# Patent

## Title
Manufacture of halogenated ketones and aldehydes

## Abstract

This is a division of application Ser. No. 340,449, filed 1/18/82, now U.S. Pat. No. 4,415,517.

## Background
The present invention relates to a new antibiotic compound to a microbiological process for its production from a Streptomyces strain, and to its use as an antimicrobial agent in medicine.

It has already been disclosed that a series of compounds of microbial origin have antimicrobial actions. Some of these antibiotics are not fully satisfactory in their spectra of action. They frequently have still further disadvantages. .beta.-Lactam antibiotics are often inactivated by penicillinase, and chloramphenicol, tetracyclins and streptomycin exhibit considerable undesired side effects in many cases (see Walter, Heilmeyer, Antibiotika Fibel (Antibiotics Primer), Georg Thieme Verlag, Stuttgart, 3rd edition, 1969, pages 248, 278-280 and 311-319).

It has now been found that a new antibiotic compound is obtained if the strain of Streptomyces spec. WS 116 is grown in a nutrient medium and the compound is isolated from the nutrient medium.

The new antibiotic compound has a powerful antimicrobial action. It can be iron-free or iron-containing. Both forms can be successfully employed as an antibacterial agent. (The new antibiotic compound is referred to for brevity hereinafter as "BAY i 3265 component B").

The new compound in the iron-free form may be characterised by the following properties:

(1) The elementary analysis C 42.3%, H 6.2%; N 15.7%; O 31.4%; S 3.6%.

It must be pointed out here that in the case of higher-molecular natural substances the margin of error of the elementary analysis can be greater, as generally customary, and an exact determination of the total molecular formula is often not possible (R. B. Woodward, Angew. Chem. 69, pages 50-51 (1957)).

(2) The freeze-dried compound decomposes at about 185.degree. C.

(3) Ultraviolet absorption spectrum:

The UV spectrum was carried out on an aqueous solution of the compound (C=1.786 mg in 25 ml of H.sub.2 O). The spectra in acid or basic solution were measured on a solution which was prepared by the addition of 100 microliters of 1N hydrochloric acid (or sodium hydroxide solution) to 3 ml of the above solution. ______________________________________ ##STR1## .lambda. max [m.mu.] ##STR2## ______________________________________ neutral      282       123 acid         304       108 basic        277       118 ______________________________________

(4) The IR absorption spectrum of the compound is represented in accompanying FIG. 1 (abscissa; wave number in cm.sup.-1, ordinate: absorption)

When the substance is pressed into KBr pressed plates, the spectrum shows absorption bands at the following wavelengths (expressed in cm.sup.-1): ______________________________________ Wavelength of the 1R absorption spectrum Wavelengths in cm.sup.-1 ______________________________________ 3388 2944 1695 1648 1545 1457 1417 1390 1299 1240 1070 1050 975 ______________________________________

(5) The .sup.1 H nuclear resonance spectrum gives the signal position in parts per million (ppm) and vibrations per second, according to accompanying FIG. 2. It was recorded for an aqueous solution of the compound, using the 3(Trimethylsilyl)propionic acid-d4 sodium salt as a standard (external), on a WH-360 spectrometer of Messrs. Bruker, at a field strength of 360 MHZ.

(6) The 13-C nuclear resonance spectrum was recorded on a WM-250 spectrometer of Messrs. Bruker, at a field strength of 62.71 MHZ, on an aqueous solution of the compound, the measurements being converted to dioxane as the external standard (shift position 67.400 ppm relative to tetramethylsilane=0).

The 13-C nuclear resonance spectrum according to FIG. 3 shows the following signals, given in parts per million (ppm) and vibrations per second (HZ), in their relative intensities: ______________________________________ Shift positions and intensities of the signals in the 13-C nuclear resonance spectrum relative to dioxane = 67.400 ppm (external) Signal NS  Relative intensity Signal position (ppm) ______________________________________ 1         3.344        175.878 2         2.094        174.610 3         1.628        174.289 4         1.634        174.032 5         1.708        171.786 6         1.25         167.843 7         1.966        156.220 8         2.580        153.171 9         3.806        138.745 10         3.979        98.082 11         3.729        80.173 12         3.207        76.001 13         3.044        69.984 14         83.487       67.400 15         2.996        64.094 16         4.082        62.072 17         1.751        58.606 18         2.995        56.392 19         4.129        54.418 20         4.430        54.322 21         2.449        54.017 22         2.983        51.064 23         3.998        48.111 24         2.442        29.834 25         4.590        29.048 26         5.047        28.967 27         2.559        23.319 28         2.276        23.223 29         1.510        22.634 30         7.743        20.222 ______________________________________

(7) The optical rotation value immediately after the substance has dissolved as [.alpha.].sub.D.sup.20 =-27.725.degree. (C=0.2723% in water)

(8) The compound has an unlimited solubility in water at pH 7, is slightly soluble in methanol, dimethylformamide and dimethylsulphoxide, and is sparingly soluble in chloroform, ether, ethyl acetate and petroleum ether.

By "slightly soluble" is meant a solubility of less than 10 g/l and by "sparingly soluble" is meant a solubility of less than 0,1 g/l.

(9) The compound is a colourless, amorphous solid, the aqueous solution of which has a neutral reaction.

(10) The R.sub.f values of the compound in the iron-free and iron-containing form in comparison with other compounds in various mobile solvents are given in Table 4.

(a) Instant thin layer chromatography plates silica gel 60 F 254 (Merck) ______________________________________ Substance            S 1    S 2 ______________________________________ Neomycin sulphate    0.01   0.16 2-Desoxystreptamine .times. 0.03   0.19 2 HCl Sisomycin base       0.14   0.42 Compound according   0.02   0.25 to the invention, iron-free Compound according   0      0.22 to the invention, iron- containing ______________________________________

(b) Instant thin layer chromatography plates cellulose F (Merck) 15/10/3/12 ______________________________________ Substance       S 1        S 2    S 3 ______________________________________ Neomycin sulphate 0.06       0.06   0.06 2-Desoxystreptamine .times. 0.10       0.13   0.42 2 H.sub.2 O Sisomycin base  0.16       0.27   0.49 Compound according 0.27       0.33   0.80 to the invention, iron-free Compound according 0.15       0.19   0.71 to the invention, iron containing ______________________________________

(11) The new compound in its iron-free form can be made visible on the thin layer plate using FeCl.sub.3.sup.(*) alkaline potassium permanganate, iodine and ninhydrin, and in UV light at 254 or 280 nm by fluorescence extinction. recipes (for example E. Stahl Dunnschichtchromatographie (Thin layer chromatography) 2nd edition, Springer Verlag, Berlin)

(12) In the aminoacid analysis, when the hydrolysis is carried out for 24 hours in a closed glass at 110.degree. C., the total hydrolysis of the compound using aqueous 57% strength hydriodic acid shows that the substance contains three units of ornithine in addition to one unit of serine. Apart from these, only traces of other natural aminoacids were found.

It was possible to determine the constitution of the compound BAY i 3265 component B according to the invention, by means of derivatives and isolation of the hydrolysis products and their derivatives.

According to the present invention there is therefore provided an antibiotic compound which, in the iron-free form, is of the formula ##STR3##

A resulting basic compound can be converted into a corresponding acid addition salt, for example by reacting it with an inorganic or organic acid, such as therapeutically useful acid, or with a corresponding anion exchange preparation, and isolating the desired salt. An acid addition salt may be converted into the free compound by treatment with a base, e.g. a metal hydroxide, ammonia or a hydroxyl ion exchange preparation. Therapeutically useful acids are, for example, inorganic acids, e.g. hydrochloric, hydrobromic, sulfuric, phosphoric, nitric or perchloric acid, or organic acids, e.g. carboxylic or sulfonic acids, such as formic, acetic, propionic, succinic, glycollic, lactic, malic, tartaric, citric, ascorbic, maleic, hydroxymaleic, pyroracemic, phenylacetic, benzoic, 4-aminobenzoic, anthranilic, 4-hydroxybenzoic, salicyclic, aminosalicyclic, embonic, nicotinic, methanesulfonic, ethanesulfonic, hydroxy-ethanesulfonic, ethylenesulfonic, benzenesulfonic, halogenobenzenesulfonic, toluensulfonic, naphthalenesulfonic and sulfanilic acid; methionine, tryptophan, lysine and arginine.

Salts of the above-mentioned acids or other salts, for example, the picrates, can also be used for purification of the bases obtained; the bases are converted into salts, the salts are separated and the bases are liberated from the salts. In view of the close relationship between the free compounds and the compounds in the form of their salts, whenever a compound is referred to in this context, a corresponding salt is also intended, provided such is possible or appropriate under the circumstances.

Racemate mixtures can be separated into the pure racemates in a known manner on the basis of the physicochemical differences of the constituents, for example by chromatography and/or fractional crystallization.

Pure racemates can be resolved according to known methods, for example by recrystallization from an optically active solvent, with the aid of micro-organisms or by reaction with an optically active acid or base which forms salts with the racemic compound and separation of the salts obtained in this manner, for example on the basis of their different solubilities, into the diastereomers from which the antipodes can be liberated by the action of suitable agents. Particularly customary optically active acids are, for example, the d- and l-forms of tartaric acid, di-o-toluyltartaric acid, malic acid, mandelic acid, camphorsulphonic acid or quinic acid. Suitable optically active bases are, for example, optically active .alpha.-phenylethylamine, .alpha.-(1-naphthyl)-ethylamine, quinine, cinchonidine and brucine. Advantageously, the more active of the two antipodes is isolated.

According to the invention it is however also possible to obtain the end product in the form of pure racemates or optical antipodes by employing starting substances, containing one or more asymmetrical C atoms, in the form of the pure racemates or optical antipodes.

The compound of the present invention may be characterised in practice by just some of the above-mentioned properties.

According to the present invention there is therefore provided an iron-free or iron-containing antibiotic compound, with a decomposition point of 185.degree. C. and an optical rotation [.alpha.].sub.D.sup.20 =-27.7.degree. (C=0.2723 in water, measured immediately) as the iron-free substance, which is readily soluble in water at pH 7, noticeably soluble in methanol, dimethylformamide and dimethylsulphoxide and sparingly soluble in chloroform, ether, ethyl acetate and petroleum ether, has a maximum at 304 m.mu. in the UV spectrum in water (acid), as a KBr pressed plate has absorption maxima at 3388, 2944, 1695, 1648, 1545, 1457, 1417, 1390, 1299, 1240, 1070, 1050 and 975 in the infrared region, and releases ornithine and serine in the ratio 3:1 on acid hydrolysis, and, preferably, with a 1H-NMR spectrum according to accompanying FIG. 2, with a 13C-NMR spectrum according to accompanying FIG. 3 and with a maximum at 282 m.mu. in the UV spectrum in water at pH 7.

The compound according to the present invention is produced by means of the submerse culture of a Streptomycetes strain in suitable nutrient solutions under suitable physical conditions. It is separated off from the culture solution by extraction or by adsorption, and is concentrated by further suitable methods.

According to the present invention we therefore provide a process for the production of the antibiotic compound of the present invention, in which Streptomyces spec. WS. 116 (DSM 1692) is grown under submerse, aerobic conditions, in a nutrient medium containing assimilable carbon, nitrogen and one or more mineral salts, particularly an iron salt or salts, at a temperature of from 15.degree. to 35.degree. C., and the compound formed is isolated from the fermentation liquid.

The new strain Streptomyces spec. WS 116 from the order of the Actinomycetales, family Streptomycetaceae, genus Streptomyces, or variants and mutants originating from it, can be employed for the preparation process. This strain was isolated from a marine soil sediment sample of the Ibero-Canary Sea. It was deposited on 7.12.1979 in the Deutsche Sammlung fur Mikroorganismen (German Collection of Microorganisms), Gottingen, under the number DSM 1692. It has the following characteristics: 0.4-0.7.times.0.7-1.2.mu. and a smooth surface. and yellowish in the mature state (Griseus type). monopodially branched. tyrosine-agar. The strain is not chromogenous.

The summarised determining characteristics identify the strain WS-116 as belonging to the species Streptomyces griseus Waksman et Henrici.

Nutrient media which contain the customary carbon and nitrogen sources and the necessary salts are used for the process for the preparation of the compound according to the invention.

The following can be used as the carbon source: carbohydrates, particularly polysaccharides (such as starch or dextrins), disaccharides (such as maltose or cane sugar), monosaccharides (such as glucose or xylose), sugar alcohols (such as mannitol or glycerol), carboxylic acids (such as citric acid, maleci acid or acetic acid) or mixtures thereof, and, in addition, naturally occurring mixtures, such as malt extract. Surprisingly, the highest active compound yields were achieved with carboxylic acids, particularly with citric acid, as the main C source.

The customary nitrogen sources can be used as the nitrogen source, such as proteins, protein hydrolysates, amino acids (such as glutamic acid, aspartic acid, argenine, lysine, ornithine or serine) and, in addition, nucleoside bases (such as cytosine or uracil), ammonium salts, nitrates, naturally-occurring complex substances (such as peptones, corn-steep liquor, soya bean flour, meat extracts or yeast extracts) and suitable mixtures of these. Particularly high active compound yields are obtained if L-ornithine and L-serine are added, in a sterile-filtered form, in the weight ratio 3:1, for example 0.3% and 0.1% by weight, to the medium, in addition to the customary complex N sources.

Mineral salts, for example phosphates, sulphates, carbonates, nitrates or chlorides of sodium, potassium, calcium, magnesium, iron, zinc, copper, molybdenum, cobalt, nickel and manganese are required in the nutrient medium as auxiliaries. The presence of about 0.01% by weight of FeCl.sub.3 proved to be significant. Some of the mineral salts, also the FeCl.sub.3, are contained as constituents, in the required concentrations, in the above-mentioned carbon or nitrogen sources or in the water used.

Furthermore, anti-foam agents of the most diverse types, such as soya oil, polyols or silicones, can also be used as auxiliaries.

Water should be mentioned as the most important diluent for the nutrient media.

It has been found to be particularly effective if the fermentation is carried out either in a nutrient solution which contains citric acid as the main carbon source, several naturally-occurring complex nitrogen sources and the amino-acids L-ornithine and L-serine, or in a completely synthetic nutrient solution which, in addition to mineral salts, contains citric acid as the carbon source and L-arginine as the only nitrogen source.

The yield of the process of the invention may be increased if a mixture of citric acid, L-arginine and salts is further fed to the nutrient solution at such a rate that a constant pH value of about 7.5 is maintained.

The preparation process is carried out under aerobic or microaerophilic conditions; the culture can be carried out in the customary batch or fedbatch process, according to customary methods, for example using shake cultures or aerated fermenter cultures. The percentage proportions (percentages by weight in each case) of the nutrient solution constituents can vary within wide ranges, and, in general, the carbon sources make up 0.5 to 8%, preferably 0.6 to 6%, in total, and the nitrogen sources make up 0.1 to 4%, preferably 0.5 to 2%, in total; the salts are present in the customary concentrations, preferably in the range between 0.001 and 0.5% by weight. The anti-foam agents are present in 0 to 1% strength concentration. The temperatures used for the sterilisation are 100.degree. to 140.degree. C., preferably 120.degree. to 130.degree. C., and sensitive substances, such as aminoacids, are sterilised by filtration.

The pH values of the growing cultures are between 5 and 10, preferably between 6 and 9.5. The growth temperature can be between 15.degree. and 35.degree. C., preferably between 20.degree. and 30.degree. C. It has been found that the quantity of the antibiotic being concentrated in the culture broth generally reaches its maximum about 1 to 10, preferably about 2 to 6 days after the beginning of growth. The end point of the fermentation is determined with the aid of biological tests (action against E. coli in a customary agar-diffusion test).

The compound according to the invention is generally isolated from the culture filtrate by extraction with mixtures of phenol/chloroform or by adsorption onto active charcoal or onto suitable resins. The compound according to the invention is advantageously bound to non-specific adsorption resins based on polystyrene (for example "Amberlite" XAD--Trade Mark of Messrs. Rohm and Haas or "Lewatit" OC 1031 of Messrs. Bayer).

It has surprisingly been found that the compound according to the invention is particularly firmly bound by non-specific adsorption resins if, before the adsorption process, iron salts, particularly iron chloride, are added, generally in a concentration of from 0.05 to 0.2, particularly about 0.1 g/liter of culture broth. The adsorption is carried out in the pH range of 3-9, particularly in the range of 5-7. The desorption of the compound according to the invention from such resins is carried out fractionally with mixtures of water and organic solvents, particularly water/methanol. The active fractions are combined, concentrated to a small volume, and lyophilised. A 0.5-3% strength crude product is obtained, which contains the compound according to the invention, in addition to other substances.

Starting from this crude product, the further concentration of the compound according to the invention can be carried out by a combination of anion exchange chromatography (for example DEAE-"Sephadex" A 25--Trade Mark of Messrs. Pharmacia) and cation exchange chromatography (for example SP- or CM-"Sephadex" C 25--Trade Mark of Messrs. Pharmacia). A 30-50% strength preparation is obtained thereby, since accompanying peptides are not separated off. These peptides can be separated off and, thus, the pure compound prepared by adsorption or partition chromatography of the approximately 30 to 50% strength compound over silica gel in the system isobutanol/ethanol/25% strength concentration ammonia=9/1/5 (parts by volume).

However, this separation process is associated with substance losses.

The separation can be carried out in a substantially simpler manner by means of affinity chromatography over a cation exchanger in an Fe.sup.3+ -containing column. For this purpose, a cation exchanger based on polystyrene or polyacrylate resin (for example "Dowex" 50 WX 4--Trade Mark of Messrs. DOW Chemical) or based on polydextrane (for example "Sephadex" C 25--Trade Mark of Messrs. Pharmacia) is converted into the Fe.sup.3+ form, using FeCl.sub.3 solution. The solution of the crude product is now introduced onto the resin in the Fe.sup.3+ form and is then rinsed with water. The crude product is then eluted with a buffer of high ionic strength, for example 0.2M NaH.sub.2 PO.sub.4 /0.3M NaCl. This buffer elutes the bulk of the inactive accompanying peptides. The active substances are then eluted from the column using the same buffer, but with the addition of 0.05M ethvlenediamine-tetraacetic acid or another iron complex-forming agent (for example citrate). The active fractions are combined and are introduced over a column with a non-specific adsorption resin (for example "Lewatit OC" 1031--Trade Mark of Messrs. Bayer), the active substances being bound. The column is eluted with methanol, and the runnings are concentrated and lyophilised.

The compound according to the invention may be obtained in pure form by partition chromatography on "Sephadex" G 25 in nBuOH/iso BuOH/0.2M (NH.sub.4).sub.2 SO.sub.4 =2/1/1.

The purification of the product according to the invention may be further carried out by simple chromatography of the active compound mixture on a CM-cellulose column in the H.sup.+ form, using distilled water without any additives. The active eluate, which is collected in fractions, is lyophilised.

The good anti-microbial (e.g. antibacterial) activity of the compound according to the invention is demonstrated by in vitro and in vivo tests.

In the agar dilution test according to the internationally customary test (American National Committee for Clinical Laboratory Standards=NCCLS), in vitro activity is found against Enterobacteriaceae, for example E. coli 14 and E. coli C 165.

An ED.sub.100 (complete cure) is found in vivo for the white mouse, at 3 mg of antibiotic/kg of body weight, in the case of infection with E. coli Newmann; therapy: application once, 30 minutes after infection, subcutaneously.

As stated above, the invention also relates to the use in medicine as anti-microbial agents of the compounds of the invention.

The present invention provides a pharmaceutical composition containing as active ingredient a compound of the invention in admixture with an inert pharmaceutical carrier, e.g. a solid or liquefied gaseous diluent, or in admixture with a liquid diluent other than a solvent of a molecular weight less than 200 (preferably less than 350) except in the presence of a surface active agent.

The invention further provides a pharmaceutical composition containing as active ingredient a compound of the invention in the form of a sterile and/or physiologically isotonic aqueous solution.

The invention also provides a medicament in dosage unit form comprising a compound of the invention.

The invention also provides a medicament in the form of tablets (including lozenges and granules), dragees, capsules, pills, ampoules or suppositories comprising a compound of the invention.

"Medicament" as used in this Specification means physically discrete coherent portions suitable for medical administration. "Medicament in dosage unit form" as used in this Specification means physically discrete coherent units suitable for medical administration each containing a daily dose or a multiple (up to four times) or submultiple (down to a fortieth) of a daily dose of the compound of the invention in association with a carrier and/or enclosed within an envelope. Whether the medicament contains a daily dose or, for example, a half, a third or a quarter of a daily dose will depend on whether the medicament is to be administered once or, for example, twice, three times or four times a day respectively.

The pharmaceutical composition according to the invention may, for example, take the form of ointments, gels, pastes, creams, sprays (including aerosols), lotions, suspensions, solutions and emulsions of the active ingredient in aqueous or non-aqueous diluents, syrups, granulates or powders.

The diluents to be used in pharmaceutical compositions (e.g. granulates) adapted to be formed into tablets, dragees, capsules and pills include the following: (a) fillers and extenders, e.g. starch, sugars, mannitol, and silicic acid; (b) binding agents, e.g. carboxymethyl cellulose and other cellulose derivatives, alginates, gelatine and polyvinyl pyrrolidone; (c) moisturizing agents, e.g. glycerol; (d) disintegrating agents, e.g. agar-agar, calcium carbonate and sodium bicarbonate; (e) agents for retarding dissolution e.g. paraffin; (f) resorption accelerators, e.g. quaternary ammonium compounds; (g) surface active agents, e.g. cetyl alcohol, glycerol monostearate; (h) adsorptive carriers, e.g. kaolin and bentonite; (i) lubricants, e.g. talc, calcium and magnesium stearate and solid polyethyl glycols.

The tablets, dragees, capsules and pills formed from the pharmaceutical compositions of the invention can have the customary coatings, envelopes and protective matrices, which may contain opacifiers. They can be so constituted that they release the active ingredient only or preferably in a particular part of the intestinal tract, possibly over a period of time. The coatings, envelopes and protective matrices may be made, for example, of polymeric substances or waxes.

The ingredient can also be made up in microencapsulated form together with one or several of the above-mentioned diluents.

The diluents to be used in pharmaceutical compositions adapted to be formed into suppositories can, for example, be the usual water-soluble diluents, such as polyethylene glycols and fats (e.g. cocoa oil and high esters (e.g. C.sub.14 -alcohol with C.sub.16 -fatty acid)) or mixtures of these diluents.

The pharmaceutical compositions which are ointments, pastes, creams and gels can, for example, contain the usual diluents, e.g. animal and vegetable fats, waxes, paraffins, starch, tragacanth, cellulose derivatives, polyethylene glycols, silicones, bentonites, silicic acid, talc and zinc oxide or mixtures of these substances.

The pharmaceutical compositions which are powders and sprays can, for example, contain the usual diluents, e.g. lactose, talc, silicic acid, aluminium hydroxide, calcium silicate, and polyamide powder or mixtures of these substances. Aerosol sprays can, for example, contain the usual propellants, e.g. chlorofluorohydrocarbons.

The pharmaceutical compositions which are solutions and emulsions can, for example, contain the customary diluents (with, of course, the above-mentioned exclusion of solvents having a molecular weight below 200 except in the presence of a surface-active agent), such as solvents, dissolving agents and emulsifiers; specific examples of such diluents are water, ethyl alcohol, isopropyl alcohol, ethyl carbonate, ethyl acetate, benzyl alcohol, benzyl benzoate, propylene glycol, 1,3-butylene glycol, dimethylformamide, oils (for example ground nut oil), glycerol, tetrahydrofurfuryl alcohol, polyethylene glycols and fatty acid esters of sorbitol or mixtures thereof.

For parenteral administration, solutions and emulsions should be sterile, and, if appropriate, blood-isotonic.

The pharmaceutical compositions which are suspensions can contain the usual diluents, such as liquid diluents, e.g. water, ethyl alcohol, propylene glycol, surface-active agents (e.g. ethoxylated isostearyl alcohols, polyoxyethylene sorbite and sorbitane esters), microcrystalline cellulose, aluminium metahydroxide, bentonite, agar-agar and tragacanth or mixtures thereof.

All the pharmaceutical compositions according to the invention can also contain colouring agents and preservatives as well as perfumes and flavouring additions (e.g. peppermint oil and eucalyptus oil) and sweetening agents (e.g. saccharin).

The pharmaceutical compositions according to the invention generally contain from 0.1 to 99.5% usually from 0.5 to 95% of the active ingredient by weight of the total composition.

In addition to a compound of the invention, the pharmaceutical compositions and medicaments according to the invention can also contain other pharmaceutically active compounds.

Any diluent in the medicaments of the present invention may be any of those mentioned above in relation to the pharmaceutical compositions of the present invention. Such medicaments may include solvents of molecular weight less than 200 as sole diluent.

The discrete coherent portions constituting the medicament according to the invention will generally be adapted by virtue of their shape or packaging for medical administration and may be, for example, any of the following: tablets (including lozenges and granulates), pills, dragees, capsules, suppositories and ampoules. Some of these forms may be made up for delayed release of the active ingredient. Some, such as capsules, include a protective envelope which renders the portions of the medicament physically discrete and coherent.

The production of the above-mentioned pharmaceutical compositions and medicaments is carried out by any method known in the art, for example, by mixing the active ingredient(s) with the diluent(s) to form a pharmaceutical composition (e.g. a granulate) and then forming the composition into the medicament (e.g. tablets).

This invention further provides a method of combating the above-mentioned diseases in warm-blooded animals, which comprises administering to the animals a compound of the invention alone or in admixture with a diluent or in the form of a medicament according to the invention.

It is envisaged that these active compounds will be administered perorally, parenterally (for example intramuscularly, intraperitoneally, subcutaneously and intravenously), rectally or locally.

In general it has proved advantageous to administer amounts of from 0.1-100 mg/kg of body weight per day to achieve effective results. The preferred dose is 2-50 mg/kg body weight. Nevertheless, it can at times be necessary to deviate from those dosage rates, and in particular to do so as a function of the nature and body weight of the subject to be treated, the individual reaction of this subject to the treatment, the type of formulation in which the active ingredient is administered and the mode in which the administration is carried out, and the point in the progress of the disease or interval at which it is to be administered. Thus it may in some case suffice to use less than the above-mentioned minimum dosage rate, whilst other cases the upper limit mentioned must be exceeded to achieve the desired results. Where larger amounts are administered it can be advisable to divide these into several individual administrations over the course of the day.

The in vivo and in vitro activity of the compound of the present invention is further illustrated by the following Examples A and B. BAY i 3265 component B (iron-containing) MIC G              in .mu.g/ml ______________________________________ Escherichia coli T7 .ltoreq.0.2 Escherichia coli F14 .ltoreq.0.1 Escherichia coli N 0.2 Klebsiella 57 US .ltoreq.0.1 Klebsiella 63    =0.1 Staphylococcus   .ltoreq.0.2 aureus 133 ______________________________________

The determination of the minimum inhibitory concentration (MIC) was effected using an inoculator in the agar dilution process with a sowing density of 10.sup.4 per inoculation point. The MIC was the concentration at which no bacteria colonies grew. BAY i 3265 component B animal test (mice) ED.sub.100 after intra-peritoneal infection and subcutaneous Infecting germ  treatment in mg/kg ______________________________________ E. coli Neumann 0.5 E. coli 205 Kn  0.1 Klebsiella pneumoniae 63 0.2 Staphylococcus aureus 0.6 ______________________________________

The animals were infected with a quantity of bacteria, which quantity led to the death of the control animals during the course of 24 hours. The ED.sub.100 was the dose which allowed all infected and treated animals to survive.

The following Examples illustrate processes for the production of the compound of the present invention.

(a) The nutrient solution in which the production strain Streptomyces spec. WS 116 was cultivated in the pre-cultures was composed of 1% by weight of glucose, 1.3% of yeast extract, 0.05% of polyol and tap water. The pH was adjusted to 7.0 before the sterilisation. 4.times.1000 ml Erlenmeyer flasks, each of which contained 150 ml of this nutrient solution, were inoculated with the production strain and were incubated for 4 days at 28.degree. C. on a rotary shaking machine at 220 revolutions/minute. A second pre-culture, a laboratory fermenter which contained 20 liters of the above-mentioned nutrient solution, was inoculated with these pre-cultures and was incubated at 200 revolutions/minute, 10 liter of air/minute and 28.degree. C. for 2 days. A production fermenter was inoculated with 20 liters of this culture, the production fermenter containing 600 liters of nutrient solution having the following composition: 0.7% by weight of citric acid, 0.8% of yeast extract, 0.2% of de-fatted soya bean flour, 0.2% of corn-steep liquor and 0.05% of silicone in tap water. The pH of this nutrient solution was adjusted to 6.4 with potassium hydroxide solution, before the sterilisation. The incubation of the production culture was effected over 2 to 4 days at 26.degree. C., at a stirring rate of 50 revolutions/minute and an aeration of only 90 liters of air/minute. The fermentation was stopped at an optimum antibiotic inhibitory activity of the culture.

(b) 2.times.150 ml of the preculture were grown as indicated in Example 1 (a). These precultures were used for inoculating a 10 liter production fermenter, the nutrient solution of which, prepared in tap water, contained the following composition: 0.7% by weight of citric acid, 0.8% by weight of yeast extract, 0.2% by weight of defatted soya bean flour, 0.2% by weight of corn-steep liquor, 0.3% by weight of L-ornithine, 0.1% by weight of L-serine and 0.05% by weight of silicone.

All constituents, except for ornithine and serine, were sterilised, as customary, in the culture vessel. A pH value of 6.4 was established before the sterilisation. Ornithine and serine, dissolved in distilled H.sub.2 O, were added, after sterile filtration, to the mixture.

The incubation of the production culture was effected over 2 to 4 days at 26.degree. C., at a stirring rate of 200 revolutions/minute and an aeration of only 1.5 liters of air/minute. The fermentation was stopped at an optimum antibiotic inhibitory activity of the supernatant liquor of the culture.

4000 liters of culture broth (pH=9.06) were adjusted to pH 6.2 with 50 l of 1:1 dilute HCl. 400 g of FeCl.sub.3.6H.sub.2 O were added to the broth, the latter was stirred and 25 liters of dilute NaOH were then added, whilst stirring, until a pH of 7 was obtained. The mixture was then separated at 200 to 250 l/h in a Westphalia separator. The supernatant liquor was introduced through a 30.times.70 cm column filled with "Lewatit" OC 1031 (Trade Mark of a non-specific adsorption resin of BAYER AG) and the permeate was conducted away as waste since it was inactive. The column was washed with 1000 liters of deionised water; the wash liquor was inactive and was discarded. The column was now washed with 1000 liters of 15% methanol, and this inactive wash liquor was also discarded. The activity was now eluted from the column using 50% methanol, and 100 liter fractions were collected. The active eluates 2 and 3 were combined, concentrated in a thin layer evaporator to approximately 20 liters and then lyophilised. 342 g of crude product of the compound according to the invention, with a content of approximately 2.5% (components B according to the invention and other antibiotic compound-component A), were obtained.

The above crude substance was dissolved in 6 liters of H.sub.2 O and 25 ml of 50% strength FeCl.sub.3 solution were added to the solution, whilst stirring. The precipitate which formed was centrifuged off after stirring for 15 minutes (Hettich Rota Magna centrifuge, 1.5 liter beaker, 30 minutes, 4000 rpm). The supernatant liquor was introduced, under the influence of gravity, over an 8.times.45 cm high column filled with SP-"Sephadex" C 25 Fe.sup.3+. The flow rate was 4 liters per hour. The black coloured column was rinsed with 5 liters of distilled H.sub.2 O, followed by 10 liters of 0.2M NaH.sub.2 PO.sub.4 /0.3NaCl buffer. Permeate and wash liquor contained less than 5% of the introduced antibiotic activity. The column which was then only pale, brown coloured was then eluted with 0.2M NaH.sub.2 PO.sub.4 /0.3M NaCl/0.05M ethylenediaminetetraacetic acid (flow rate 2 to 3 l/h), and the column eluate was collected fractionally in 500 ml portions. The active fractions 6 to 14 were combined and were introduced over a 5.times.40 column filled with "Lewatit" OC 1031. The flow rate was 3 l/h. The column was then washed with distilled water until no Cl.sup.- could be detected, using AgNO.sub.3, in the column eluate (approximately 6 liters, flow rate 5 l/h). The column was then eluted with 3 liters of 90% methanol, which was collected in a batch, concentrated and lyophilised. Yield: 6.74 g, 82.6% of BAY i3265 component A and component B.

Half the yield from Example 2 (=3.37 g) were dissolved in 100 ml of distilled H.sub.2 O. The conductivity was 210 .mu.S.

The solution was introduced onto a 5.times.30 cm column filled with CM-cellulose in the H.sup.+ form (CM-cellulose C 52, Messrs. Whatmann). The column was developed with distilled water, at a flow rate of 840 ml/h. The eluate was fractionated on the basis of the refraction curve, conductivity curve and extraction curve. First runnings (inactive) of 980 mg were obtained.

Fractions 2 to 8 combined comprised the compound according to the invention, BAY i 3265 component B.

## Claims

1. A process for the production of an iron-containing or iron-free antibiotic compound which, in the iron-free form, is of the formula ##STR4##

2. A process according to claim 1, in which an iron salt is present as a mineral salt.

3. A process according to claim 2, in which 0.01% by weight of FeCl.sub.3 is present in the nutrient medium.

4. A process according to claim 1, in which isolation is effected by binding to a non-specific adsorption resin and desorbing with mixtures composed of water and an organic solvent.

5. A process according to claim 4, in which an iron salt is added, before the adsorption, to the culture broth.

6. A process according to claim 6, in which the iron salt is present in a concentration of 0.05 to 0.2 g/l of culture broth.

7. A process according to claim 1, in which the antibiotic is isolated by subjecting it in the Fe.sup.3+ form to chromatography over a cation exchanger in a Fe.sup.3+ -containing column, eluting inactive accompanying substances with a buffer of high ionic strength and eluting the antibiotic with the same buffer and an additive of an iron complex-forming agent.

8. A process according to claim 7, in which the product obtained according to claim 10 is subjected to chromatography over a CM-cellulose column in the H.sup.+ form and is fractionally eluted with water.

9. A process according to claim 1, in which the fermentation is carried out in a nutrient solution which contains citric acid as the main carbon source, complex nitrogen sources and the aminoacids L-ornithine and L-serine.

10. A process according to claim 9 in which the complex nitrogen sources are selected from yeast extract, soya bean flour and corn-steep liquid.

11. A process according to claim 9 in which the L-ornithine and L-serine are added in a weight ration of 3:1.

12. A process according to claim 4, in which the fermentation is carried out in a completely synthetic nutrient solution which contains, in addition to mineral salts, citric acid as the main carbon source and L-arginine as the only nitrogen source.

13. A process according to claim 2, characterised in that, in order to increase the yield, a mixture of citric acid, L-arginene and salts is further fed to a nutrient solution at such rates that a constant pH value is maintained.

14. A process according to claim 1, wherein said naturally-occurring complex substance is selected from the group consisting of peptones, corn-steep liquor, soya bean flour, meat extracts and yeast extracts.

15. A process according to claim 1, wherein said carbohydrate is selected from the group consisting of starch, dextrins, meltose, cane sugar, glucose and xylose.

16. A process according to claim 1, wherein said sugar alcohols are selected from the group consisting of mannitol and glycerol.

17. A process according to claim 1, wherein said carboxylic acid is selected from the group consisting of citric acid, maleic acid and acetic acid.

18. A process according to claim 1, wherein said amino acids are selected from the group consisting of glutamic acid, aspartic acid, argenine, lysine, ornithine and serine.

19. A culture consisting essentially of Streptomyces species WS 116 (DMS 1692), said species having the ability to produce an iron-containing or iron-free antibiotic compound which, in the iron-free form, is of the formula ##STR5##

20. A culture of claim 19 in biologically pure form.