GB2036076A - Genetic Process for the Production of Antibiotic Producing Micromonospora strains - Google Patents
Genetic Process for the Production of Antibiotic Producing Micromonospora strains Download PDFInfo
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- GB2036076A GB2036076A GB7938689A GB7938689A GB2036076A GB 2036076 A GB2036076 A GB 2036076A GB 7938689 A GB7938689 A GB 7938689A GB 7938689 A GB7938689 A GB 7938689A GB 2036076 A GB2036076 A GB 2036076A
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- micromonospora
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- gentamicin
- strains
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- 238000000034 method Methods 0.000 title claims abstract description 38
- 230000008569 process Effects 0.000 title claims abstract description 25
- 241000187708 Micromonospora Species 0.000 title claims abstract description 20
- 230000002068 genetic effect Effects 0.000 title claims description 12
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 230000003115 biocidal effect Effects 0.000 title description 11
- 210000001938 protoplast Anatomy 0.000 claims abstract description 49
- 239000000725 suspension Substances 0.000 claims abstract description 30
- 229920001817 Agar Polymers 0.000 claims abstract description 18
- DHMQDGOQFOQNFH-UHFFFAOYSA-N Glycine Chemical compound NCC(O)=O DHMQDGOQFOQNFH-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000008272 agar Substances 0.000 claims abstract description 18
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 18
- 102000004169 proteins and genes Human genes 0.000 claims abstract description 15
- 102000016943 Muramidase Human genes 0.000 claims abstract description 12
- 108010014251 Muramidase Proteins 0.000 claims abstract description 12
- 108010062010 N-Acetylmuramoyl-L-alanine Amidase Proteins 0.000 claims abstract description 12
- 229930006000 Sucrose Natural products 0.000 claims abstract description 12
- 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 claims abstract description 12
- 229960000274 lysozyme Drugs 0.000 claims abstract description 12
- 235000010335 lysozyme Nutrition 0.000 claims abstract description 12
- 239000004325 lysozyme Substances 0.000 claims abstract description 12
- 239000005720 sucrose Substances 0.000 claims abstract description 12
- ONIBWKKTOPOVIA-UHFFFAOYSA-N Proline Chemical compound OC(=O)C1CCCN1 ONIBWKKTOPOVIA-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000004471 Glycine Substances 0.000 claims abstract description 9
- 239000002202 Polyethylene glycol Substances 0.000 claims abstract description 7
- 229920001223 polyethylene glycol Polymers 0.000 claims abstract description 7
- 150000003839 salts Chemical class 0.000 claims abstract description 4
- 241000187722 Micromonospora echinospora Species 0.000 claims description 15
- 241000218919 Micromonospora inyonensis Species 0.000 claims description 8
- 241000894007 species Species 0.000 claims description 5
- 230000003698 anagen phase Effects 0.000 claims 1
- 238000007747 plating Methods 0.000 claims 1
- 238000002360 preparation method Methods 0.000 abstract description 4
- 239000002609 medium Substances 0.000 description 38
- UCSJYZPVAKXKNQ-HZYVHMACSA-N streptomycin Chemical compound CN[C@H]1[C@H](O)[C@@H](O)[C@H](CO)O[C@H]1O[C@@H]1[C@](C=O)(O)[C@H](C)O[C@H]1O[C@@H]1[C@@H](NC(N)=N)[C@H](O)[C@@H](NC(N)=N)[C@H](O)[C@H]1O UCSJYZPVAKXKNQ-HZYVHMACSA-N 0.000 description 36
- 229960005322 streptomycin Drugs 0.000 description 18
- 230000004927 fusion Effects 0.000 description 17
- 239000002253 acid Substances 0.000 description 15
- 239000000203 mixture Substances 0.000 description 13
- 230000001419 dependent effect Effects 0.000 description 10
- 239000012153 distilled water Substances 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- JQXXHWHPUNPDRT-WLSIYKJHSA-N rifampicin Chemical compound O([C@](C1=O)(C)O/C=C/[C@@H]([C@H]([C@@H](OC(C)=O)[C@H](C)[C@H](O)[C@H](C)[C@@H](O)[C@@H](C)\C=C\C=C(C)/C(=O)NC=2C(O)=C3C([O-])=C4C)C)OC)C4=C1C3=C(O)C=2\C=N\N1CC[NH+](C)CC1 JQXXHWHPUNPDRT-WLSIYKJHSA-N 0.000 description 8
- 229960001225 rifampicin Drugs 0.000 description 8
- 238000005215 recombination Methods 0.000 description 7
- 230000006798 recombination Effects 0.000 description 7
- 239000007983 Tris buffer Substances 0.000 description 6
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 6
- 235000013619 trace mineral Nutrition 0.000 description 6
- 239000011573 trace mineral Substances 0.000 description 6
- 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 5
- ZPWVASYFFYYZEW-UHFFFAOYSA-L dipotassium hydrogen phosphate Chemical compound [K+].[K+].OP([O-])([O-])=O ZPWVASYFFYYZEW-UHFFFAOYSA-L 0.000 description 5
- 229910000396 dipotassium phosphate Inorganic materials 0.000 description 5
- 235000019797 dipotassium phosphate Nutrition 0.000 description 5
- 239000008103 glucose Substances 0.000 description 5
- 230000008929 regeneration Effects 0.000 description 5
- 238000011069 regeneration method Methods 0.000 description 5
- 239000007836 KH2PO4 Substances 0.000 description 4
- 229940041514 candida albicans extract Drugs 0.000 description 4
- 230000004545 gene duplication Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 4
- 235000019796 monopotassium phosphate Nutrition 0.000 description 4
- GNSKLFRGEWLPPA-UHFFFAOYSA-M potassium dihydrogen phosphate Chemical compound [K+].OP(O)([O-])=O GNSKLFRGEWLPPA-UHFFFAOYSA-M 0.000 description 4
- 229910052939 potassium sulfate Inorganic materials 0.000 description 4
- 239000012138 yeast extract Substances 0.000 description 4
- 239000003242 anti bacterial agent Substances 0.000 description 3
- 229940088710 antibiotic agent Drugs 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000000872 buffer Substances 0.000 description 3
- 210000004027 cell Anatomy 0.000 description 3
- WRUGWIBCXHJTDG-UHFFFAOYSA-L magnesium sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Mg+2].[O-]S([O-])(=O)=O WRUGWIBCXHJTDG-UHFFFAOYSA-L 0.000 description 3
- 230000035772 mutation Effects 0.000 description 3
- 235000010333 potassium nitrate Nutrition 0.000 description 3
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- 230000003190 augmentative effect Effects 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- 210000002421 cell wall Anatomy 0.000 description 2
- 210000000349 chromosome Anatomy 0.000 description 2
- 210000000805 cytoplasm Anatomy 0.000 description 2
- 229940088598 enzyme Drugs 0.000 description 2
- 238000011081 inoculation Methods 0.000 description 2
- 239000003471 mutagenic agent Substances 0.000 description 2
- 238000007500 overflow downdraw method Methods 0.000 description 2
- QKNYBSVHEMOAJP-UHFFFAOYSA-N 2-amino-2-(hydroxymethyl)propane-1,3-diol;hydron;chloride Chemical compound Cl.OCC(N)(CO)CO QKNYBSVHEMOAJP-UHFFFAOYSA-N 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 229930182566 Gentamicin Natural products 0.000 description 1
- CEAZRRDELHUEMR-URQXQFDESA-N Gentamicin Chemical compound O1[C@H](C(C)NC)CC[C@@H](N)[C@H]1O[C@H]1[C@H](O)[C@@H](O[C@@H]2[C@@H]([C@@H](NC)[C@@](C)(O)CO2)O)[C@H](N)C[C@@H]1N CEAZRRDELHUEMR-URQXQFDESA-N 0.000 description 1
- ONIBWKKTOPOVIA-BYPYZUCNSA-N L-Proline Chemical compound OC(=O)[C@@H]1CCCN1 ONIBWKKTOPOVIA-BYPYZUCNSA-N 0.000 description 1
- 239000001888 Peptone Substances 0.000 description 1
- 108010080698 Peptones Proteins 0.000 description 1
- 241000191963 Staphylococcus epidermidis Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 241001655322 Streptomycetales Species 0.000 description 1
- 238000012459 agar diffusion assay Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 235000010216 calcium carbonate Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000009089 cytolysis Effects 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 238000007499 fusion processing Methods 0.000 description 1
- 229960002518 gentamicin Drugs 0.000 description 1
- 239000001963 growth medium Substances 0.000 description 1
- 125000004029 hydroxymethyl group Chemical group [H]OC([H])([H])* 0.000 description 1
- 230000000415 inactivating effect Effects 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 238000011534 incubation Methods 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 231100000219 mutagenic Toxicity 0.000 description 1
- 230000003505 mutagenic effect Effects 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- 230000004260 plant-type cell wall biogenesis Effects 0.000 description 1
- 229920001592 potato starch Polymers 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 230000035899 viability Effects 0.000 description 1
Classifications
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- 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
- C12N15/00—Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
- C12N15/02—Preparation of hybrid cells by fusion of two or more cells, e.g. protoplast fusion
- C12N15/03—Bacteria
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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- 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
- C12N1/20—Bacteria; Culture media therefor
- C12N1/205—Bacterial isolates
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- 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
- C12P19/44—Preparation of O-glycosides, e.g. glucosides
- C12P19/46—Preparation of O-glycosides, e.g. glucosides having an oxygen atom of the saccharide radical bound to a cyclohexyl radical, e.g. kasugamycin
- C12P19/48—Preparation of O-glycosides, e.g. glucosides having an oxygen atom of the saccharide radical bound to a cyclohexyl radical, e.g. kasugamycin the cyclohexyl radical being substituted by two or more nitrogen atoms, e.g. destomycin, neamin
- C12P19/485—Having two saccharide radicals bound through only oxygen to non-adjacent ring carbons of the cyclohexyl radical, e.g. gentamycin, kanamycin, sisomycin, verdamycin, mutamycin, tobramycin, nebramycin, antibiotics 66-40B, 66-40D, XK-62-2, 66-40, G-418, G-52
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- 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
- C12R2001/01—Bacteria or Actinomycetales ; using bacteria or Actinomycetales
- C12R2001/29—Micromonospora
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Abstract
A process for the preparation of antibiotic-producer Micromonospora strains having modified genetic material, wherein following cultivation in a glycine medium, a protoplast suspension is prepared with lysozyme, under osmotically buffered conditions ensured by sucrose, from each culture of two mutants of the antibiotic- producer Micromonospora, at least one of which is genetically labelled, the two suspensions obtained are combined in the present of polyethylene glycol, and incubated at room temperature. The resulting fused protoplasts are suspended in soft agar, then plated on an agar plate containing prolin and inorganic salts, incubated for 20 to 30 days, and finally all mutants are selected from the regenerated colonies which are sure to have genetic material different from that of the parent strains.
Description
SPECIFICATION
New Genetic Process for the Preparation of
Antibiotic-producer Micromonospora Strains
The invention relates to a novel process for the preparation of antibiotic-producer
Micromonospora strains having modified genetic material.
It is widely known that antibiotic production is a genetically determined property. Consequently any change induced in the genetic material of a producer strain may alter its antibiotic-producing property, too. These stable genetic changes (mutations) occur also spontaneously, though very rarely. The incidence of mutations may be enhanced by known methods, i.e. UV, near-UV, gamma and x-ray irradiations as well as treatment with different mutagenic agents. These methods have been successfully applied at a variety of strains to enhance their antibiotic-producing capacity. It is a severe drawback of these methods that the mutation induced is a random process, cannot be controlled, and that not all survivors of the mutagenic treatment become mutants. So a large number of survivors has to be screened in order to obtain finally a better producer mutant.
It is known that several enzyme levels are raised by enhancing the gene dose, i.e. if the gene is doubled within a given chromosome, the level of the protein coded by it is doubled, too.
Similarly, the synthesis of antibiotics may be increased by raising the level of enzymes responsible for antibiotic synthesis. The mechanism of gene duplication has not been elucidated yet, nor is it known which of the mutagenic agents is primarily inducing gene duplication.
It can be concluded that any process able to increase significantly the number of gene duplications may be of major importance in augmenting the productivity of antibioticproducer strains.
Considering industrial applications, a new species can be prepared from two
Micromonospora strains producing antibiotics of related structure, which has more advantageous properties both as regards cultivation or yield, or which can produce a novel valuable antibiotic having a similar structure as the antibiotics formed by the parent strains.
The process of protoplast fusion may be the method of choice to solve the above problems.
It is the objective of the present invention to advantageously modify the genetic properties of
Micromonospora strains by means of recombination.
Except for one paper (Beretta et al., J. Bact., 107, 41 5/1971/) no method is described for the genetic information transfer in the
Micromonospora genus having industrial importance. Compared to the incidence of recombinations (10-6) described in
Streptomycetes, in Micromonospora no recombinations could be attained by any of the conventional methods while the protoplast fusion method developed could achieve genetic information transfer with a frequency of 10-3~ 10-4.
In the course of protoplast fusion the entire cytoplasm of two or more protoplasts, consequently their complete genetic material, is unified. The selection performed thereafter furnished either stable merodiploids or recombinants. With merodiploids the number of genes responsible for antibiotic synthesis may be enhanced within the cell even if the selection is not carried out with the objective of augmenting antibiotic production. Gene duplication may occur also in the course of recombination. It is a further advantage of the method that in the course of protoplast fusion large chromosome fragments, transferred from the donor into the recipient, are fixed with a higher incidence in the colonies surviving selection than with any other method applied till now in bacterial genetics.
The protoplast fusion method has been widely applied for studying the genetic properties of both thhal a eplant cells as well as those of fungi.
Due to difficulties in cell wall regeneration the first papers published about bacterial protoplast fusion appeared around 1 976 (K. Fodor and L.
Alföldi, Proc. Natl. Acad. Sci. USA 73, 2147/1976/; P. Schaeffer et al., Proc. Natl. Acad.
Sci. USA 73,2151/y576/; D. A. Hopwood et al.,
Nature 268, 171/1977/; R. H. Baltz, J. Gen.
Microbiol., 107,93/1978/; 0. Godfrey et al., Can.
J. Microbiol., 24, 994/1 978/).
No paper has ever been published about protoplast fusion in the Micromonospora genus.
Accordingly, the present invention provides a process for the preparation of antibiotic-producer
Micromonopora strains having modified genetic material, wherein following cultivation in a glycine medium, a protoplast suspension is prepared with lysozyme, under osmotically buffered conditions ensured by sucrose, from each culture of the two mutants of the antibiotic-producer
Micromonospora, at least one of the mutants being genetically labelled, the two suspensions obtained are combined in the presence of polyethylene glycol, and incubated at room temperature. The resulting fused protoplasts are suspended in soft agar, then plated on an agar plate containing prolin and inorganic salts, incubated for 20 to 30 days, and finally all mutants are selected from the regenerated colonies which are sure to have genetic material different from that of the parent strains.
To promote the lysis of the cell wall by means of lysozyme, glycine (0.2 to 0.5 percent) is preferably added to the culture medium. Due to the inhibiting effect exerted by glycine on cell wall synthesis, it is a common feature of these glycinesensitized cultures that mycelial hyphae are both shorter and thicker compared to those grown in the absence of glycine, and in addition bulges appear on them. Only cultures showing simiiar microscopic picture can yield protoplast suspensions with satisfactory efficacy.
These sensitized cultures are treated for 30 to 90 minutes with lysozyme (5-10 mg/ml) under osmotically buffered conditions (in a medium containing preferably 0.2-0.35 M sucrose).
Combining the individual protoplast suspensions prepared from various mutants at a ratio of 1:1, and treating the mixture with polyethylene glycol (m.w. 6000) the protoplasts undergo fusion. The suspension containing the fused protoplasts is incubated in a regenerating agar under osmotically buffered conditions ensured by sucrose, and proline as well as inorganic salts, preferably CaCI2, MgCI2 and
KH2Po4, promoting regeneration, in a temperature range of 30 to 370C. The protoplasts are regenerated within 20 to 30 days.
The genetic properties of each parent pair chosen should ensure the successful selection of recombinants formed in the course of fusion. For this purpose antibiotic resistance or various auxotrophs may be applied which were already used with success in conventional microbial genetics.
In accordance with the present invention in the case of the sisomicin-producer Micromonospora inyoensis ATCC 27600 a casamino acid dependent but rifampicin resistant, and a casamino acid non-dependent but rifampicin sensitive (sensitive already to 0.5 Mg/ml of rifampicin) parent pair was utilized. Following completed fusion mutants were looked for which are non-dependent to casamino acid for growth but are rifampicin resistant, i.e. are forming colonies in minimal medium containing 10,ug/ml of rifampicin. Regeneration is carried out in nonselective medium ensuring optimal conditions for regeneration. In order to select recombinant phenotypes, the regenerated colonies are washed off, and the suspension obtained is plated onto a minimal medium containing 10yg/ml of rifampicin.The colonies formed from individual cells having recombinant phenotypes are obtained as a result of fusion.
According to a further advantageous method of execution of the process of the invention a novel selecting process is used whereby the protoplasts of one of the parents are inactivated by heat treatment. The heat treatment should be effective enough to ensure loss of viability, at the same time should be mild enough to preserve the genetic material intact. In this case the complete genetic material of one partner is transferred into the heat-inactivated cytoplasm of the other partner. This procedure provides a means for selection when only one of the parents is marked genetically.
This principle was used for the gentamicinproducer Micromonospora purpurea Var.
nigrescens (MNG-National Collection of
Microorganisms, Budapest-00122) strain by applying a streptomycin-resistant-streptomycin- sensitive parent pair. For the selection of recombinants the protoplasts of the resistant parent were carefully heat-inactivated (550C) prior to fusion. As streptomycin sensitivity is a dominant feature over streptomycin resistance, 8 to 10 days have to elapse prior to the selection of recombinants (phenotype lag). After 8 to 10 days 10,000 Jug/ml of streptomycin is layered on the regeneration plates. The genetic material of the colonies formed after 20 to 30 days is different from that of the parent pairs.
Applying heat inactivating techniques and utilizing the fact that Micromonospora purpurea var. nigrescens is more resistant to streptomycin by two orders of magnitude than
Micromonospora inyoensis, the interspecific hybride of the two strains is prepared by protopiast fusion. According to this procedure the protoplast suspension of streptomycin-resistant
Micromonospora purpurea var. nigrescens is heat-inactivated and fused with the protoplast suspension of streptomycin-sensitive
Micromonospora inyoensis. After 8 to 10 days agar containing 1000,ug/ml of streptomycin is layered on the fused protoplasts to be regenerated. The colonies formed after 20 to 30 days are interspecific hybrides.
The above principle was also applied for parent pairs bearing other genetic marking. One parent is casamino-acid dependent while the other is nondependent. For the selection of recombinants the protoplasts of the casamino-acid dependent parent are carefully heat-inactivated. The fused protoplasts are layered on minimal agar. The colonies formed after 20 to 30 days have recombinant properties.
In studies investigating the antibioticproducing property of strains having genetic material modified by the process of the present invention, methods described in the literature are used. Thus for instance, in studying the antibiotic production of recombinants prepared from the gentamicic-producer Micromonospora purpurea var. nigrescens (MNG 00122), the strain is grown at conditions optimized for antibiotic production (I. Gado et al., Hungarian Patent No.
168,778/1973/). The microbiological activity of the fermentation broth is determined by agar diffusion assay applying Staphylococcus
epidermidis as test organism, and the
composition of the gentamicin biosynthesized is assayed according to the procedure described in the Federal Register (21. Food and Drugs, April 1, 1977, 444.20 a/b, pp. 433 to 435).
It was found that the protoplast fusion process
is suitable for the transfer of genetic information
into other aminoglycoside-producer
Micromonospora, too, at a fairly high frequency.
In addition studies were carried out with the following strains:
Micromonospora olivoasterospora,
Micromonospora echinospora,
Micromonospora purpurea (holotype).
The process of the invention is further
illustrated with the aid of the following non
limiting Examples.
Example 1
The deep-freezed, vegetative mycelium of the following two mutants of sisomicin-producer
Micromonospora inyoensis ATCC 27600:
1. casamino-acid dependent, rifampicin
resistant Cas-RifR, and
2. casamino-acid non-dependent, rifampicinsensitive Cas+RifS
each is inoculated under sterile conditions into
500 ml Erlenmeyer flasks containing each 100 ml of a sterile seed medium consisting of 1% soymeal,
1% potato starch, 1% sucrose
0.4% CaCO3 suspended in tap water.
The seed medium inoculated with Cas-RisR is incubated for 40 hours at 370C on a rotary shaker. Then this seed medium is inoculated under sterile conditions into a 500 ml Erlenmeyer flask containing 100 ml of a sterile medium having the following composition:
0.1 % KNO3 0.05% K2HPO4
0.05% MgSO4.7H2O
0.05% NaCI
1.0 %glucose
0.1 % yeast extract
0.3 % casamino acid
0.2 % glycine
in distilled water.
Following inoculation this culture is incubated
in this medium for 48 hours at 370C on a rotary
shaker.
The seed medium inoculated with Cas+Rif5 is
incubated for 65 hours at 370C on a rotary
shaker, then this seed medium is inoculated under
sterile conditions into 500 ml Erlenmeyer flasks
each containing 100 ml of sterile medium having
the following composition:
0.1 % KNO3 0.05% K2HPO4
0.05% MgSO4.7H2O 0.05% NaCI
1.0 %glucose
0.1 % yeast extract
0.5 % glycine dissolved in distilled water.
Following inoculation this culture is incubated in this medium for 23 hours at 370C on a rotary shaker.
The culture of both mutants is centrifuged (6000 r.p.m.), the supernatant is discarded and the residue resuspended in 20 ml of medium P consisting of 0.2 M sucrose
0.25 g/l K2SO4
0.025 M TRIS--HCl+buffer, pH 7.2
50 mM MgCI2 10 mM CaCI2
0.8 mM K2HPO4
2 ml/l solution of trace elements dissolved dissolved in distilled water.
(+TRIS=tris/hydroxymethyl/-aminomethane) Composition of the solution containing trace
elements:
40 mg/l ZnCI2
200 mg/l FeCl3.6H20
10 mg/l CUC12j2H2 10 mg/l MnCl2.4H20
10 mg/l Na2B407. 1 OH20 10 mg/l (NH4)eMo7024.4H20 The suspensions obtained are centrifuged (6000 r.p.m.) under sterile conditions and resuspended in 2 ml each of medium Pt. To 1 ml of each suspension 1 ml of sterile lysozyme solution is added (20 mg/ml) under sterile conditions (final concentration of lysozyme is 10 mg/ml). Lysozyme itself (Calbiochem, San Diego,
California; 17,000 U/mg) is dissolved in medium
P1. The cultures containing lysozyme are slowly shaken in 25 ml Erlenmeyerflasks at 370C.
According to microscopic observations the cultures are quantitatively converted into protoplasts within 30 to 60 minutes. The protoplast suspensions obtained are centrifuged under sterile conditions, and resuspended in 2 ml each of medium P1, then this operation is repeated once more.
To carry out protoplast fusion the protoplast suspension of the two different mutants is combined in a ratio of 1 then 0.1 ml of this suspension is left to stand for 30 minutes in 0.9 ml of 50% aqueous polyethylene glycol)m.w.
6000) containing 15% of dimethyl sulfoxide. 0.05 ml of the suspension treated with polyethylene glycol is added dropwise into soft medium R1 containing 0.5% of agar. The resulting mixture is layered on solid medium R1 containing 2.2% of agar. The composition of medium R1 is as follows:
0.2 M sucrose
0.25 g/l K2S04
1.0 % glucose
0.3 % prolin
0.01 % casamino acid
2.0 ml/l solution containing
trace elements
0.025 M TR!S--HCI buffer pH 7.5
50 mM MgCI2 10 mM CaCI2
0.2 mM KH2PO4 0.1 % yeast extract dissolved in distilled water.
After 20 days the colonies grown at 32OC are washed off with a physiological salt solution, and plated onto a medium of the following composition:
0.1 %KNO3 0.05 % K2HPO4 0.05 % MgS04.7H20
0.05 % NaCI
0.001% FeS04.7H20
2.0 % water-soluble starch
0.001% rifampicin
1.5 %agar dissolved in distilled water
Following incubation of 4 to 6 days the colonies grown on this medium have genetic
material which is different from that of the parent
strains.
Example 2
The deep-freezed, vegetative mycelium of the following two mutants of gentamicin-producer
Micromonospora purpurea var. nigrescens (MNG
00122):
1. streptomycin resistant SmR
2. streptomycin sensitive Sms each js inoculated under sterile conditions into
500 ml Erlenmeyer flasks containing each 100 ml
of a sterile medium consisting of
1 % glucose
0.4 % peptone
0.4 % yeast extract
0.3 % glycine
0.2 % KH2PO4
0.4 % K2HPO4 0.05 % MgSO4.7H2O
2 ml/l solution containing
trace elements dissolved
in distilled water.
The cultures are incubated for 42 to 44 hours at 370C on a rotary shaker (320 r.p.m.). Then both cultures are centrifuged (6000 r.p.m., OOC) under sterile conditions, and the residue is suspended in 20 ml. f medium P2 having the following composition:
0.2 M sucrose
0.25 g/l K2SO4
0.025 M TRIS--HCI buffer pH 7.2
50 mM CaCI2
50 mM MAC12 0.8 mM KH2PO4
2 ml/l solution containing trace elements
dissolved in distilled water.
The suspensions obtained are centrifuged (6000 r.p.m., OOC) under sterile conditions, and resuspended in 2 ml of medium P2. To 1 ml of each suspension sterile lysozyme solution (10 mg/ml) is added (final lysozyme concentration: 5 mg/ml). The iysozyme (Calbiochem, San Diego,
California; 1 7 000 U/mg) itself is dissolved in medium P2. The cultures containing lysozyme are slowly (30 r.p.m.) shaken in 25 ml Erlenmeyer flasks at 370C. According to microscopic observations the cultures are converted quantitatively into protoplasts in about 30 to 45 minutes. The protoplast suspensions obtained are centrifuged (6000 r.p.m.) under sterile conditions.
The protopiasts of the streptomycin sensitive mutant are washed twice, i.e. they are resuspended in 10 ml each of medium R2 and centrifuged. This operation is repeated once more.
Composition of medium R2:
0.35 M sucrose
0.25 g/l K2SO4
1.0 % glucose
0.3 % prolin
0.01 % casamino acid
50 mM CaCI2
50 mM MgCl2 0.2 mM KH2PO4
2 ml/l solution containing trace
elements dissolved in
distilled water.
The streptomycin-resistant mutant is also washed twice with medium P2 then poured into a conic 25 ml flask containing 10 ml of a TRIS medium and preheated to 550C. Composition of theTRIS medium:
1.2 %TRIS
0.035 % KCI
0.1 % NH4CI 0.03 % MgCI2.6H20 0.0058 % NaCI
0.03 % Na2SO4.1 OH2O 0.5 Mg/ml FeCI2 0.35 M sucrose
dissolved in distilled water.
The pH value of the medium is set to 7.5.
The flask is incubated for 3 hours at 55"C without shaking, then the protoplasts are suspended by cautious shaking. Both the streptomycin-sensitive protoplast suspension, which did not undergo heat inactivation, and the streptomycin-resistant protoplast suspension, which received heat treatment, are combined at a ratio of 1:1.0.1 ml of the resulting suspension is left to stand for 10 minutes in 0.9 ml of a 50% aqueous polyethylene glycol (m.w. 6000) solution. 0.05 ml of the suspension containing the fused protoplasts are added dropwise to medium R2 (3 ml) containing 0.4% of agar. The mixture obtained is layered on solid medium R2 containing 2.2% of agar, and subsequently incubated at 370C. On the 8th day
TRIS medium containing 10,000,ug/ml of streptomycin and 0.5% of agar (3 ml) is layered on the plates.The colonies appearing after the 20th day are growing as a result of protoplast fusion and subsequent recombination.
Example 3
The protoplast fusion of the following gentamicin-producer Micromonospora purpurea var. nigrescens parent pair
1. casamino-acid dependent and
2. non-dependent on casamino acid for growth is performed according to the process described in Example 2. The mutant nondependent on casamino acid is heat-inactivated as described in Example 2 for the streptomycinresistant mutant. The heat-inactivated protoplast suspension prepared from the prototrophic parent, and the protoplast suspension untreated by heat and prepared from the casamino-acid dependent parent, are fused according to Example 2. The resulting mixture is layered on solid medium R2 containing 2.2% of agar and free from casamino acid, and incubated at 370C. The colonies appearing after 20 to 30 days are growing as a result of protoplast fusion and subsequent recombination.
Example 4
In order to prove the fusion between two species the following two parent pairs are applied:
1. Micromonospora purpurea var. nigrescens resistant to 100,ug/ml streptomycin
2. Micromonospora inyoensis resistant to 0.5 ,lg/ml streptomycin.
Heat-inactivated protoplast suspension is prepared from Micromonospora purpurea var.
nigrescens according to Example 2. The protoplasts which received heat treatment and the protoplast suspension prepared from
Micromonospora inyoensis according to Example 1 are combined at a ratio of 1:1, the resulting suspension is fused according to Example 1, and subsequently regenerated. On the 8th day the regenerated protoplasts are layered with 3 ml of a
TRIS medium containing 1000 yg/ml of streptomycin and 0.5% of agar. The colonies appearing after the 20th day are growing as a result of protoplast fusion between the two species and their subsequent recombination.
Claims (12)
1. Process for preparing antibiotic-producer
Micromonospora strains having modified genetic material, which comprises preparing, following cultivation in a glycine medium, a protoplast suspension with lysozyme, under osmotically buffered conditions ensured by sucrose, from each culture of two mutants of the antibioticproducer Micromonospora, at least one of the mutants being genetically marked, combining the two suspensions obtained in the presence of polyethylene glycol, and incubating at room temperature, suspending the resulting fused protoplast in soft agar, then plating on an agar plate incubating for 20 to 30 days, and finally selecting all colonies from the regenerated colonies which are sure to have genetic material different from that of the parent strains.
2. A process as claimed in claim 1 wherein the protoplasts are prepared from cultures being at the beginning of their logarithmic growth phase.
3. A process as claimed in claim 1 or claim 2 wherein the agar plate contains sucrose prolin and organic salts.
4. A process as claimed in any one of claims 1 to 3 wherein the transfer of genetic information is carried out within a species.
5. A process as claimed in claim 4 in which sisomicin-producer Micromonospora inyoensis strain is used.
6. A process as claimed in claim 4 in which gentamicin-producer Micromonospora purpurea var. nigrescens strain is used.
7. A process as claimed in claim 4 in which gentamicin-producer Micromonospora purpurea (holotype) is used.
8. A process as claimed in claim 4 in which gentamicin-producer Micromonospora echinospora strain is used.
9. A process as claimed in claim 4 in which fortimicin-producer Micromonospora olivoasterospora strain is used.
10. A process as claimed in any one of claims 1 to 3, in which the transfer of genetic information is carried out between any of the following species pairs: sisomicin-producer
Micromonospora inyoensis strain; gentamicinproducer Micromonospora purpurea vir.
nigrescens; gentamicin-producer
Micromonospora purpurae (holotype); gentamicin-producer Micromonospora echinospora strain; fortimicin-producer
Micromonospora olivoasterospora strain.
11. A process as claimed in any one of the preceding claims wherein the protoplasts of one of the parents are inactivated by heat.
12. A process for producing a Micromonospora strain as claimed in claim 1 substantially as hereinbefore described in any one of the
Examples.
1 3. A Micromonospora strain when produced by a process as claimed in any one of claims 1 to 12.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
HU78GO1430A HU184125B (en) | 1978-11-13 | 1978-11-13 | New genetic process for preparing antibiotic producing micromono spora strains |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2036076A true GB2036076A (en) | 1980-06-25 |
GB2036076B GB2036076B (en) | 1982-11-10 |
Family
ID=10996880
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB7938689A Expired GB2036076B (en) | 1978-11-13 | 1979-11-08 | Genectic process for the production of antibiotic producing micromonospora strains |
Country Status (5)
Country | Link |
---|---|
BE (1) | BE879962A (en) |
DE (1) | DE2945762A1 (en) |
FR (1) | FR2441660A1 (en) |
GB (1) | GB2036076B (en) |
HU (1) | HU184125B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1986002382A1 (en) * | 1984-10-12 | 1986-04-24 | Gca Corporation | Medium for the production of viable, fused cells |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
HU194306B (en) * | 1983-05-16 | 1988-01-28 | Gyogyszerkutato Intezet | Process for influencing biosynthesis of antibiotics with in vivo genetical recombination |
EP0155594A3 (en) * | 1984-03-06 | 1987-10-07 | Massachusetts Institute Of Technology | Cloned plasmids of corynebacterium |
US6886207B1 (en) | 1999-06-14 | 2005-05-03 | The Procter & Gamble Company | Toothbrush |
US20050000043A1 (en) | 2003-04-23 | 2005-01-06 | The Procter & Gamble Company | Electric toothbrushes |
-
1978
- 1978-11-13 HU HU78GO1430A patent/HU184125B/en unknown
-
1979
- 1979-11-08 GB GB7938689A patent/GB2036076B/en not_active Expired
- 1979-11-12 FR FR7927773A patent/FR2441660A1/en active Granted
- 1979-11-12 BE BE1/9605A patent/BE879962A/en not_active IP Right Cessation
- 1979-11-13 DE DE19792945762 patent/DE2945762A1/en not_active Withdrawn
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1986002382A1 (en) * | 1984-10-12 | 1986-04-24 | Gca Corporation | Medium for the production of viable, fused cells |
GB2179368A (en) * | 1984-10-12 | 1987-03-04 | Gca Corp | Medium for the production of viable, fused cells |
Also Published As
Publication number | Publication date |
---|---|
HU184125B (en) | 1984-07-30 |
FR2441660B1 (en) | 1983-06-24 |
BE879962A (en) | 1980-05-12 |
GB2036076B (en) | 1982-11-10 |
FR2441660A1 (en) | 1980-06-13 |
DE2945762A1 (en) | 1980-05-22 |
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