DK143765B - METHOD FOR PRODUCING YEAR CELL MASS WITH HIGH PROTEIN CONTENT - Google Patents
METHOD FOR PRODUCING YEAR CELL MASS WITH HIGH PROTEIN CONTENT Download PDFInfo
- Publication number
- DK143765B DK143765B DK560477AA DK560477A DK143765B DK 143765 B DK143765 B DK 143765B DK 560477A A DK560477A A DK 560477AA DK 560477 A DK560477 A DK 560477A DK 143765 B DK143765 B DK 143765B
- Authority
- DK
- Denmark
- Prior art keywords
- strain
- cell mass
- methanol
- protein content
- high protein
- Prior art date
Links
- 238000004519 manufacturing process Methods 0.000 title description 9
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 42
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 18
- 239000002028 Biomass Substances 0.000 description 11
- 108090000623 proteins and genes Proteins 0.000 description 8
- 102000004169 proteins and genes Human genes 0.000 description 8
- 239000000758 substrate Substances 0.000 description 8
- 239000001963 growth medium Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 5
- 238000000855 fermentation Methods 0.000 description 5
- 230000004151 fermentation Effects 0.000 description 5
- 239000002609 medium Substances 0.000 description 5
- 239000003208 petroleum Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- YBJHBAHKTGYVGT-ZKWXMUAHSA-N (+)-Biotin Chemical compound N1C(=O)N[C@@H]2[C@H](CCCCC(=O)O)SC[C@@H]21 YBJHBAHKTGYVGT-ZKWXMUAHSA-N 0.000 description 4
- 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 4
- 241000222120 Candida <Saccharomycetales> Species 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 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
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 210000004027 cell Anatomy 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 210000005253 yeast cell Anatomy 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- OWEGMIWEEQEYGQ-UHFFFAOYSA-N 100676-05-9 Natural products OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(OC2C(OC(O)C(O)C2O)CO)O1 OWEGMIWEEQEYGQ-UHFFFAOYSA-N 0.000 description 2
- FBPFZTCFMRRESA-KVTDHHQDSA-N D-Mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KVTDHHQDSA-N 0.000 description 2
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 description 2
- GUBGYTABKSRVRQ-PICCSMPSSA-N Maltose Natural products O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 2
- 229930006000 Sucrose Natural products 0.000 description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 229960002685 biotin Drugs 0.000 description 2
- 235000020958 biotin Nutrition 0.000 description 2
- 239000011616 biotin Substances 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 2
- 239000008101 lactose Substances 0.000 description 2
- 108020004707 nucleic acids Proteins 0.000 description 2
- 102000039446 nucleic acids Human genes 0.000 description 2
- 150000007523 nucleic acids Chemical class 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000005720 sucrose Substances 0.000 description 2
- 239000011573 trace mineral Substances 0.000 description 2
- 235000013619 trace mineral Nutrition 0.000 description 2
- 239000012138 yeast extract Substances 0.000 description 2
- CDVZCUKHEYPEQS-GGVUXYEMSA-N (2s,3r,4r)-2,3,4,5-tetrahydroxypentanal;(2r,3r,4r)-2,3,4,5-tetrahydroxypentanal Chemical compound OC[C@@H](O)[C@@H](O)[C@@H](O)C=O.OC[C@@H](O)[C@@H](O)[C@H](O)C=O CDVZCUKHEYPEQS-GGVUXYEMSA-N 0.000 description 1
- PYMYPHUHKUWMLA-UHFFFAOYSA-N 2,3,4,5-tetrahydroxypentanal Chemical compound OCC(O)C(O)C(O)C=O PYMYPHUHKUWMLA-UHFFFAOYSA-N 0.000 description 1
- 102100034612 Annexin A4 Human genes 0.000 description 1
- 108090000669 Annexin A4 Proteins 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- GUBGYTABKSRVRQ-CUHNMECISA-N D-Cellobiose Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-CUHNMECISA-N 0.000 description 1
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 1
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 1
- QWIZNVHXZXRPDR-UHFFFAOYSA-N D-melezitose Natural products O1C(CO)C(O)C(O)C(O)C1OC1C(O)C(CO)OC1(CO)OC1OC(CO)C(O)C(O)C1O QWIZNVHXZXRPDR-UHFFFAOYSA-N 0.000 description 1
- SRBFZHDQGSBBOR-IOVATXLUSA-N D-xylopyranose Chemical compound O[C@@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-IOVATXLUSA-N 0.000 description 1
- 239000004386 Erythritol Substances 0.000 description 1
- UNXHWFMMPAWVPI-UHFFFAOYSA-N Erythritol Natural products OCC(O)C(O)CO UNXHWFMMPAWVPI-UHFFFAOYSA-N 0.000 description 1
- SQUHHTBVTRBESD-UHFFFAOYSA-N Hexa-Ac-myo-Inositol Natural products CC(=O)OC1C(OC(C)=O)C(OC(C)=O)C(OC(C)=O)C(OC(C)=O)C1OC(C)=O SQUHHTBVTRBESD-UHFFFAOYSA-N 0.000 description 1
- 229920001202 Inulin Polymers 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 241000364057 Peoria Species 0.000 description 1
- MUPFEKGTMRGPLJ-RMMQSMQOSA-N Raffinose Natural products O(C[C@H]1[C@@H](O)[C@H](O)[C@@H](O)[C@@H](O[C@@]2(CO)[C@H](O)[C@@H](O)[C@@H](CO)O2)O1)[C@@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 MUPFEKGTMRGPLJ-RMMQSMQOSA-N 0.000 description 1
- JVWLUVNSQYXYBE-UHFFFAOYSA-N Ribitol Natural products OCC(C)C(O)C(O)CO JVWLUVNSQYXYBE-UHFFFAOYSA-N 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- MUPFEKGTMRGPLJ-UHFFFAOYSA-N UNPD196149 Natural products OC1C(O)C(CO)OC1(CO)OC1C(O)C(O)C(O)C(COC2C(C(O)C(O)C(CO)O2)O)O1 MUPFEKGTMRGPLJ-UHFFFAOYSA-N 0.000 description 1
- AOONYBGXPVAVPT-UHFFFAOYSA-N acetic acid;2-hydroxypropane-1,2,3-tricarboxylic acid;2-hydroxypropanoic acid Chemical compound CC(O)=O.CC(O)C(O)=O.OC(=O)CC(O)(C(O)=O)CC(O)=O AOONYBGXPVAVPT-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 description 1
- DLRVVLDZNNYCBX-ZZFZYMBESA-N beta-melibiose Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@@H]1OC[C@@H]1[C@@H](O)[C@H](O)[C@@H](O)[C@H](O)O1 DLRVVLDZNNYCBX-ZZFZYMBESA-N 0.000 description 1
- OHJMTUPIZMNBFR-UHFFFAOYSA-N biuret Chemical compound NC(=O)NC(N)=O OHJMTUPIZMNBFR-UHFFFAOYSA-N 0.000 description 1
- 229940041514 candida albicans extract Drugs 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000019414 erythritol Nutrition 0.000 description 1
- UNXHWFMMPAWVPI-ZXZARUISSA-N erythritol Chemical compound OC[C@H](O)[C@H](O)CO UNXHWFMMPAWVPI-ZXZARUISSA-N 0.000 description 1
- 229940009714 erythritol Drugs 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000035784 germination Effects 0.000 description 1
- 239000003102 growth factor Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229960000367 inositol Drugs 0.000 description 1
- CDAISMWEOUEBRE-GPIVLXJGSA-N inositol Chemical compound O[C@H]1[C@H](O)[C@@H](O)[C@H](O)[C@H](O)[C@@H]1O CDAISMWEOUEBRE-GPIVLXJGSA-N 0.000 description 1
- JYJIGFIDKWBXDU-MNNPPOADSA-N inulin Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)OC[C@]1(OC[C@]2(OC[C@]3(OC[C@]4(OC[C@]5(OC[C@]6(OC[C@]7(OC[C@]8(OC[C@]9(OC[C@]%10(OC[C@]%11(OC[C@]%12(OC[C@]%13(OC[C@]%14(OC[C@]%15(OC[C@]%16(OC[C@]%17(OC[C@]%18(OC[C@]%19(OC[C@]%20(OC[C@]%21(OC[C@]%22(OC[C@]%23(OC[C@]%24(OC[C@]%25(OC[C@]%26(OC[C@]%27(OC[C@]%28(OC[C@]%29(OC[C@]%30(OC[C@]%31(OC[C@]%32(OC[C@]%33(OC[C@]%34(OC[C@]%35(OC[C@]%36(O[C@@H]%37[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O%37)O)[C@H]([C@H](O)[C@@H](CO)O%36)O)[C@H]([C@H](O)[C@@H](CO)O%35)O)[C@H]([C@H](O)[C@@H](CO)O%34)O)[C@H]([C@H](O)[C@@H](CO)O%33)O)[C@H]([C@H](O)[C@@H](CO)O%32)O)[C@H]([C@H](O)[C@@H](CO)O%31)O)[C@H]([C@H](O)[C@@H](CO)O%30)O)[C@H]([C@H](O)[C@@H](CO)O%29)O)[C@H]([C@H](O)[C@@H](CO)O%28)O)[C@H]([C@H](O)[C@@H](CO)O%27)O)[C@H]([C@H](O)[C@@H](CO)O%26)O)[C@H]([C@H](O)[C@@H](CO)O%25)O)[C@H]([C@H](O)[C@@H](CO)O%24)O)[C@H]([C@H](O)[C@@H](CO)O%23)O)[C@H]([C@H](O)[C@@H](CO)O%22)O)[C@H]([C@H](O)[C@@H](CO)O%21)O)[C@H]([C@H](O)[C@@H](CO)O%20)O)[C@H]([C@H](O)[C@@H](CO)O%19)O)[C@H]([C@H](O)[C@@H](CO)O%18)O)[C@H]([C@H](O)[C@@H](CO)O%17)O)[C@H]([C@H](O)[C@@H](CO)O%16)O)[C@H]([C@H](O)[C@@H](CO)O%15)O)[C@H]([C@H](O)[C@@H](CO)O%14)O)[C@H]([C@H](O)[C@@H](CO)O%13)O)[C@H]([C@H](O)[C@@H](CO)O%12)O)[C@H]([C@H](O)[C@@H](CO)O%11)O)[C@H]([C@H](O)[C@@H](CO)O%10)O)[C@H]([C@H](O)[C@@H](CO)O9)O)[C@H]([C@H](O)[C@@H](CO)O8)O)[C@H]([C@H](O)[C@@H](CO)O7)O)[C@H]([C@H](O)[C@@H](CO)O6)O)[C@H]([C@H](O)[C@@H](CO)O5)O)[C@H]([C@H](O)[C@@H](CO)O4)O)[C@H]([C@H](O)[C@@H](CO)O3)O)[C@H]([C@H](O)[C@@H](CO)O2)O)[C@@H](O)[C@H](O)[C@@H](CO)O1 JYJIGFIDKWBXDU-MNNPPOADSA-N 0.000 description 1
- 229940029339 inulin Drugs 0.000 description 1
- SURQXAFEQWPFPV-UHFFFAOYSA-L iron(2+) sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Fe+2].[O-]S([O-])(=O)=O SURQXAFEQWPFPV-UHFFFAOYSA-L 0.000 description 1
- 238000009630 liquid culture Methods 0.000 description 1
- 229910000357 manganese(II) sulfate Inorganic materials 0.000 description 1
- 235000010355 mannitol Nutrition 0.000 description 1
- QWIZNVHXZXRPDR-WSCXOGSTSA-N melezitose Chemical compound O([C@@]1(O[C@@H]([C@H]([C@@H]1O[C@@H]1[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O1)O)O)CO)CO)[C@H]1O[C@H](CO)[C@@H](O)[C@H](O)[C@H]1O QWIZNVHXZXRPDR-WSCXOGSTSA-N 0.000 description 1
- HEBKCHPVOIAQTA-UHFFFAOYSA-N meso ribitol Natural products OCC(O)C(O)C(O)CO HEBKCHPVOIAQTA-UHFFFAOYSA-N 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 235000013379 molasses Nutrition 0.000 description 1
- 230000000877 morphologic effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 108020001775 protein parts Proteins 0.000 description 1
- MUPFEKGTMRGPLJ-ZQSKZDJDSA-N raffinose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO[C@@H]2[C@@H]([C@@H](O)[C@@H](O)[C@@H](CO)O2)O)O1 MUPFEKGTMRGPLJ-ZQSKZDJDSA-N 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- HEBKCHPVOIAQTA-ZXFHETKHSA-N ribitol Chemical compound OC[C@H](O)[C@H](O)[C@H](O)CO HEBKCHPVOIAQTA-ZXFHETKHSA-N 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- CDAISMWEOUEBRE-UHFFFAOYSA-N scyllo-inosotol Natural products OC1C(O)C(O)C(O)C(O)C1O CDAISMWEOUEBRE-UHFFFAOYSA-N 0.000 description 1
- 235000010356 sorbitol Nutrition 0.000 description 1
- 229960002920 sorbitol Drugs 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 150000003722 vitamin derivatives Chemical class 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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
- C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
- C12N1/32—Processes using, or culture media containing, lower alkanols, i.e. C1 to C6
-
- 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
- C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
- C12N1/14—Fungi; Culture media therefor
- C12N1/16—Yeasts; Culture media therefor
- C12N1/165—Yeast isolates
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
- C12R2001/00—Microorganisms ; Processes using microorganisms
- C12R2001/645—Fungi ; Processes using fungi
- C12R2001/72—Candida
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Biotechnology (AREA)
- Organic Chemistry (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Microbiology (AREA)
- General Engineering & Computer Science (AREA)
- Mycology (AREA)
- Medicinal Chemistry (AREA)
- Virology (AREA)
- Tropical Medicine & Parasitology (AREA)
- Biochemistry (AREA)
- Biomedical Technology (AREA)
- General Health & Medical Sciences (AREA)
- Botany (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Fodder In General (AREA)
Description
(19) DANMARK (W)(19) DENMARK (W)
|j| (12) FREMLÆGGELSESSKRIFT an 143765 B| J | (12) PUBLICATION NOTICE and 143765 B
DIREKTORATET FOR PATENT- OG VAREMÆRKEVÆSENETDIRECTORATE OF THE PATENT AND TRADEMARKET SYSTEM
(21) Ansøgning nr. 5604/77 (51) |nt.CI.3 C 12 N 1/32 (22) Indleveringsdag 15· dec. 1977 (24) Løbedag 15· dec. 1977 (41) Aim. tilgængelig 24. jun. 1978 (44) Fremlagt 5 · Okt. 1 g8l (86) International ansøgning nr. “ (86) International indleveringsdag (85) Videreførelsesdag “ (62) Stamansøgning nr. “(21) Application No. 5604/77 (51) | nt.CI.3 C 12 N 1/32 (22) Filing Day 15 · Dec. 1977 (24) Race day 15 · dec. 1977 (41) Aim. available Jun 24 1978 (44) Presented 5 · Oct. 1 g8l (86) International application no. "(86) International filing day (85) Transfer day" (62) Master application no. "
(30) Prioritet 23· dec. 1976, 30798/76, IT(30) Priority 23 · Dec. 1976, 30798/76, IT
(71) Ansøger SNAMPROGETTI S.P.A., Milano, IT.(71) Applicant SNAMPROGETTI S.P.A., Milan, IT.
(72) Opfinder Pasquale Zaffaroni, IT: Antonio _Senni, IT: Paolo(72) Inventor Pasquale Zaffaroni, IT: Antonio _Senni, IT: Paolo
Branduzzi, IT: Lamterto Formiconi, IT.Branduzzi, IT: Lamterto Formiconi, IT.
(74) Fuldmægtig Internationalt Patent-Bureau.(74) International Patent Bureau.
(54) Fremgangsmåde til fremstilling af gærcellemasse med højt protein» indhold.(54) Process for producing high protein yeast cell mass.
Opfindelsen angår en fremgangsmåde til fremstilling af gærcellemasse med højt proteinindhold ved dyrkning af en stamme af slægten Candida på et dyrkningsmedium, der omfatter en saltopløsning indeholdende methanol som eneste carbon- og energikilde, ved en temperatur fra 20°C til 35°C og en pH-værdi mellem 2,5 og 6,5.The invention relates to a process for producing high protein yeast cell mass by growing a strain of the genus Candida on a culture medium comprising a salt solution containing methanol as the sole carbon and energy source, at a temperature from 20 ° C to 35 ° C and a pH value between 2.5 and 6.5.
På grund af mikroorganismernes store reproduktionshastighed og deres proteinindhold, er produktionen af mikrobielle biomasser n ^ en meget hurtig proteinproducerende metode.Due to the high rate of reproduction of the microorganisms and their protein content, the production of microbial biomasses is a very fast protein producing method.
<£) Til fremstillingen af biomasser er der hidtil blevet anvendt ^ affaldskulhydrater som f.eks. melasse fra sukkerfabrikker eller -d" anvendt sulfitkogevæsker fra papirmøller.<£) For the production of biomasses, waste carbohydrates such as e.g. molasses from sugar mills or -d "used sulphite cooking liquids from paper mills.
T“T "
For nylig har man på grund af jordoliers lettilgængelighed *Recently, due to the availability of petroleum *
2 1Λ3765 og lave pris tilpasset biomasseproduktionsmetoder, der som substrat enten anvender de rå fraktioner af jordolie eller højt rensede blandinger af normale paraffiner.2 1Λ3765 and low cost adapted to biomass production methods using as substrate either the crude fractions of petroleum or highly purified mixtures of normal paraffins.
Anvendelsen af sådan jordoliebaserede substrater udviser nogle få mangler fra et teknologisk standpunkt, hvilket skyldes deres uopløselighed i vand, den betydelige mængde af oxygen, der kræves til deres assimilering af mikroorganismer og den store varme-dannelse under forgæringen. Yderligere forøges de løbende omkostninger ved fremstillingen af biomasser, fordi det er nødvendigt at rense substratet grundigt og/eller omhyggeligt at vaske den således producerede biomasse for at fjerne potentielle skadelige jordolie-komponenter.The use of such petroleum-based substrates exhibits a few shortcomings from a technological standpoint, due to their insolubility in water, the considerable amount of oxygen required for their assimilation of microorganisms and the high heat generation during fermentation. Further, the ongoing cost of biomass production is increased because it is necessary to thoroughly and thoroughly clean the substrate to wash the biomass thus produced to remove potential harmful petroleum components.
Sådanne vanskeligheder ses ikke, dersom produktionen af biomasserne udføres ved at anvende de lavere alkoholer som methanol eller ethanol som substrat. Det er faktisk muligt på grund af deres fuldstændige opløselighed i vand, deres flygtighed,og at de er tilgængelige i så stor renhed at opnå en biomasse, hvor der ikke findes de uønskede rester. Blandbarheden med vand løser blandingsproblemerne, der findes med jordoliefraktionerne, medens oxygenbehovet, fordi de allerede indeholder oxygen i deres molekyler, reduceres ved deres assimilering: derfor får man en yderligere fordel, som består i, at produktionen af biomassen er ledsaget af en mindre varmedannelse, hvorved resultatet bliver en reduktion af køleomkostningerne.Such difficulties are not seen if the production of the biomasses is carried out using the lower alcohols such as methanol or ethanol as a substrate. Indeed, because of their complete solubility in water, their volatility, and their availability in such purity, it is possible to obtain a biomass where the undesirable residues are not found. The miscibility with water solves the mixing problems that exist with the petroleum fractions, while the oxygen demand, because they already contain oxygen in their molecules, is reduced by their assimilation: therefore, there is an additional advantage that the production of the biomass is accompanied by less heat generation, thereby reducing the cost of cooling.
Ethanol anvendes af et stort antal mikroorganismer og vil være det idelle substrat til fremstillingen af biomasser, men prisen herfor er forholdsvis høj. Derimod kan methanol fremstilles billigt og med høj renhed. Dette er grunden til de anstrengelser, man har gjort sig for at finde mikroorganismer, der er i stand til effektivt at udnytte methanol. I den tekniske litteratur og i patentlitteraturen er beskrevet mange bakterier, der er i stand til at opfylde disse krav, medens virkningsgraden af de gærarter, der er beskrevet, hidtil har været temmelig lav. De foran omtalte ulemper undgås ved fremgangsmåden ifølge den foreliggende opfindelse, som er af den kendte art, ved hvilken man dyrker en stamme af slægten Candida på et dyrkningsmedium, der omfatter en saltopløsning indeholdende methanol som eneste carbon- og energikilde, ved en temperatur fra 20°C til 35°C og en pH-værdi mellem 2,5 og 6,5. Fremgangsmåden er ejendommelig ved, at der som stamme af slægten Candida anvendes den hidtil ukendte stamme NRRL-Y 11062 (SP M 180 cc). Derved opnås en gærcellemasse med stort proteinindhold, der kan 143765 3 indgå som proteindelen i animalske foderstoffer eller hvoraf der kan udvindes ædlere produkter såsom proteiner, aminosyrer eller nucleinsyrer.Ethanol is used by a large number of microorganisms and will be the ideal substrate for biomass production, but the cost is relatively high. In contrast, methanol can be produced cheaply and with high purity. This is why efforts have been made to find microorganisms capable of efficiently utilizing methanol. In the technical literature and patent literature, many bacteria capable of meeting these requirements have been described, while the efficacy of the yeast species described has so far been rather low. The foregoing disadvantages are avoided by the method of the present invention, which is of the prior art in which a strain of the genus Candida is grown on a culture medium comprising a saline solution containing methanol as the sole carbon and energy source, at a temperature of 20 ° C to 35 ° C and a pH between 2.5 and 6.5. The process is characterized in that as the strain of the genus Candida the new strain NRRL-Y 11062 (SP M 180 cc) is used. Thereby a high protein yeast cell mass can be obtained which can be included as the protein part in animal feed or from which more noble products such as proteins, amino acids or nucleic acids can be recovered.
Den omhandlede stamme er den 6. januar 1977 blevet deponeret i Northern Regional Research Laboratory, Peoria, Illinois, USA, under betegnelsen NRRL-Y 11062.The strain in question was deposited on January 6, 1977, in the Northern Regional Research Laboratory, Peoria, Illinois, USA, under the designation NRRL-Y 11062.
Den hidtil ukendte stammes karakteristika beskrives i det følgende.The characteristics of the novel strain are described below.
Stammen SP M 180 cc reproduceres ved multipolar udspiring og danner adskilte ægformede celler eller klatter, der består af et antal aflange celler (pseudomycelium).The SP M 180 cc strain is reproduced by multipolar germination, forming separate egg-shaped cells or clumps consisting of a plurality of elongated cells (pseudomycelium).
I flydende dyrkningsmedier danner den bundfald, medens den i fast medium danner enten glatte og skinnende kolonier, eller uigennemsigtige og rynkede kolonier. Når man dyrker stammen på et fast medium, bliver stammen mere og mere glat og skinnende, hvilket i et flydende medium svarer til de adskilte celler, medens når man dyrker stammen i et flydende medium under visse betingelser, dominerer den pseudomyceliære form, hvilket svarer til de rynkede og uigennemsigtige celler. Man har aldrig set sporer af nogen art.In liquid culture media, it forms a precipitate, while in solid medium it forms either smooth and shiny colonies, or opaque and wrinkled colonies. When growing the strain on a solid medium, the strain becomes more and more smooth and shiny, which in a liquid medium corresponds to the separated cells, whereas when cultured in a liquid medium under certain conditions, the pseudomycelial form predominates, corresponding to the wrinkled and opaque cells. No traces of any kind have ever been seen.
Ud fra sådanne morphologiske karakteristika, antager man, at stammen hører til arten Candida ifølge den klassifikation, der er foreslået af J. Lodder, The Yeasts : a taxonomic Study, 1970.Based on such morphological characteristics, it is assumed that the strain belongs to the species Candida according to the classification proposed by J. Lodder, The Yeasts: a taxonomic Study, 1970.
De fysiologisk karakteristika af stammen SP M 18 cc er følgende: 1. Forgæringsudnyttelse af nogle få carbonkilder: D-glucose + D-galactoseThe physiological characteristics of the strain SP M 18 cc are as follows: 1. Fermentation utilization of a few carbon sources: D-glucose + D-galactose
Saccharosesucrose
Maltosemaltose
TrealoseTrealose
Lactose 2. Vækst: D-glucose + D-galactose 1-sorboseLactose 2. Growth: D-glucose + D-galactose 1-sorbose
Saccharosesucrose
Maltosemaltose
Cellobiose +Cellobiose +
TrealoseTrealose
Lactose , 143765 4Lactose, 143765 4
Melibiosemelibiose
Raffinoseraffinose
Melezitosemelezitose
Inulin -Inulin -
Stivelse D-xylose + 1-Arabinose + D-Arabinose - D-Ribose + (svag) 1-Rhamnose -Starch D-xylose + 1-arabinose + D-arabinose - D-Ribose + (weak) 1-Rhamnose -
Ethanol +Ethanol +
Glycerolglycerol
Erythritolerythritol
Ribitol +Ribitol +
Galacticol D-Mannitol + D-Glucitol + Mælkesyre Ravsyre Citronsyre Inositol NitratGalacticol D-Mannitol + D-Glucitol + Lactic Acid Acetic Acid Citric Acid Inositol Nitrate
Ingen vitamin ved 37°C + (svag)No vitamin at 37 ° C + (weak)
En sammenligning af de fysiologiske karakteristika for SP M 180 cc stammen med de karakteristika, der er beskrevet i arbejdet af Lodder citeret ovenfor såvel som sammenlignet med de oplysninger, der er omtalt i bogen "A new Key to the Yeasts", af J. A. Barrett og R. J. Pankhurst, 1974 har vist, at stammen SP M 180 cc er forskellig fra alle de gærarter, der er beskrevet i disse bøger.A comparison of the physiological characteristics of the SP M 180 cc strain with the characteristics described in the work by Lodder quoted above as well as compared with the information discussed in the book "A new Key to the Yeasts" by JA Barrett and RJ Pankhurst, 1974 has shown that the strain SP M 180 cc is different from all the yeast species described in these books.
Den tekniske litteratur og patentlitteraturen har hidtil beskrevet mange gærarter, der er i stand til at anvende methanol (jfr. C. L. Cooney og D. W. Levine i "Single-Cell Protein II - MIT Press, 1975), men karakteristika for stammen SP M 180 cc er forskellig fra alle de hidtil kendte stammer.The technical literature and patent literature have so far described many yeast species capable of using methanol (cf. CL Cooney and DW Levine in "Single-Cell Protein II - MIT Press, 1975), but the characteristics of the strain SP M 180 cc are different from all the known tribes.
En "sui generis" egenskab ved denne stamme er dens evne til at assimilere methanol mere effektivt end ethanol. Stammen kan dyrkes både i diskontinuerte og kontinuerte kulturer, men dens egen- 143765 5 skaber er bedre udnyttet i kontinuerte kulturer.A "sui generis" property of this strain is its ability to assimilate methanol more efficiently than ethanol. The strain can be grown in both discontinuous and continuous cultures, but its properties are better utilized in continuous cultures.
Yderligere kan der opnås en kultur, der meget let falder til bunds, på grund af dens evne til at danne pseudomycelium. En sådan egenskab kan udnyttes til at udføre kontinuert kultur med en partiel biomasse feed back eller recirkulering, en evne der muliggør, at man kan opnå et højere udbytte pr. time. Yderligere muliggør den lette bundfældning,at opsamlingen af biomassen er mere bekvem.Furthermore, a culture that can very easily fall to the ground can be obtained because of its ability to form pseudomycelium. Such a feature can be utilized to perform continuous culture with a partial biomass feed back or recycling, a capability that allows a higher yield per capita to be obtained. hour. Furthermore, the light precipitation allows the collection of the biomass to be more convenient.
I praksis består fremgangsmåden i,at man poder et dyrkningsmedium med stammen SP M 180 cc, idet dyrkningsmediet indeholder de nødvendige grundstoffer (N, P, K, Mg, Fe, Ca), vækstfaktorer (gærekstrakter og biotin), mineralsporstoffer, og methanol som carbon- og energikilde. Builionen dyrkes under omrøring ved en temperatur fra 20°C til 35°C, fortrinsvis mellm 30°C og 33°C, idet pH-værdien holdes mellem 2,5 og 6,5, fortrinsvis mellem 4 og 4,5, idet man tilfører en kontinuert mængde af en gasblanding, der indeholder oxygen, som f.eks. luft.In practice, the process consists of inoculating a culture medium with strain SP M 180 cc, the culture medium containing the necessary elements (N, P, K, Mg, Fe, Ca), growth factors (yeast extracts and biotin), mineral trace elements, and methanol as carbon and energy source. The builion is grown with stirring at a temperature from 20 ° C to 35 ° C, preferably between 30 ° C and 33 ° C, maintaining the pH between 2.5 and 6.5, preferably between 4 and 4.5, supplies a continuous amount of a gas mixture containing oxygen, e.g. air.
Gærcellerne, der formerer sig på bekostning af næringsmidlerne, der tilføres, opsamles ved bundfalching og filtrering, vaskes med vand og tørres ved opvarmning.The yeast cells, which multiply at the expense of the nutrients being supplied, are collected by bottom phaling and filtration, washed with water and dried by heating.
Den således opnåede biomasse kan anvendes som proteindelen af animalske foderstoffer, eller man kan ekstrahere ædlere produkter fra det såsom proteiner, aminosyrer og nucleinsyrer.The biomass thus obtained can be used as the protein portion of animal feed, or more noble products may be extracted from it such as proteins, amino acids and nucleic acids.
Nærværende patent omfatter ikke fremgangsmådens anvendelse ved tilvirkning af næringsmidler.The present patent does not cover the use of the process in the manufacture of foodstuffs.
Opfindelsen belyses nærmere nedenfor ved følgende eksempler.The invention is further illustrated below by the following examples.
Eksempel 1Example 1
Der anvendtes 500 ml Erlenmeyer-kolber, der hver indeholdt 50 ml af et dyrkningsmedium med følgende sammensætning: KH2P04 2,0 g pr. liter500 ml Erlenmeyer flasks were used, each containing 50 ml of a culture medium of the following composition: KH 2 PO 4 2.0 g / ml liter
NaH2P04.H20 2,0 " (NH4)2S04 5,0 "2.0 "(NH 4) 2 SO 4 5.0"
MgS04.7H20 0,2 "MgS04.7H20 0.2 "
FeS04.7H20 2,0 mg pr. literFeSO4.7H2O 2.0 mg per liter
CaCl3 2,0 "CaCl3 2.0 "
ZnS04.7H20 2,0 " Gærekstrakt 200,0 "2.0 "Yeast Extract 200.0"
Biotin 25,0 mikrogram pr. literBiotin 25.0 micrograms per liter
Sporstoffer (opløsning) 1 ml pr. liter c 143765 6Tracers (solution) 1 ml. liter c 143765 6
Opløsningen af sporstofferne er fremstillet i fortyndet HC1 (1 ml koncentreret HC1 i 1 liter vand) og havde følgende sammensætning:The solution of the trace elements was prepared in dilute HCl (1 ml of concentrated HCl in 1 liter of water) and had the following composition:
CuS04.5H20 200 mg pr. liter H3B03 500 "CuS04.5H20 200 mg per liter H3B03 500 "
MnS04.H20 500 "MnS04.H20 500 "
Kl 10 "10 o clock "
CoC12,6H20 10 "CoC12.6H20 10 "
Mo03 10 "Mo03 10 "
Substratets pH indstilledes på 5,0, og kolben steriliseredes ved 116°C i 20 minutter. Til to kolber sattes der 0,75 ml (1,9% vol/vol) methanol, og kolberne tilsåedes med en skråpodning af stammen SP M 180 cc. Kolberne dyrkedes i 72 timer på en roterende anordning (220 omdr. pr. minut, idet bevægelsens diameter var 3,5 cm), og en temperatur på 32,5°C, der kontrolleredes termostatisk.The pH of the substrate was adjusted to 5.0 and the flask sterilized at 116 ° C for 20 minutes. To two flasks, 0.75 ml (1.9% v / v) of methanol was added and the flasks were sown with a bevel graft of strain SP M 180 cc. The flasks were grown for 72 hours on a rotary device (220 rpm, with the movement diameter 3.5 cm) and a temperature of 32.5 ° C, thermostatically controlled.
Andre kolber, der indeholdt det samme medium,og til hvilke der var sat 1% (vol/vol) methanol, 2% (vol/vol) ethanol og 2% vægt/vol) glucose tilsåedes med 5 ml af den ovenfor beskrevne forkultur. Efter 24 timers dyrkning tilsattes yderligere 1% vol/vol methanol til hver kolbe. Efter ialt 48 timers dyrkning måltes indholdet af biomasse i kolberne, idet resultaterne var følgende:Other flasks containing the same medium to which 1% (v / v) methanol, 2% (v / v) ethanol and 2% w / v glucose were added were added with 5 ml of the preculture described above. After 24 hours of culture, an additional 1% v / v methanol was added to each flask. After a total of 48 hours of culture, the contents of biomass in the flasks were measured, the results being as follows:
Substrat Optisk tæthed Tør biomasse _ (1:10) ved 660 nm g/liter ProteinerSubstrate Optical density Dry biomass _ (1:10) at 660 nm g / liter Proteins
Glucose 0,340 3,99 54,5Glucose 0.340 3.99 54.5
Methanol 0,270 3,68 51,0Methanol 0.270 3.68 51.0
Ethanol 0,095 1,18 54,1Ethanol 0.095 1.18 54.1
Proteinindholdet bestemtes ved biuret-prøven.The protein content was determined by the biuret sample.
Eksempel 2Example 2
En forgæringsbeholder, der havde et effektivt rumfang på ca. 8 liter, og som indeholdt dyrkningsmediet fra eksempel 1 podedes med en suspension af stammen SP M 180 cc. Til forgæringsbeholderen, der var kontrolleret termostatisk på 32,5°C, sattes methanol, idet man sikrede sig at restkoncentrationen i builionen aldrig oversteg 1% vol/vol. Når kulturen var groet tilfredsstillende, påbegyndtes den kontinuerte tilsætning af steril builion til forgæringsbeholderen , idet den sterile builion indeholdt 29,6 g methanol pr. liter, medens en del af buillonkulturen samtidig fjernedes, svarende til den mængde, der blev sat til dyrkningssubstratet. Mængden af tilsatA fermentation vessel that had an effective volume of approx. 8 liters and containing the culture medium of Example 1 were seeded with a suspension of strain SP M 180 cc. To the fermentation vessel, which was thermostatically controlled at 32.5 ° C, was added methanol, ensuring that the residual concentration in the builion never exceeded 1% v / v. When the culture had grown satisfactorily, the continuous addition of sterile builion to the fermentation vessel began, with the sterile builion containing 29.6 g of methanol per ml. liters, while at the same time removing part of the buillon culture, corresponding to the amount added to the culture substrate. The amount of added
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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IT3079876 | 1976-12-23 | ||
IT30798/76A IT1123648B (en) | 1976-12-23 | 1976-12-23 | PROCEDURE FOR THE PRODUCTION OF HIGH PROTEIN CONTENT AND MEANS SUITABLE FOR THE PURPOSE |
Publications (3)
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DK560477A DK560477A (en) | 1978-06-24 |
DK143765B true DK143765B (en) | 1981-10-05 |
DK143765C DK143765C (en) | 1982-03-22 |
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DK560477A DK143765C (en) | 1976-12-23 | 1977-12-15 | METHOD FOR PRODUCING YEAR CELL MASS WITH HIGH PROTEIN CONTENT |
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JP (1) | JPS5379089A (en) |
AU (1) | AU517658B2 (en) |
BE (1) | BE862291A (en) |
CA (1) | CA1106786A (en) |
CH (1) | CH631054A5 (en) |
CS (1) | CS214802B2 (en) |
DD (1) | DD137120A5 (en) |
DE (1) | DE2757877C3 (en) |
DK (1) | DK143765C (en) |
FR (1) | FR2375322A1 (en) |
GB (1) | GB1578200A (en) |
HU (1) | HU178342B (en) |
IT (1) | IT1123648B (en) |
LU (1) | LU78772A1 (en) |
NL (1) | NL7714383A (en) |
NO (1) | NO146207C (en) |
SE (1) | SE7714710L (en) |
SU (1) | SU759055A3 (en) |
YU (1) | YU307077A (en) |
ZA (1) | ZA777212B (en) |
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1976
- 1976-12-23 IT IT30798/76A patent/IT1123648B/en active
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1977
- 1977-12-05 ZA ZA00777212A patent/ZA777212B/en unknown
- 1977-12-08 CA CA292,704A patent/CA1106786A/en not_active Expired
- 1977-12-08 AU AU31346/77A patent/AU517658B2/en not_active Expired
- 1977-12-14 CH CH1538377A patent/CH631054A5/en not_active IP Right Cessation
- 1977-12-15 DK DK560477A patent/DK143765C/en not_active IP Right Cessation
- 1977-12-22 HU HU77SA3085A patent/HU178342B/en unknown
- 1977-12-23 BE BE183819A patent/BE862291A/en not_active IP Right Cessation
- 1977-12-23 NL NL7714383A patent/NL7714383A/en not_active Application Discontinuation
- 1977-12-23 SE SE7714710A patent/SE7714710L/en not_active Application Discontinuation
- 1977-12-23 JP JP15460677A patent/JPS5379089A/en active Pending
- 1977-12-23 SU SU772558413A patent/SU759055A3/en active
- 1977-12-23 GB GB53855/77A patent/GB1578200A/en not_active Expired
- 1977-12-23 NO NO774441A patent/NO146207C/en unknown
- 1977-12-23 YU YU03070/77A patent/YU307077A/en unknown
- 1977-12-23 CS CS778778A patent/CS214802B2/en unknown
- 1977-12-23 DE DE2757877A patent/DE2757877C3/en not_active Expired
- 1977-12-23 LU LU78772A patent/LU78772A1/xx unknown
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DK560477A (en) | 1978-06-24 |
FR2375322B1 (en) | 1980-06-06 |
SE7714710L (en) | 1978-06-24 |
DE2757877C3 (en) | 1980-01-17 |
SU759055A3 (en) | 1980-08-23 |
CS214802B2 (en) | 1982-06-25 |
CA1106786A (en) | 1981-08-11 |
ZA777212B (en) | 1978-10-25 |
GB1578200A (en) | 1980-11-05 |
NO146207C (en) | 1982-08-18 |
BE862291A (en) | 1978-06-23 |
NL7714383A (en) | 1978-06-27 |
AU517658B2 (en) | 1981-08-20 |
CH631054A5 (en) | 1982-07-30 |
DE2757877B2 (en) | 1979-05-23 |
DD137120A5 (en) | 1979-08-15 |
YU307077A (en) | 1983-04-30 |
DK143765C (en) | 1982-03-22 |
NO774441L (en) | 1978-06-26 |
HU178342B (en) | 1982-04-28 |
JPS5379089A (en) | 1978-07-13 |
DE2757877A1 (en) | 1978-06-29 |
LU78772A1 (en) | 1978-04-17 |
FR2375322A1 (en) | 1978-07-21 |
IT1123648B (en) | 1986-04-30 |
NO146207B (en) | 1982-05-10 |
AU3134677A (en) | 1979-06-14 |
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