Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
  • C07H19/00—Compounds containing a hetero ring sharing one ring hetero atom with a saccharide radical; Nucleosides; Mononucleotides; Anhydro-derivatives thereof
  • C07H19/01—Compounds containing a hetero ring sharing one ring hetero atom with a saccharide radical; Nucleosides; Mononucleotides; Anhydro-derivatives thereof sharing oxygen

Definitions

• the present invention relates to an improvement in a method of producing polyether type antibiotics on an industrial sc le.
• Salinomvcin 4-methvlsalino- mycin, SY-1, SY-2, SY-3, SY-4, SY-5, SY-6, SY-7 and SY-8 substance are called Salinomycin type antibiotics because they have similar chemical structures.
• salinomycins means each compound, or any mixture of at least two compounds, selected from the group SY-7, SY-8 consisting of salinomycin, SY-1, SY-2, SY-3, SY-4, SY-5, SY-6/and the like.
• the present inventors already found that salinomycin, SY-1 and SY-2 were produced in the culture of Streptomyces albus waxman and henrich No.80614 strain ( FERM-P. No.419 ), and succeeded in isolating the antibiotics from the culture ( British Patent No.1378414, Japanese Unexamined Patent Publication No. 86191/1976 and Japanese Patent Application No. 5762/1977).
• the inventors continued the study and found that, when the above strain is cultured in a medium containing fatty acid or its precursor, it produces salinomycin, SY-1, and SY-2 ' in high yield, and also produces new compounds such as SY-3, SY-4, SY-5, SY-6, SY-7 and SY-8.
• Another object of the present invention is to provide a method of producing Salinomycin type antibiotics such as salinomycin, 4-methylsalinomycin, SY-1, SY-2, SY-3, SY-4, SY-5, SY-6, SY-7 and SY-8 substances in high yield.
• Salinomycin type antibiotics such as salinomycin, 4-methylsalinomycin, SY-1, SY-2, SY-3, SY-4, SY-5, SY-6, SY-7 and SY-8 substances in high yield.
• salinomycin type antibiotics such as salinomycin, 4-methylsalinomycin, SY-1, SY-2, SY-3, SY-4, SY-5, SY-6, SY-7 and SY-8 substances are produced by culturing a salinomycin type antibiotic-producing microorganism in a medium containing a fatty acid or its precursor and ammonia or an ammonium salt or urea.
• the fatty acids used in the present invention are saturated or unsaturated fatty acids, for example, acetic acid, propionic acid, caproic acid, capric acid, palmitic acid, stearic acid, methacrylic acid, undecylic acid, and particularly linolic acid, linolenic acid or oleic acid being preferable.
• the precursor of fatty acid means a substance that is capable of giving said fatty acid .outside or inside the microorganism cell, such as mono- di- or triglycerides of fatty acid, esters of fatty acid or salts of fatty acid.
• esters with The esters of fatty acid can be/C1-C18 alcohols of said fatty acid.
• the salts of fatty acid can be ammonium salt and alkali metal salts and alkaline earth metal salts of said fatty acid.
• the addition amount is generally about 1-25 % , particularly about 12-20% based on the medium.
• Ammonia is used in gaseous form or in the form of an aqueous solution.
• ammonium salt there are used ammonium salts of inorganic acids such as hydrochloric acid, sulfuric acid, nitric acid and phosphoric acid or organic acids such as acetic acid, propionic acid, higher fatty acid, oxalic acid, tartaric acid, hydrogentartaric acid, citric acid, lactic acid and malic acid.
• the addition amount is generally about 0.1-1.0% particularly about 0.3-0.5% based on the medium.
• addition is effective so long as production of potency of I the addition polyether type antibiotic continues, and / is conducted at any time either before or after beginning of cultivation.
• cultivation conditions of the present invention can be selected in accordance with the methods described in said known literatures, excepting that fatty acid or its precursor is used as major carbon source and that ammonia or ammonium salt is used as essential component of the medium, it is possible to raise the production efficiency by varying the conditions depending on the kind of antibiotics.
• microorganismsused in the present invention include generally polyether type antibiotics producing strains belonging to the genus of Streptomyces as well as the strains described in said literatures and their natural or artificial mutants.
• Separation and purification of the products can be carried out in accordance with known methods. Since the objective substance is often contained mainly in the solid portion containing the cells when the production amount of the objective substance is abundant, it is desirable to vary the extraction step properly in order to heighten the recovery percentage of the objective substance from the solid portion. It is possible to use the objective compound in the state that it is contained in the solid portion depending on the use purposes, without separating the objective substance from the solid portion.
• the production amount of polyether type antibiotics, particularly Salinomycin type antibiotics can be remarkably increased.
• the yield of Salinomycin is generally 100-300 Y/ml in known method, whereas the yield is about 10,000-20,000 y/ml in the medium containing fatty acid or its precursor, and the yield is further increased to about 50,000-80,000 Y/ml when said medium contains further ammonia or ammonium salt.
• salinomycins mainly occur in the mycelial mass,and it is preferrable to recover salinomycins from the mycelial mass.
• other new compounds especially SY-3, SY-4, SY-5, SY-6 and the like are obtained from the culture.
• the strains used in this invention include Streptomyces albus No.80614 and its mutants artificially or naturally produced, as well as the other Streptomyces strains capable of producing salinomycins. However, some of the salinomycins can occasionally not be detected in the culture, depending on the strain and fermentation conditions.
• Fermentation conditions employed in this invention can be any one commonly used for culturing Actinomycetes, except that main carbon source should be a fatty acid or its precursor. Maximum production of salinomycins usually occurs after 150 to 260 hours The from the start of fermentation. /ratio of each of salinomycins produced sometimes varies depending on the incubation time. Naturally, the composition of medium and fermentation conditions should be decided for each strain and external conditions, so that most desirable results are obtained.
• Salinomycins can be isolated from the culture medium by utilizing the physico-chemical properties of salinomycins. Because salinomycins are structurally related to each other, the known extraction methods for salinomycin and SY-1 can be applied to the isolation of salinomycins, however, as for salinomycin, because a large portion of salinomycin is contained in mycelial mass, the extraction process is preferrably modified so as to increase the recovery rate of salinomycin. For example, it is preferred to adjust the whole fermentation broth to PH 2.0-6.0 to precipitate salinomycin, and then to extract the mycelial mass together with the precipitate thus formed with an organic solvent.
• the preferred solvents are acetone, ethyl acetate, butyl acetate, n-hexane, chloroform and the like.
• the effluent is collected in 2-5 fractions according to the purpo-e. Separation and purification of salinomycins are effected by the procedures utilizing the difference between the properties of desired compound and imprities. Chromatograpy, solvent extraction and the like are repeated for each fraction to give salinomycin, SY-1, SY-2, SY-3, SY-4, SY-5, SY-6, SY-7, SY-8 anc the like, individually or as mixtures. The resulting products can be further purified by recrystallization or chromatography.
• Table 1 The properties of salinomycins obtained by the process of this invention are shown in the following table 1.
• salinomycin, SY-1, and SY-2 especially salinomycin are obtained in surprisingly higher yield than the known process.
• New compounds, SY-3 through -8 are also obtained according to this invention. They are comparable to salinomycin in their activities against microorganisms and useful as medicines. Also, because of their structural similarity to salinomycin, their usefulness as veterinary medicines looks very likely.
• Streptomyces albus waxman and henrich No.80614 strain (FERM-P. No.419) is inoculated to a medium containing glycerine 2.0%, peptone 0.5% and meat extract 0.5% and cultured at 33°C for 48 hours under shaking.
• 1 litre of this culture liquid is inoculated to 100 litres of liquid medium ( 200 litre tank made of stainless steel ) containing glucose 2%, starch 1%, soy bean powder 2.5%, beer yeast 0.4%, meat extract 0.1%, sodium chloride 0.2% and antifoaming agent KM-68-2F ( product of Shinetsu Chemical Industry Co., Ltd., silicone type ) 0.1% and cultured at 33°C for 144 hours under stirring with the aeration volume of 100 1/m. There is obtained a culture liquid containing .100-300 y/ml of Salinomycin.
• the 80614 strain which is the same strain as described in Example 1 is inoculated to a medium containing glycerine 2.0%, peptone 0.25%, meat extract 0.5% and edible salt 0.1%, and cultured at 33°C for 48 hours under shaking.
• This culture liquid in an amount corresponding to 1% of the medium is inoculated to the medium containing glucose 4.0%, soy bean powder 1.0%, beer yeast 1.0% and calcium carbonate 0.2%, and cultured for 30 hours at 33°C under shaking, and this culture liquid is made the second-stage pre-culture liquid.
• This second-stage pre-culture liquid is inoculated to 100 litres of liquid medium containing soy bean oil 10%, glucose 1.0%, soy bean powder 1.0%, calcium carbonate 0.5%, potassium secondary phosphate 0.01%, and cultured for 210 hours at 33°C with an aeration volume of 100 1/m under stirring. There is obtained a culture liquid containing 20,000 Y/ml of Salinomycin.
• the 80614 strain which is the same strain as described in Example 1 is inoculated to a medium containing glycerine 2.0%, peptone 0.25%, meat extract 0.5% and edible salt 0.1%, and cultured at 33°C for 48 hours under shaking.
• This culture liquid in an amount corresponding to 1% of the medium is inoculated to the medium containing glucose 4.0%, soy bean powder 1.0%, beer yeast 1.0% and calcium carbonate 0.2%, and cultured for 30 hours at 33°C under shaking, and this culture liquid is made the second-stage, pre-culture liquid.
• This second-stage pre-culture liquid is inoculated to 100 litres of liquid medium containing soy.bean oil 10%, glucose 1.0%, soy bean powder 1.0%, calcium carbonate 0.5%, potassium secondary phosphate 0.01%, and cultured for 210 hours at 33°C with an aeration volume of 100 1/m under stirrinq. There is obtained a culture liquid containing 20,000 ⁇ /ml of salinomycin(salinomycin only).
• the culture liquid obtained in (A) is adjusted to PH 4.5-5.0 with dilute hydrochloride, admixed with 4% by weight per volume of filter aid with stirring, and filtered.
• the filtrate ( 80 litres ) is extracted with 50 litres of butyl acetate with stirring.
• Mycelial mass is extracted with 30 litres of butyl acetate.
• Both butyl acetate solutions are combined and washed with 20 litres of 5% aqueous sodium bicarbonate solution.
• One litre of the washed butyl acetate solution is concentrated under vacuum to dryness to give 250g of crude powder of salinomycin containing trace amount of SY-1 and SY-2.
• the almina column as mentioned above is further developed with a 100:15 mixture of ethyl acetate-methanol to elute SY-2, which is separated and purified by silica gel chromatography in the same manner as described above, and crystallized from acetone-water solution to give 3mg of pure crystalline SY-2.
• the culture obtained in (A) is adjusted to pH 4.5-5.0, heated at 60°C for 10 minutes with stirring, admixed with 4% by weight per volume of filter aid with stirring and filtered.
• the resulting mycelial mass contains salinomycins and SY group compounds in high yield.
• Mycelial mass obtained in (B) is extracted twice with 50 litres of ethyl acetate. The extracts are combined and washed with 50 litres of 5% aqueous sodium bicarbonate solution. Ethyl acetate phase is concentrated under vacuum to dryness to yield 7kg of crude salinomycins complex containing SY group compounds.
• the mother liquor separated from the precipitate in the process in (A) is concentrated to dryness to give 4.6kg of complex contain-- ing a small amount of salinomycin and SY group compounds.
• the complex is dissolved in 50 litres of hexane-ethyl acetate solvent mixture (2:1) and applied to the column of 12kg of almina packed in the same solvent system, developed with 20 litres of a 100:2 mixture of ethyl acetate-methanol to elute SY-3, SY-7 and salinomycin.
• Two hundred g of the mixture of salinomycin and SY-1 is separated by precipitation in the same manner as described in (D).
• the filtrate containing SY-3 and SY-7 is concentrated to dryness to give 100g of crude powder.
• the above almina column is eluted with 20 litres of a 5:1 mixture of ethyl acetate-methanol, and the effluent is concentrated under vacuum to give 200g of crude powder, which contains the complex of SY-2, SY-4, SY-5, SY-6 and SY-8.
• These compounds are isolated individually by silica gel column chromatography. Two hundred g of the crude powder is dissolved in 500ml of a 100:2 mixture of chloroform-methanol, applied to the column of 2kg silica gel (Wakogel C-200) packed in the same solvent mixture, and developed with the same solvent mixture to give.each fraction containing SY-2, SY-4, SY-5, SY-6 and SY-8, respectively.
• Example 1 The second-stage pre-culture liquid of Example 1 in an amount corresponding 10% of the medium is inoculated to the medium containing glucose 4%, soy bean powder 3%, defatted wheat germs 3.0%, calcium carbonate 0.2% and antifoaming agent KM-68-2F 0.1%, and cultured for 24 hours at 33°C to give the third-stage pre-culture liquid.
• the complex is dissolved in 600ml of chloroform-methanol solution(100:2), and then treated by chromatography(20kg silica gel) in the same manner as described above to give 40g of SY-2, 600mg each of SY-4 and SY-5, 1900mg of SY-6 and 300ing of SY-8 as crude powders, purification of which according to the procedure of Example 2 (E) gives 30g of crystallin SY-2, 180mg of SY-4 powder, 120mg of SY-5 powder, 350mg of SY-6 powder and 90mg of SY-8 powder, all in pure form.
• the third-stage pre-culture liquid in Example 3 in an amount corresponding to 10% of the medium is inoculated to the medium (50ml-) containing each fat-and-oil shown in the following Table 12%, soy bean powder 0.5%, defatted wheat germs 1.0%, sodium chloride 0.2%, potassium chloride 0.2%, calcium carbonate 0.5%, ammonium sulfate 0.3%, potassium secondary phosphate,0.02% and magnesium sulfate 0.01%, and cultured at 33°C for 216 hours under shaking.
• the production amounts of salinomycin at the end of cultivation are shown in the following Table.

Landscapes

• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Health & Medical Sciences (AREA)
• Life Sciences & Earth Sciences (AREA)
• Engineering & Computer Science (AREA)
• Biochemistry (AREA)
• Biotechnology (AREA)
• General Health & Medical Sciences (AREA)
• Genetics & Genomics (AREA)
• Molecular Biology (AREA)
• Preparation Of Compounds By Using Micro-Organisms (AREA)

Applications Claiming Priority (2)

Publications (2)

Family

ID=13222746

Family Applications (1)

Country Status (3)

Cited By (3)

Families Citing this family (1)

Citations (3)

• 1977
  • 1977-06-01 JP JP6321577A patent/JPS53148595A/ja active Pending
• 1978
  • 1978-06-01 EP EP19780100061 patent/EP0000037B1/fr not_active Expired
  • 1978-06-01 DE DE7878100061T patent/DE2861764D1/de not_active Expired

Patent Citations (3)

Also Published As

Similar Documents

Legal Events