fragilis | |
US5372942A (en) | Protease K resistant arginine deiminase, its method of preparation and its use as an anti-neoplastic agent | |
Tal et al. | On the nature of the toxic component of the somatic antigen of Shigella paradysenteriae type Z (Flexner) | |
EP0302887B1 (en) | Bacterial antigens, antibodies, vaccines, and methods of manufacture | |
EP0120532A2 (en) | Mucoid exopolysaccharide vaccine against Pseudomonas aeruginosa | |
EP0008969B1 (en) | Vaccine and method of making | |
CA1155057A (en) | Vaccine and method of making | |
CN1230219A (en) | Detection of mammalian heparanase activity and purification of mammalian heparanase | |
NO152281B (en) | PREPARATION OF HEAT STABLE E.COLI ENTEROTOXIN DERIVATIVES | |
JPS6344883A (en) | Novel hyaluronidase sd-678 and production thereof | |
JPH05502157A (en) | Enzymatic production and recovery of group B Streptococcus type 3 capsular oligosaccharides | |
US4356263A (en) | Method of making a polysaccharide vaccine | |
JP2724588B2 (en) | Methods for producing neuraminidase isozyme S and gangliosides | |
US4752578A (en) | Collagenase inducing factor | |
JP2726898B2 (en) | Methods for producing neuraminidase isozyme L and gangliosides | |
CN102462839B (en) | polysaccharide conjugate vaccine and preparation method thereof | |
Pardoe | The inducible neuraminidase (N-acyl-neuraminyl hydrolase EC 3.2. 1.18) of Klebsiella aerogenes NCIB 9479 | |
JPH03227939A (en) | Immunological competence-activating substance and production thereof | |
USRE31672E (en) | Polysaccharide antigens | |
WO2023132795A2 (en) | Modified bacterial glycans and conjugates thereof | |
SU1750690A1 (en) | Method for preparation of escherichia coli conjugated enterotoxin | |
CN117467001A (en) | Preparation method and application of clostridium perfringens antitoxin A serum | |
EP0091745A1 (en) | Preparation of an antibiotic selectively effective against staphylococcus infections |