TW200409816A - Antibiotics GE 81112 factors A,B,B1, pharmaceutically acceptable salts and compositions, and use thereof - Google Patents

Antibiotics GE 81112 factors A,B,B1, pharmaceutically acceptable salts and compositions, and use thereof Download PDF

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TW200409816A
TW200409816A TW91135061A TW91135061A TW200409816A TW 200409816 A TW200409816 A TW 200409816A TW 91135061 A TW91135061 A TW 91135061A TW 91135061 A TW91135061 A TW 91135061A TW 200409816 A TW200409816 A TW 200409816A
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antibiotic
factor
ppm
supplement
acid
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TW91135061A
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Enrico Selva
Flavia Marinelli
Daniele Losi
Linda Cavaletti
Ameriga Lazzarini
Alessandre Marazzi
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Biosearch Italia Spa
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Abstract

The invention relates to an antibiotic substances of microbial origin, arbitrarily denominated antibiotic GE 81112 factor A, factor B1 and factor B, which is produced by fermentation of Streptomyces sp. DSMZ 14386, the pharmaceutically acceptable salts and compositions thereof, and their use as an antibacterial agent having inhibitory activity versus susceptible microbes.

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200409816 瞧纖麵- 本發明係有關一種微生物來源之抗生素物質,任意定名 爲GE81112因子A、GE81112因子B以及GE81112因子 B !,該等因子以任一種比例之混合物,藥物可容許鹽及其 組成物,及其用作爲抗菌劑之用途。 本發明之另一目的爲一種製備 GE 81112因子 A、GE 81112因子B以及GE 81112因子B!之方法,該等因子以 任一種比例之混合物,後文係以報告G E 8 1 1 1 2化合物或 GE 81112抗生素之名報告。 菌株與發酵 鏈絲菌DSMZ 1 43 86原先以內部代碼GE 81112表示,係 由土壤樣本分離且於2 0 0 1年7月1 6日遵照布達佩斯條約 的規定以 DSMZ 之名寄存(Deutsche Sammlung von Mikroorganismen und Zellkulturen GmbH, Mascheroder Weg lb,D-38124 Braunschweig,德國)。該菌株帶有存取 編號 D S Μ Z 1 4 3 8 6。 GE 81112化合物的製造方式係經由培養可製造該等化 合物之鏈絲菌菌株亦即鏈絲菌D SMZ 1 43 8 6或其維持可製 造該等GE 81112化合物之遺傳能力之變異株或突變株; 由液態培養基分離所得抗生素;純化分離之抗生素;以及 藉層析術手段分離抗生素之三種因子A、B及Βι或其混合 物。總而言之,較佳化合物GE 8 1 1 1 2之製造方法係於有 氧條件下於含有可同化碳、氮及無機鹽來源之水性營養培 養基進行,且利用層析技術純化所得化合物。可使用多種 發酵領域常用之營養培養基,但以某些培養基爲佳。 6 312/發明說明書(補件)/92-02/91135061 200409816 較佳碳源爲葡萄糖、木糖、澱粉、果糖、甘油等。較佳 氮源爲大豆粉、蛋白陳、肉萃取物、酵母萃取物、胰蛋白 腺、胺基酸、水解酪蛋白等。可摻混於培養基之無機鹽類 又包括習知可產生鈉、鉀、鐵、鋅、鈷、鎂、鈣、銨、氯 陰離子、碳酸根、硫酸根、磷酸根、硝酸根等離子之可溶 性鹽類。較佳可產生G E 8 1 1 1 2化合物之菌株於發酵管或振 搖瓶內前培養,然後培養菌用以接種發酵瓶來製造大量發 酵物質。前培養用之培養基可與大量發酵時使用的培養基 相同,但也可使用其它培養基。可產生GE81112化合物之 種系可於20 °C至40 °C且較佳221至37 t之溫度生長。溫 度高於4 4 °C時未見生長。 發酵期間可於敏感微生物之生物檢定分析及/或HPLC分 析監視GE 81 1 12因子。GE 81 1 12化合物之最大產量通常 係出現於約發酵20小時後至發酵80小時。 化合物GE 81 1 12係經由培養鏈絲菌DSMZ 1 43 86或其可 製造化合物GE 8 1 1 1 2之變異株或突變株生產,且化合物係 製造於液態培養基中。 鏈絲菌D S Μ Z 1 4 3 8 6之形熊璺特徵 鏈絲菌 DSMZ 1 4 3 8 6於多種標準土壤培養基之生長良 好。使用於十分之一強度腐植酸培養基生長的培養菌進行 顯微鏡檢以及細胞尺寸的測定(Η . Ν ο η 〇 m u r a,1 9 8 4 - D e s i g η of a new medium for isolation of soil a c t i η o m y c e t e s. The Actinomy cetes 18 · 2 0 6-209) o 於液態培養(V6培養基,組成參考實施例1),於28 t生 長2日後未觀察得菌絲體碎片。 312/發明說明書(補件)/92-02/91135061 200409816 於28°C培養15日後於HV/2瓊脂進行顯微鏡檢,顯示既 未破碎也未廣闊分支的營養菌絲體。需氧菌絲體也未廣闊 分支。需氧菌絲產生含有多於10個(大半大於20個)孢子 之鏈;排列成簡單但非緊密的3至5個迴圈螺旋。孢子形 狀包含球體(平均直徑約0.9微米)至卵形或圓柱形(0.8至 0.9微米X 1.1至1.3微米)。 _絲蘭DSMZ 143S(S之培養特徵 鏈絲菌DSMZ 1 43 86於V6液態培養基(培養基組成參考 實施例1)生長2日。藉離心收穫菌絲體,以無菌食鹽水洗 3次,然後稀釋獲得適當接種物。懸浮液以十字影線方式 劃線培養於Shirling及Gottlieb推薦之各種培養基上(E. B. Shirling and D. Gottlieb, 1 966 一 Method for Characterization of S treptomy ces species - Int. J. Syst. Bacteriol., 16., 313-340)以及Waksman推薦的若千培養基上(WaksmanS.A., 19 61 - The Actinomycetes - The Williams and Wilkins Co·, Baltimore· Vol 2_,PP 328-334)。 使用多種碳水化合物作爲碳源及能源之能力係於IS P8 培養基(Shirling及Gottlieb,同文)測定,該培養基含有終 濃度1 % (w/v)之碳源。氯化鈉忍受性以及於不同溫度生長 的能力係於IS P2培養基測定。全部培養基皆於28 °C接種 21日;除非另行載明,否則此處說明係指14日。於自然 光下使用 Mae ι·ζ及Paul之色圖於自然光下評估色彩(A. Maerz and M. R. Paul, 1950 - A Dictionary of Colour, 2nd edition· McGraw-Hill Book Co. Inc·,New York)。還原硝酸 鹽成爲亞硝酸鹽之能力係於2 8 °C於有氧條件下培養隔夜 8 312/發明說明書(補件)/92-02/91135061 200409816 後使用巴克多(Bacto)亞硝酸鹽試紙(迪汗 遵照製造商提示之方法於硝酸鹽液態培 評級。 鏈絲菌D S Μ Z 1 4 3 8 6菌株之生長、菌 需氧菌絲體的顏色及色素的製造係記錄 養基皆出現生長,但G 1瓊脂除外,G 1 氮源的培養基。於任何使用的培養基皆 沉著現象。該種系之生理特徵示於表 1 4 3 8 6顯示可生長至7%(w/v)氯化鈉;於 以上之濃度,該菌株之需氧菌絲體不會 明膠液化以及乳蛋白踱化能力只能微弱 碳水化合物來生長之能力顯示於表III。 的基礎培養基上,觀察得營養菌絲體及 有限。於全部使用的碳源皆生長白色需 除外。 312/發明說明書(補件)/92-02/91135061 I 可(Difco)公司), 養基(ISP8培養基) 落外觀、基質以及 於表I。於全部培 瓊脂爲唯一含無機 未顯示特徵性色素 II。鏈絲菌DSMZ 1 % (w / v )氯化鈉及 分化。生長7日後 檢測得。利用多種 於未添加任何碳源 需氧菌絲體的生長 氧菌絲體,葡萄糖 9 表I:鏈絲菌DSMZ 14386之生長特徵200409816 Look at the fiber surface-The present invention relates to an antibiotic substance of microbial origin, arbitrarily named GE81112 factor A, GE81112 factor B, and GE81112 factor B! These factors are mixtures in any ratio. The drug allows the salt and its composition , And its use as an antibacterial agent. Another object of the present invention is a method for preparing GE 81112 factor A, GE 81112 factor B, and GE 81112 factor B !. These factors are in a mixture of any ratio, and the following is to report GE 8 1 1 1 2 compounds or GE 81112 Antibiotic Name Report. Strains and Streptomyces spp. DSMZ 1 43 86 were originally expressed as internal code GE 81112, which were isolated from soil samples and deposited under the name of DSMZ on July 16, 2001 in accordance with the provisions of the Budapest Treaty (Deutsche Sammlung von Mikroorganismen und Zellkulturen GmbH, Mascheroder Weg lb, D-38124 Braunschweig, Germany). This strain carries the accession number DSM Z 1 4 3 8 6. The manufacturing methods of GE 81112 compounds are Streptomyces strains capable of manufacturing these compounds, that is, Streptomyces D SMZ 1 43 8 6 or variants or mutants that maintain the genetic ability to produce these GE 81112 compounds; The obtained antibiotics are separated from the liquid culture medium; the isolated antibiotics are purified; and the three factors A, B, and Bι or the mixture thereof are separated by chromatography. All in all, the method for producing the preferred compound GE 8 1 1 12 is performed under aerobic conditions on an aqueous nutrient medium containing assimilable carbon, nitrogen and inorganic salt sources, and the resulting compound is purified by chromatography. A variety of nutrient media commonly used in fermentation can be used, but certain media are preferred. 6 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816 Preferred carbon sources are glucose, xylose, starch, fructose, glycerol and the like. Preferred nitrogen sources are soy flour, protein age, meat extract, yeast extract, trypsin gland, amino acid, hydrolyzed casein, and the like. The inorganic salts that can be blended into the culture medium also include the soluble salts that are conventionally known to produce sodium, potassium, iron, zinc, cobalt, magnesium, calcium, ammonium, chloride anions, carbonate, sulfate, phosphate, nitrate and other ions. . Preferably, a strain capable of producing the G E 8 1 1 1 2 compound is cultured in a fermentation tube or a shake flask, and then the culture bacteria are used to inoculate the fermentation bottle to produce a large amount of fermentative substances. The medium used for the pre-cultivation may be the same as that used for the mass fermentation, but other mediums may be used. The germline that produces the GE81112 compound can be grown at a temperature of 20 ° C to 40 ° C, preferably 221 to 37 t. No growth was seen above 4 4 ° C. GE 81 1 12 factor can be monitored during bioassay analysis and / or HPLC analysis of sensitive microorganisms during fermentation. The maximum yield of the GE 81 1 12 compound usually occurs after about 20 hours to 80 hours of fermentation. The compound GE 81 1 12 was produced through the culture of Streptomyces sp. DSMZ 1 43 86 or a mutant or mutant strain thereof capable of producing the compound GE 8 1 1 12 and the compound was produced in a liquid medium. Characteristics of Streptomyces D S M Z 1 4 3 8 6 The characteristics of ursinus streptomyces DSMZ 1 4 3 8 6 grow well in a variety of standard soil media. Microscopic examination and cell size determination using cultured bacteria grown on a tenth-strength humic acid medium (Η. Ν ο η 〇mura, 1 9 8 4-D esig η of a new medium for isolation of soil acti η omycete s. The Actinomy cetes 18 · 2 0 6-209) o In liquid culture (V6 medium, composition reference example 1), no mycelial debris was observed after 2 days of growth at 28 t. 312 / Inventory (Supplement) / 92-02 / 91135061 200409816 Microscopic examination of HV / 2 agar after 15 days incubation at 28 ° C revealed vegetative mycelia that were neither broken nor broadly branched. Aerobic mycelia are also not extensively branched. Aerobic mycelia produce chains containing more than 10 (mostly more than 20) spores; arranged in simple but non-tight 3 to 5 loop spirals. The spore shape includes spheres (average diameter of about 0.9 microns) to oval or cylindrical (0.8 to 0.9 microns x 1.1 to 1.3 microns). _ Yucca DSMZ 143S (culture characteristic of S. streptococcus DSMZ 1 43 86) was grown in V6 liquid medium (medium composition reference example 1) for 2 days. Mycelia were harvested by centrifugation, washed with sterile saline 3 times, and then diluted to obtain Appropriate inoculum. Suspension was cross-hatched and cultured on various media recommended by Shirling and Gottlieb (EB Shirling and D. Gottlieb, 1 966-Method for Characterization of S treptomy ces species-Int. J. Syst. Bacteriol ., 16., 313-340) and Waksen's medium recommended by Waksman (Waksman S.A., 19 61-The Actinomycetes-The Williams and Wilkins Co., Baltimore · Vol 2_, PP 328-334). Use a variety of carbon water The ability of compounds to act as a carbon source and energy source was determined in an IS P8 medium (Shirling and Gottlieb, same article), which contains a carbon source at a final concentration of 1% (w / v). Sodium chloride tolerance and ability to grow at different temperatures It is measured on IS P2 medium. All mediums are inoculated at 28 ° C for 21 days; unless otherwise stated, the explanation here refers to the 14th. Use the color map of Mae ι and Paul under natural light. Evaluating color under natural light (A. Maerz and MR Paul, 1950-A Dictionary of Colour, 2nd edition · McGraw-Hill Book Co. Inc ·, New York). The ability to reduce nitrate to nitrite is at 2 8 ° C After overnight cultivation in aerobic conditions 8 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816 Bacto nitrite test strips were used (Dihan followed the manufacturer's method to grade the nitrate liquid culture. The growth of Streptomyces DS Μ Z 1 4 3 8 6 strains, the production of aerobic mycelia, and the production of pigments have recorded that growth of nutrients has occurred, with the exception of G 1 agar, G 1 nitrogen source medium. Any The culture media used are all calm. The physiological characteristics of this line are shown in Table 1 4 3 8 6 shows that it can grow to 7% (w / v) sodium chloride; at the above concentrations, the aerobic mycelium of this strain is not The ability of gelatin liquefaction and milk protein peptidation to grow only weak carbohydrates is shown in Table III. The basal medium was observed, and the vegetative mycelium was limited. Except when all carbon sources used grow white. 312 / Invention Specification (Supplement) / 92-02 / 91135061 I (Difco), culture medium (ISP8 medium), appearance, matrix, and Table I. In all cultures, the agar is the only one that contains inorganic pigments and does not show characteristic pigment II. Streptomyces DSMZ 1% (w / v) sodium chloride and differentiation. Detected after 7 days of growth. Utilizing a variety of aerobic mycelium growth without adding any carbon source Aerobic mycelium, glucose 9 Table I: Growth characteristics of Streptomyces DSMZ 14386

培養基 生長與形態 反色代碼 ISP 2酵母萃取物-麥芽 萃取物瓊脂 生長茂密,盤旋,接近劃線培養的末端變成硬皮;橙/褐色;生長邊緣褪色。白色需氧 菌絲體簇。未產生可溶性色素。濃土味。 12L9 ISP3燕麥糊瓊脂 生長茂密帶有光滑面;乳黃色。白需氧菌絲體薄層只出現於接近生長邊緣。未產生可溶 性色素。 11H3 ISP 4無機鹽-澱粉瓊脂 生長茂密,盤旋,接近劃線培養的末端變成硬皮;黃色。出現白色需氧菌絲體,鬆軟。 未製造可溶性色素。濃土味。 10F3 ISP5甘油·天冬醯胺瓊 脂 分開生長至生長良好;無色至淺黃色;邊緣羽毛狀且褪色。出現細白色菌絲體,隨著老 化轉成帶粉紅色(10A2) 〇未產生可溶性色素。 10G2 ISP 6蛋白难-酵母萃取 物-鐵瓊脂 分開生長,接近劃線培養末端起皺;菌落直徑小;由劃線區的展開少;黏質;淺褐色。 未產生需氧菌絲體。菌絲體顏色略深。 11 J3 ISP7酪胺酸瓊脂 生長茂密,盤旋,接近劃線培養末端變成硬皮;褐色;邊緣羽毛狀且褪色。白色需氧菌 絲體之產生良好,粉狀。產生褐色可溶性顏料。淡土味。 14L9 SYE澱粉獅萃取物 瓊脂 生長茂密’盤旋,接近劃線培養的末端變成硬皮;黃褐色;寬邊、邊緣羽毛狀且褪色。 白色稀疏需氧菌絲體的生長有限。未產生可溶性色素。淡土味。 10L7 CZ-GLU 柴派克 (Czapeck)-葡萄糖瓊脂 分開生長至生長良好,接近劃線培養的末端產生硬皮;菌落直徑小;乳白-淺褐色:邊 緣羽毛狀。白色稀疏需氧菌絲體的生長受限制。未產生可溶性色素。淡土味。 12H6 GAUZE 1瓊脂 不生長 • GAUZE 2瓊脂 生長良好,劃線培養末端稀疏起皺且爲硬皮狀,劃線培養之交叉點爲平坦;黃/褐色。 平坦區極少出現稀疏白需氧菌絲體。菌絲體顏色略深。 11L6 NA營養瓊脂 分開生長至生長良好 '光滑;乳黃色。未產生需氧菌絲體。未產生可溶性色素。 11L2 SE 土壤萃取物瓊脂 幾乎無目測可見之營養菌絲體;無色;由劃線極少展開。未產生需氧菌絲體《•未產生可 溶性色素。 ND HV/2W直酸·維生素瓊 脂 營養菌絲體之生長良好,穿透深入瓊脂;深褐色:邊緣羽毛狀。存在有白色需氧菌絲體, 粉狀。 ND 312/發明說明書(補件)/92-02/91135061 10 200409816 菌DSMZ 1 4 3 8 6之生理特徵 — ------ 試驗 反應 澱粉水解 ~———— 陽性 酪蛋白水解 陰性 蘋果酸鈣消化 陽性 石蕊乳蛋白睐化 陽性(弱) 石蕊乳凝結 陰性 明膠液化 陽性(弱) 酪胺酸反應 陽性 於ISP6硫化氫的產生 陰性 (4日):+乙酸錯試紙 弱陽性 硝酸鹽的還原 陰性 氯化鈉忍受性 ^7% 表III:鏈絲菌D S Μ Z 1 4 3 8 6對碳源之利用 碳源 營養菌絲體生長 需氧菌絲體生長 阿拉伯糖 + + /- 果糖 + + + + 肌糖醇 + + /- 甘露醇 + + + 棉籽糖 + + + + 鼠李糖 + + + + 蔗糖 + /- 木糖 + + + + 葡萄糖 + + - + +生長良好;+生長中度;-乏/無生長 312/發明說明書(補件)/92-02/91135061 200409816 §車絲菌DSMZ 1 4 3 8 6之化學分類特徵 鏈絲菌D S Μ Z 1 4 3 8 6生長於沙頓(S a u t ο η )培養基4週,然 後收穫菌絲體,菌絲體以無菌蒸餾水洗滌三次然後凍乾。 二胺基庚二酸(DAP)之立體異構形式係根據 Staneck及 Roberts 之方法測定(J.L. Staneck and G.D. Roberts, Simplified approach to identification of aerobic actinomy cetes by thin-layer chromatography, Appl. Microbiol.丛,226-23 1,1 9 7 4)。 爲了萃取脂肪酸,濕生物質塊使用 Miller方法(L.T. Miller, A single deri vatization method for bacterial fatty acid methyl esters including hydroxy acids, J. Clin. Microbiol.过,5 84 -5 8 6,1 98 2)之略爲修改方法萃取(L.D· Kuykendall, M. A. Roy, J. J.〇’Neill and T.E. Devine,Fatty acid, antibiotic resistance, and deoxyribonucleic acid homology groups of Bradyrhizobium j aponicium, Int. J. System. Bact. 38_, 3 5 1 - 3 6 1, 1 9 8 8)。分析係如 R.M.Medium Growth and Morphology Inverse Color Code ISP 2 Yeast Extract-Malt Extract Agar Growing densely, circling, becoming crusty near the end of the streak culture; orange / brown; discoloration of growth edges. White aerobic mycelium clusters. No soluble pigments were produced. Thick earthy flavor. 12L9 ISP3 oatmeal agar thick and smooth with smooth surface; cream yellow. A thin layer of white aerobic mycelia appears only near the growth edge. No soluble pigments were produced. 11H3 ISP 4 inorganic salt-starch agar grows densely, spirals, and becomes crusty near the end of the streak culture; yellow. White aerobic mycelia appear, fluffy. No soluble pigments were made. Thick earthy flavor. 10F3 ISP5 glycerol-asparagine agar Separately grown to good growth; colorless to pale yellow; feathery and faded at the edges. Fine white mycelia appeared and turned pinkish (10A2) with aging. No soluble pigment was produced. 10G2 ISP 6 protein difficulty-yeast extract-iron agar Separate growth, wrinkling near the end of the streak culture; small colony diameter; less expansion from the streak area; sticky; light brown. No aerobic mycelium was produced. Mycelium is slightly darker. 11 J3 ISP7 tyrosine agar grows densely, spirals, and becomes crusty near the end of the culture line; brown; feathery and faded at the edges. The production of white aerobic mycelia is good and powdery. A brown soluble pigment was produced. Light earthy taste. 14L9 SYE starch lion extract agar grows densely circling, becomes hard crust near the end of the streak culture; yellow-brown; broad-edged, feathery and faded at the edges. Limited growth of white sparse aerobic mycelia. No soluble pigments were produced. Light earthy taste. 10L7 CZ-GLU Czapeck-glucose agar Separately grown to good growth, producing crusts near the end of the streak culture; small colony diameter; opalescent-light brown: feathered edges. Growth of white sparse aerobic mycelia is restricted. No soluble pigments were produced. Light earthy taste. 12H6 GAUZE 1 agar does not grow • GAUZE 2 agar grows well, the end of the streak culture is sparse and wrinkled and crusty, the intersection of the streak culture is flat; yellow / brown. Sparse white aerobic mycelia rarely occur in flat areas. Mycelium is slightly darker. 11L6 NA Nutritional Agar Separately grows well to grow 'smooth; creamy yellow. No aerobic mycelium was produced. No soluble pigments were produced. 11L2 SE Soil Extract Agar There are almost no vegetative mycelia visible by sight; colorless; rarely spread by streaking. No aerobic mycelium was produced "• No soluble pigment was produced. ND HV / 2W straight acid · vitamin agar The growth of vegetative mycelia is good, penetrating deep into the agar; dark brown: feathery edges. Presence of white aerobic mycelia, powdery. ND 312 / Invention Specification (Supplement) / 92-02 / 91135061 10 200409816 Physiological characteristics of DSMZ 1 4 3 8 6 ------- Test reaction starch hydrolysis ~ -------- Positive casein hydrolysis negative malate Calcium digestion positive litmus milk protein positive (weak) litmus milk coagulation negative gelatin liquefaction positive (weak) tyrosine reaction positive than ISP6 hydrogen sulfide production negative (4th): + acetic acid test paper weak positive nitrate Reduction-negative sodium chloride tolerance ^ 7% Table III: Streptomyces DS M Z 1 4 3 8 6 Use of carbon source Carbon source nutrition Mycelium growth Aerobic mycelium growth Arabinose + + /-Fructose + + + + Inositol + + /-mannitol + + + raffinose + + + rhamnose + + + + sucrose + /-xylose + + + + glucose + + + + + good growth; + growing Degree; -Deficiency / No growth 312 / Invention specification (Supplement) / 92-02 / 91135061 200409816 § Chemical classification characteristics of Trichoderma DSMZ 1 4 3 8 6 Streptomyces DS MH Z 1 4 3 8 6 grows in sand (S aut ο η) medium for 4 weeks, then mycelia were harvested, the mycelia were washed three times with sterile distilled water and then Lyophilized. The stereoisomeric form of diaminopimelic acid (DAP) is determined according to the methods of Staneck and Roberts (JL Staneck and GD Roberts, Simplified approach to identification of aerobic actinomy cetes by thin-layer chromatography, Appl. Microbiol. Plex, 226 -23 1, 1, 9 7 4). In order to extract fatty acids, the wet biomass block uses the Miller method (LT Miller, A single deri vatization method for bacterial fatty acid methyl esters including hydroxy acids, J. Clin. Microbiol., 5 84 -5 8 6, 1 98 2). Extraction with slight modification (LD · Kuykendall, MA Roy, JJ〇'Neill and TE Devine, Fatty acid, antibiotic resistance, and deoxyribonucleic acid homology groups of Bradyrhizobium j aponicium, Int. J. System. Bact. 38_, 3 5 1 -3 6 1, 1 9 8 8). Analytical systems such as R.M.

Kroppenstedt 所述進行(R.M. Kroppenstedt, Ε· Stackebrandt and M. Goodfellow, Taxonomic revision of the actinomycete genera Actinomadura and Microtetraspora, System. Appl. Microbiol. J_i,1 48- 1 60,1 990),資料係使用微生物識別系 統檢驗(L.T· Miller,同文)。 鏈絲菌DSMZ 1 43 8 6菌株含有LL-二胺基庚二酸於胜肽 聚糖,不含黴菌酸。存在有異·以及反異-分支型脂肪酸, 而未檢測得任何羥基脂肪酸或1 0-甲基·分支脂肪酸,亦即 脂肪酸2c型鏈絲菌型。 12 312/發明說明書(補件)/92-02/91135061 200409816 鏈絲菌D S Μ Z 1 4 3 8 6菌株之識別 可製造化合物GE 8 1 1 1 2之菌株由於具有下列 化學特徵而定名於鏈絲菌: -形成分支但未分段的營養菌絲體。需氧菌絲 10個(大部分>20)節孢子之鏈; -根據Kroppenstedt,於細胞壁存在有LL·二胺 及 2c 型脂肪酸側繪(R.M. Kroppenstedt,Fatty menaquinone analysis of actinomy cetes and organisms, pp.1 7 3 - 1 9 9,in: Chemical Methods in Systematics,M. Goodfellow and D. E. Minnikin eds Accademic Press, 1985)。 如同其它微生物,可製造GE81112化合物之菌 有變化。例如該菌株之人工變異株及突變株可經 知多種突變原例如紫外光及例如亞硝酸、N-甲基 -N-亞硝基胍以及多種其它化學品處理獲得。鏈絲 1 4 3 8 6之全部天然及人工變異株及突變株其含有ΐ 8 111 2化合物之遺傳能力者被視爲相當於本發明 因而係屬於本發明之範圍。 抗生素可由發酵液之表面部分回收。 GE 8 1 1 1 2化合物之萃那及純仆 GE 8 1 1 1 2化合物由可製造微生物之發酵液回收 知技術進行,已知回收技術例如於佐劑存在下使 取,藉加入非溶劑、鹽或變更溶液之pH沉澱、 術、反相分選層析術、離子交換層析術、分子排 等。 312/發明說明書(補件)/92-02/91135061 形態學及 產生大於 基庚二酸 acid and related bacterial ;London, 株特徵也 由使用已 -Ν'硝基 菌 DSMZ 丁製造GE 之目的, 係根據已 用溶劑萃 分選層析 除層析術 13 200409816 由發酵液回收本發明之抗生素物質之程序包括藉離子 父換層析術萃取G E 8 1 11 2。根據此種程序,經過過爐後之 發酵液可與離子交換樹脂接觸。洗提可藉由變更pH或離 子強度進行。可方便地用於回收本發明化合物之離子交換 樹脂例如爲陰離子性及陽離子性離子交換樹脂,亦即由例 如合成聚合物(如聚苯乙烯、丙烯酸系聚合物)或天然聚合 物(例如纖維素、西法羅思(s e p h a r 〇 s e)聚合物、二氧化政) 之基體藉導入酸(例如C〇〇H、-SChH)或驗(例如_n(CH3)2、 -n + (ch3)3)官能基衍生所組成的樹脂。 前述樹脂例如爲朵威司(Dowex)50W樹脂(陶氏化學公司 (Dow Chemical Co·))、安伯萊特(Amberlite)IR-200 及 IR-120(羅門哈斯公司(Rohm&Haas))、PL-SCX 1000 以及 APL-SCX 4000 A(聚合物實驗室(Polymer Laboratories))、伊 索露(Isolute)SCX IST(國際吸附劑技術公司(International Sorbent Technology))、SP西法羅思快速流動及SP西法戴 思(Sephadex)G25(法瑪西亞生技公司(Pharmacia Biotech))。 回收抗生素物質之另一種程序包括吸附於適當基體 上,接著使用極性水可溶混溶劑或其混合物洗提,於減壓 下濃縮成爲水殘餘物,以及使用前述類型沉澱劑沉澱。可 於適當値調整pH。可方便用於回收本發明化合物之吸附基 體例如爲活性碳(例如達可(Darco) G60、諾瑞(Norit) CG1)、聚苯乙烯或混合聚苯乙烯-二乙烯苯樹脂(例如戴恩 (Diaion)HP20、三井化學公司;M112或S112陶氏化學公 司;安伯萊特XAD2或XAD4,羅門哈斯公司)、.丙烯酸系 樹脂(例如XAD7或XAD8,羅門哈斯公司)、酚系吸附劑(例 14 312/發明說明書(補件)/92-02/91135061 200409816 如朵萊特(DuolUe)X AD 761,羅門哈斯公司)、聚醯胺樹脂例 如聚己內醯胺、尼龍以及交聯聚乙烯基吡略啶酮(例如聚醯 胺-CC 6、聚醯胺-SC 6'聚醯胺-CC 6.6、聚醯胺-CC 6AC 及聚醯胺-SC 6AC,麥克琳娜吉(Macherey-Nagel)公司,西 德;PA400、烏爾(M.Woelm)公司 AG,西德;PVP-CL、亞 利敘(Aldrich)化學公司,西德)、孔隙經過控制之交聯葡萄 聚糖(例如西法戴思LH-20、法瑪西亞精細化學品公司)。 常用活性碳及/或聚苯乙烯樹脂,特佳爲戴恩HP 20樹脂(三 井化學公司)。 吸附於前述類別之吸附基體上也可利用離子(例如陽離 子)交換層析術作爲純化由發酵液回收粗產物之程序。 較佳由吸附基體洗提GE 81 1 12化合物之溶劑係依據特 定靜相決定。當使用活性碳時,洗提係藉由改變成爲酸性 pH洗提緩衝液達成,緩衝液典型含有水可溶混溶劑例如低 碳酮如丙酮或低碳醇如甲醇。如此水性混合物被調整爲適 當pH値。當使用聚苯乙烯樹脂、聚苯乙烯-二乙烯苯樹脂、 丙烯酸系樹脂或聚醯胺樹脂時較佳洗提劑爲水可溶混溶劑 或其水性混合物例如水與(Cl-C3)烷醇之混合物。 用於本案「水可溶混溶劑」一詞當未特別規定時意圖表 示業界目前對該詞的定義,表示一種溶劑其於使用條件下 可與水於合理寬廣之濃度範圍溶混且適合供預期用途。可 用於洗提本發明化合物之水可溶混有效溶劑例如爲低碳烷 醇如(ChCd醇如甲醇、乙醇及丙醇;苯基(Ci-Cd烷醇如苄 醇;低碳酮類如(C3-C4)酮類如丙酮及乙基甲基甲酮;環狀 醚類如二#烷及四氫呋喃;二醇類及其部分醚化產物例如 15 312/發明說明書(補件)/92-02/91135061 200409816 乙二醇、丙二醇以及乙二醇一甲醚;低碳醯胺類例如二甲 基甲醯胺及二乙基甲醯胺;乙酸、二甲亞硕及乙腈。 另一種由發酵液回收GE 81 1 12化合物之方法爲使用水 可溶混有機溶劑萃取GE 8 1 1 1 2化合物或其鹽,萃取時經由 將pH調整於適當値,及/或經由鹽化,經由添加可與可溶 於萃取溶劑之抗生素形成離子對之適當有機鹽。然後抗生 素例如藉添加沉澱劑而由濃縮萃取物沉澱。 用於本案「水不溶混溶劑」一詞意圖具有目前業界使用 的定義,表示~種溶劑於使用條件下略爲可溶混或實際不 可於水溶混。可用於由發酵液萃取本發明化合物之水不溶 混有機溶劑例如至少含4個碳原子之烷醇可爲線性、分支 或環狀例如正丁醇、1-戊醇、2-戊醇、3-戊醇、1-己醇、2-己醇、3 -己醇、3,3 -二甲基-1-丁醇、4 -甲基-1·戊醇、3·甲 基-1-戊醇、2,2-二甲基-3-戊醇、2,心二甲基-3-戊醇、4,4-二甲基-2-戊醇、5·甲基-2-己醇、1-庚醇、2·庚醇、5-甲基 •1·己醇、2-乙基-1-己醇、2-甲基-3-己醇、1-辛醇、2·辛醇、 環戊醇、2-環戊基乙醇、3-環戊基-1-丙醇、環己醇、環庚 醇、環辛醇、2,3-二甲基環己醇、4-乙基環己醇、環辛基 甲醇、6-甲基-5-庚烯-2-醇、1-壬醇、2-壬醇、1-癸醇、2-癸醇及3 -癸醇;含至少5個碳原子之酮類如甲基異丙基甲 酮、甲基異丁基甲酮、甲基正戊基甲酮、甲基異戊基甲酮 及其混合物。與G E 8 1 1 1 2化合物形成之方便離子對例如係 經由添加酸於適當pH獲得,例如磺酸以對甲苯磺酸、戊 烷磺酸、己烷磺酸、庚烷磺酸等爲代表;或羧酸以己酸、 庚酸、苯甲酸等爲代表。另外離子對可經由添加陽離子例 3 Π/發明說明書(補件)/92-〇2/91135061 200409816 如於適當pH之三乙基錢、四丁基錢等產生。 粗製G E 8 1 1 1 2化合物之純化可藉已知技術達成,但較佳 係利用層析術進行。方便地也可採用所謂之立體排除層析 技術而獲得良好結果。特別此項技術通常係使用孔隙經過 控制之交聯葡萄聚糖,其中大部分羥基已經經過烷化例如 西法戴思LH-2C (法瑪西亞精細化學公司)。 例如可採用中壓液相層析分離系統,於R P · 8或R P -1 8 官能化矽膠進行反相層析術且使用甲酸銨溶液洗提。由發 酵液分離之粗產物以及純化產物依據發酵及純化條件而 定,通常含有不等比例之單一 GE 81112因子人、31及B 混合物。 各別因子A、B及B!之分離及純化可方便地藉含有GE 8 1 1 1 2化合物混合物之製劑接受半製備性HPLC進行。 較佳用於分離純GE 8 1 1 1 2因子A、B !及B之製備性 HPLC技術係於半製備性HPLC儀器(島津-LC8A)進行,該 儀器配備有西伯理可索(Hibar Lichrosorb)(莫克(Merck)公 司)25 X 2 5 0毫米管柱RP 8 (7微米粒徑),使用40 mM甲酸銨 且以甲酸調整至pH 4.5,以35毫升/分鐘之流速洗提。含 有經分離之GE 81112因子之重覆層析洗提產物根據其內 容匯集,於減壓下濃縮成水溶液,水溶液經凍乾獲得經純 化之GE 81112因子A、:^及B。 如業界常見,製造、回收及純化步驟可藉多種分析程序 監視,該等分析程序包括使用敏感微生物進行生物檢定分 析及/或HPLC程序。較佳分析HPLC之技術係於島津LC10 儀器進行,儀器配備有2 5 0 X 4 . 6毫米管柱塡裝對稱 17 312/發明說明書(補件)/92-02/91135061 200409816 (Symmetry)(瓦特氏(Waters)公司)或阿帝瑪(Altima)(全科技 (Alltech)公司)5微米粒徑C18靜相,以40mM甲酸銨以甲 酸調整至p Η 4 · 5,以1毫升/分鐘流速洗提。於2 3 0奈米檢 測。此種情況下,因子A、Β!及Β之滯留時間典型分別爲 13、 18、 21 分鐘。 因本發明之抗生素物質具有酸及鹼官能基,故於適當pH 値也可呈內鹽或兩性離子形式存在。此外可根據習知程序 形成鹽。本發明化合物之代表性酸加成鹽包括經由與有機 及無機酸進行標準反應生成之鹽,該等酸例如爲氫氯酸、 氫溴酸、硫酸、磷酸、乙酸、三氟乙酸、三氯乙酸、丁二 酸、檸檬酸、抗壞血酸、乳酸、順丁烯二酸、反丁烯二酸、 棕櫚酸、膽酸、巴母酸(p a m 〇 i c a c i d)、黏酸、麩胺酸、樟 腦酸、戊二酸、乙醇酸、苯二甲酸、酒石酸、月桂酸、硬 脂酸、水楊酸、甲烷磺酸、苯磺酸、山梨酸、苦味酸、苯 甲酸、桂皮酸等。 可用於與GE 81 1 12化合物形成加成鹽之鹼之代表例有: 鹼金屬或鹼土金屬氫氧化物例如氫氧化鈉、氫氧化鉀及氫 氧化鈣;氨及有機脂肪族胺、環脂族胺或芳香族胺例如甲 胺、二甲胺、三甲胺及甲基吡啶。 本發明之自由態化合物或兩性離子化合物轉成對應 鹽,以及相反地,本發明化合物之鹽轉成兩性離子或自由 態化合物形式係屬於熟諳技藝人士之技巧範圍且涵蓋於本 發明之範圍。 例如本發明化合物可經由將非加成鹽形式溶解於水性 溶劑及加入略爲過量之選用酸或鹼而被轉成對應酸或鹼加 18 312/發明說明書(補件)/92-02/91135061 200409816 成鹽。然後結果所得之溶液或懸浮液經凍乾而回收所需鹽。 若終產物鹽形式不可溶於溶劑,而非鹽形式可溶於溶劑 時,可由溶液藉過濾回收。 非鹽形式可由對應酸或鹼鹽溶解於水溶劑,然後中和而 釋放出非鹽形式製備。 當於中和之後需要脫鹽之時,可採用常見脫鹽程序。例 如可方便地使用於矽烷化矽膠、非官能化聚苯乙烯、丙烯 酸系以及孔徑經控制的聚葡萄糖樹脂(例如西法戴思LH 20) 或活性碳進行管柱層析術。使用水溶液洗提非期望之鹽之 後,所需產物利用水與極性溶劑或非極性有機溶劑混合物 之線性梯度或階級梯度洗提,例如使用乙腈/水5 0 : 5 0至約 1 0 0 %乙腈洗提。 如業界已知,與藥物可容許性酸(或鹼)或非藥物可容許 性酸(或鹼)生成之加成鹽可用作爲方便純化技術。於形成 及分離後,GE 8 1 1 1 2化合物之酸加成鹽形式可轉成對應自 由態·兩性離子或轉成不同的藥物可容許加成鹽。 GE 8 111 2因子A之物理化學性質 A)質譜術 GE 81112因子 A於配備有電噴霧來源之熱費尼根 (Thermofinnigan)LCQ戴卡(deca)儀器之MS實驗,使用熱費 尼根校準混合物於m/z = 644進行一質子化。電噴霧條件爲 噴霧電壓:4.7千伏特;毛細溫度:25 0 °C ;毛細電壓:9伏特; 輸注模式5微升/分鐘。光譜係由〇.〇1毫克/毫升於乙腈: 水50:50(v/v)之溶液記錄。 圖1顯示GE 81 1 12因子A於使用規度化之碰撞能25% 19 312/發明說明書(補件)/92-02/91135061 200409816 於m/z = 644之一質子化離子分選後之典型MS-MS光譜。GE 81112 因子 A 於布克(Bruker)達通尼克(Daltonics)APEXII, 4 · 7泰思拉(T e s 1 a)光譜儀配備有電噴霧來源之實驗中,獲得 於m/z = 644.2 1 8 6之一質子化離子之確切質量。FTMS條件 爲:電噴霧:分析來源,偏軸噴霧,60微升/小時;乾燥氣體 2 00 °C ;毛細電壓:70伏特;脫脂器電壓:1〇伏特;累進:40 掃描;寬帶模式:解析度20’000。 B)紅外線光譜術 GE 8 1 1 1 2因子A之紅外線光譜顯示於圖2。光譜係以潤 滑油糊(nujol mull)使用IFS-48富立葉轉換分光光度計測 定。觀察得下列主吸收帶(厘米^):3356: 2956; 2855; 2256; 2128; 1663; 1596; 1455; 1378; 1345; 1123; 1050; 1026; L002; 825; 764° .Performed as described by Kroppenstedt (RM Kroppenstedt, E. Stackebrandt and M. Goodfellow, Taxonomic revision of the actinomycete genera Actinomadura and Microtetraspora, System. Appl. Microbiol. J_i, 1 48- 1 60, 1 990), using a microbiological identification system Inspection (LT. Miller, same text). The Streptomyces DSMZ 1 43 8 6 strain contains LL-diaminopimelate and peptidoglycan, and does not contain mycolic acid. Iso- and anti-iso-branched fatty acids were present, and no hydroxy fatty acid or 10-methyl-branched fatty acid was detected, that is, fatty acid type 2c streptomyces. 12 312 / Instruction of the Invention (Supplement) / 92-02 / 91135061 200409816 Identification of the Streptomyces DS M Z 1 4 3 8 6 Strain that can produce the compound GE 8 1 1 1 2 is named on the chain because it has the following chemical characteristics Mycelia:-Vegetative mycelia that form branches but are not segmented. 10 aerobic hyphae (mostly > 20) arthrospore chains;-According to Kroppenstedt, there are LL · diamine and 2c fatty acid side pictures on the cell wall (RM Kroppenstedt, Fatty menaquinone analysis of actinomy cetes and organisms, pp .1 7 3-199, in: Chemical Methods in Systematics, M. Goodfellow and DE Minnikin eds Accademic Press, 1985). Like other microorganisms, the bacteria that make GE81112 compounds have changed. For example, artificial mutants and mutants of this strain can be obtained by treating various mutants such as ultraviolet light and treatments such as nitrous acid, N-methyl-N-nitrosoguanidine, and various other chemicals. All natural and artificial variants and mutants of the strand 1 4 3 8 6 which contain the genetic ability of the ΐ 8 111 2 compound are considered to be equivalent to the present invention and thus fall within the scope of the present invention. Antibiotics can be recovered from the surface portion of the fermentation broth. Extraction of GE 8 1 1 1 2 compounds and pure GE 8 1 1 1 2 compounds are performed by known techniques for the recovery of fermentation broths that can produce microorganisms. Known recovery techniques such as extraction in the presence of adjuvants, by adding non-solvents, PH precipitation of salt or changing solution, operation, reversed-phase separation chromatography, ion exchange chromatography, molecular row, etc. 312 / Description of the Invention (Supplement) / 92-02 / 91135061 Morphology and production of acid and related bacterial greater than pimelic acid; London, Strain characteristics are also made by the use of -N'nitro bacteria DSMZ Ding for the purpose of making GE The procedure for removing chromatography according to the used solvent extraction sorting chromatography 13 200409816 to recover the antibiotic substance of the present invention from the fermentation broth includes the extraction of GE 8 1 11 2 by ion exchange chromatography. According to this procedure, the fermentation broth after the furnace can be contacted with the ion exchange resin. Elution can be performed by changing the pH or ion intensity. Ion exchange resins that can be conveniently used to recover the compounds of the present invention are, for example, anionic and cationic ion exchange resins, that is, synthetic polymers (such as polystyrene, acrylic polymers) or natural polymers (such as cellulose , Sephar ose polymer, dioxide, etc. The matrix is introduced by acid (such as COOH, -SChH) or test (such as _n (CH3) 2, -n + (ch3) 3) Functional group derived resin. The aforementioned resins are, for example, Dowex 50W resin (Dow Chemical Co.), Amberlite IR-200 and IR-120 (Rohm & Haas), PL-SCX 1000 and APL-SCX 4000 A (Polymer Laboratories), Isolute SCX IST (International Sorbent Technology), SP Westfaros Fast Flow and SP Sephadex G25 (Pharmacia Biotech). Another procedure for the recovery of antibiotic substances involves adsorption onto a suitable substrate, followed by elution with a polar water-miscible solvent or a mixture thereof, concentration under reduced pressure to form a water residue, and precipitation using the aforementioned type of precipitant. The pH can be adjusted as appropriate. Adsorption matrices that can be conveniently used to recover the compounds of the present invention are, for example, activated carbon (such as Darco G60, Norit CG1), polystyrene, or mixed polystyrene-divinylbenzene resins (such as Dyne ( Diaion) HP20, Mitsui Chemicals Corporation; M112 or S112 The Dow Chemical Company; Amberlite XAD2 or XAD4, Rohm and Haas Corporation), acrylic resins (such as XAD7 or XAD8, Rohm and Haas Corporation), phenolic adsorbents ( Example 14 312 / Explanation of the Invention (Supplement) / 92-02 / 91135061 200409816 Such as DuolUe X AD 761 (Rohm and Haas Company), polyamide resins such as polycaprolactam, nylon and cross-linked polyethylene Pyridoxone (eg Polyamide-CC 6, Polyamide-SC 6'Polyamine-CC 6.6, Polyamide-CC 6AC and Polyamide-SC 6AC, Macherey-Nagel ) Company, West Germany; PA400, M. Woelm AG AG, West Germany; PVP-CL, Aldrich Chemical Company, West Germany, cross-linked glucosan (such as West France Days LH-20, Famacia Fine Chemicals). Activated carbon and / or polystyrene resins are commonly used, particularly as Dane HP 20 resin (Mitsui Chemical Co., Ltd.). Adsorption on the aforementioned types of adsorption matrices can also use ion (e.g. cation) exchange chromatography as a procedure to purify the crude product recovered from the fermentation broth. It is preferred that the solvent for the elution of the GE 81 1 12 compound by the adsorption matrix is determined based on the specific stationary phase. When activated carbon is used, the elution is achieved by changing to an acidic pH elution buffer, which typically contains a water-miscible solvent such as a lower ketone such as acetone or a lower alcohol such as methanol. In this way, the aqueous mixture is adjusted to an appropriate pH. When polystyrene resin, polystyrene-divinylbenzene resin, acrylic resin or polyamide resin is used, the eluent is preferably a water-miscible solvent or an aqueous mixture thereof such as water and (Cl-C3) alkanol. Of a mixture. The term "water-miscible solvent" used in this case is intended to indicate the current definition of the word in the industry when not specifically stated, meaning that a solvent can be miscible with water in a reasonably wide concentration range under the conditions of use and is suitable for anticipation use. Water-miscible effective solvents that can be used to elute the compounds of the present invention are, for example, lower alkanols such as (ChCd alcohols such as methanol, ethanol, and propanol; phenyl (Ci-Cd alkanols such as benzyl alcohol; lower ketones such as ( C3-C4) ketones such as acetone and ethyl methyl ketone; cyclic ethers such as di # alkane and tetrahydrofuran; glycols and partial etherification products thereof such as 15 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816 Ethylene glycol, propylene glycol, and ethylene glycol monomethyl ether; low-carbon ammonium amines such as dimethylformamide and diethylformamide; acetic acid, dimethylarsox, and acetonitrile. The method for recovering the GE 81 1 12 compound is to extract the GE 8 1 1 1 2 compound or a salt thereof using a water-miscible organic solvent, and adjust the pH to an appropriate pH value during the extraction, and / or via salting, and then add the The antibiotic dissolved in the extraction solvent forms an appropriate organic salt of the ion pair. The antibiotic is then precipitated from the concentrated extract by, for example, adding a precipitant. The term "water-immiscible solvent" used in this case is intended to have the definition currently used in the industry, indicating ~ Solvents are slightly miscible or practical under the conditions of use Miscible in water. Water-immiscible organic solvents that can be used to extract the compounds of the present invention from fermentation broth. For example, alkanols containing at least 4 carbon atoms can be linear, branched or cyclic such as n-butanol, 1-pentanol, 2- Amyl alcohol, 3-pentanol, 1-hexanol, 2-hexanol, 3-hexanol, 3,3-dimethyl-1-butanol, 4-methyl-1 · pentanol, 3 · methyl 1-pentyl alcohol, 2,2-dimethyl-3-pentanol, 2, cardiac dimethyl-3-pentanol, 4,4-dimethyl-2-pentanol, 5.methyl-2 -Hexanol, 1-heptanol, 2.heptanol, 5-methyl • 1 · hexanol, 2-ethyl-1-hexanol, 2-methyl-3-hexanol, 1-octanol, 2 · Octanol, cyclopentanol, 2-cyclopentylethanol, 3-cyclopentyl-1-propanol, cyclohexanol, cycloheptanol, cyclooctanol, 2,3-dimethylcyclohexanol, 4 -Ethylcyclohexanol, cyclooctylmethanol, 6-methyl-5-hepten-2-ol, 1-nonanol, 2-nonanol, 1-decanol, 2-decanol, and 3-decanol ; Ketones containing at least 5 carbon atoms, such as methyl isopropyl ketone, methyl isobutyl ketone, methyl n-pentyl ketone, methyl isoamyl ketone and mixtures thereof. With GE 8 1 1 1 2 Convenient ion pairs formed by compounds are obtained, for example, by the addition of an acid at the appropriate pH. Thus, for example, sulfonic acid is represented by p-toluenesulfonic acid, pentanesulfonic acid, hexanesulfonic acid, heptanesulfonic acid, or the like; or carboxylic acid is represented by hexanoic acid, heptanoic acid, benzoic acid, etc. In addition, the ion pair may be passed Example 3 of adding cations / Instruction of the invention (Supplement) / 92-〇2 / 91135061 200409816 It is produced at the appropriate pH such as triethylcopper, tetrabutylcopper, etc. The purification of crude GE 8 1 1 1 2 compound can be borrowed. Known technology is achieved, but it is preferably performed using chromatography. Conveniently, so-called stereo exclusion chromatography can also be used to obtain good results. In particular, this technique usually uses cross-linked glucosan with controlled porosity, most of which have been alkylated, such as Sifa Days LH-2C (Famacia Fine Chemicals). For example, a medium pressure liquid chromatography separation system can be used to perform reverse-phase chromatography on R P · 8 or R P -1 8 functionalized silica gel and elute with ammonium formate solution. The crude product and purified product separated from the fermentation broth depends on the fermentation and purification conditions, and usually contains unequal proportions of a single GE 81112 factor human, 31 and B mixture. The separation and purification of the individual factors A, B, and B! Can be conveniently performed by semi-preparative HPLC using a formulation containing the GE 8 1 1 12 compound mixture. The preparative HPLC technique, which is preferably used for the separation of pure GE 8 1 1 1 2 factors A, B! And B, is performed on a semi-preparative HPLC instrument (Shimadzu-LC8A) equipped with Hibar Lichrosorb (Merck) 25 x 250 mm column RP 8 (7 micron particle size), using 40 mM ammonium formate and adjusting to pH 4.5 with formic acid, eluting at a flow rate of 35 ml / min. The repeated chromatography elution products containing the isolated GE 81112 factor were pooled according to their contents, and concentrated under reduced pressure to form an aqueous solution. The aqueous solution was lyophilized to obtain purified GE 81112 factors A,: ^, and B. As is common in the industry, manufacturing, recovery, and purification steps can be monitored by a variety of analytical procedures, including bioassay analysis and / or HPLC procedures using sensitive microorganisms. A better analytical HPLC technique was performed on a Shimadzu LC10 instrument equipped with a 250 x 4.6 mm column mounted symmetrical 17 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816 (Symmetry) (Watt Waters) or Altima (Alltech) 5 micron particle size C18 stationary phase, adjusted to p Η 4 · 5 with 40 mM ammonium formate and formic acid, and washed at a flow rate of 1 ml / min mention. Detected at 230 nm. In this case, the retention times of factors A, B !, and B are typically 13, 18, and 21 minutes, respectively. Because the antibiotic substance of the present invention has acid and base functional groups, it can also exist in the form of internal salts or zwitterions at appropriate pH. In addition, salts can be formed according to conventional procedures. Representative acid addition salts of the compounds of the present invention include salts formed by standard reactions with organic and inorganic acids such as hydrochloric acid, hydrobromic acid, sulfuric acid, phosphoric acid, acetic acid, trifluoroacetic acid, and trichloroacetic acid. , Succinic acid, citric acid, ascorbic acid, lactic acid, maleic acid, fumaric acid, palmitic acid, cholic acid, pamolic acid, mucoic acid, glutamic acid, camphoric acid, pentyl acid Diacid, glycolic acid, phthalic acid, tartaric acid, lauric acid, stearic acid, salicylic acid, methanesulfonic acid, benzenesulfonic acid, sorbic acid, picric acid, benzoic acid, cinnamic acid, etc. Representative examples of bases that can be used to form addition salts with GE 81 1 12 compounds are: alkali metal or alkaline earth metal hydroxides such as sodium hydroxide, potassium hydroxide, and calcium hydroxide; ammonia and organic aliphatic amines, cycloaliphatic Amines or aromatic amines such as methylamine, dimethylamine, trimethylamine and methylpyridine. The conversion of the free-state compound or zwitterionic compound of the present invention into the corresponding salt, and conversely, the conversion of the salt of the compound of the present invention to the zwitterionic or free-state compound form is within the skill of those skilled in the art and is within the scope of the present invention. For example, the compound of the present invention can be converted to the corresponding acid or base by dissolving the non-addition salt form in an aqueous solvent and adding a slight excess of the selected acid or base. 200409816 into salt. The resulting solution or suspension is then lyophilized to recover the desired salt. If the salt form of the final product is insoluble in the solvent and the non-salt form is soluble in the solvent, it can be recovered from the solution by filtration. Non-salt forms can be prepared by dissolving the corresponding acid or base salt in an aqueous solvent and then neutralizing to release the non-salt form. When desalination is required after neutralization, common desalination procedures can be used. For example, it can be conveniently used for column chromatography on silylated silicone, non-functional polystyrene, acrylic and polydextrose resins with controlled pore size (such as Sifa Days LH 20) or activated carbon. After the undesired salt is eluted with an aqueous solution, the desired product is eluted with a linear gradient or a step gradient of a mixture of water and a polar or non-polar organic solvent, such as acetonitrile / water 50:50 to about 100% acetonitrile Elution. As known in the industry, addition salts with pharmaceutically acceptable acids (or bases) or non-pharmacologically acceptable acids (or bases) can be used as convenient purification techniques. After formation and separation, the acid addition salt form of the GE 8 1 1 12 compound can be converted to the corresponding free state, zwitterion, or into a different drug tolerable addition salt. Physicochemical properties of GE 8 111 2 factor A A) Mass spectrometry MS experiment of factor 81 GE 81112 on a Thermofinnigan LCQ deca instrument equipped with an electrospray source, using a thermofenigan calibration mixture One protonation was performed at m / z = 644. Electrospray conditions were: spray voltage: 4.7 kV; capillary temperature: 250 ° C; capillary voltage: 9 volts; infusion mode 5 μl / min. The spectra were recorded from a solution of 0.01 mg / ml in acetonitrile: water 50:50 (v / v). Figure 1 shows that the collision energy of GE 81 1 12 factor A after using regularization is 25%. 19 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816 After sorting with one of the protonated ions at m / z = 644 Typical MS-MS spectrum. GE 81112 Factor A was obtained in an experiment with Bruker's Daltonics APEXII, 4 · 7 Tesla spectrometer equipped with an electrospray source at m / z = 644.2 1 8 6 The exact mass of one of the protonated ions. FTMS conditions are: electrospray: analysis source, off-axis spray, 60 μl / h; dry gas at 200 ° C; capillary voltage: 70 volts; degreaser voltage: 10 volts; progressive: 40 scans; broadband mode: analysis Degree 20'000. B) Infrared spectroscopy The infrared spectrum of GE 8 1 1 1 2 factor A is shown in Figure 2. The spectrum was measured with a lujol mull using an IFS-48 Fourier transform spectrophotometer. The following main absorption bands (cm ^) were observed: 3356: 2956; 2855; 2256; 2128; 1663; 1596; 1455; 1378; 1345; 1123; 1050; 1026; L002; 825; 764 °.

C^H-NMR 及 13C-NMR 添加三氟乙酸(TFA)後於25°C於DMS〇-d6記錄GE 81112 因子 A 之 όΟΟΜΗζΑ-ΝΜΙΙ 光譜(圖 3)以及 150MHz13C-NMR 光譜(圖4)。二光譜檢測來自於純化過程之甲酸鹽信號(1}] 化學位移 8.13 及 7.07-7.25ppm;13C 化學位移 163.0ppm)。 表IV及表V報告對因子A觀察得之1Η及13C NMR光譜。 20 312/發明說明書(補件)/92-02/91135061 200409816 表 IV:GE81112(因子 A)於 DMSO-ch + TFA 之1H-NMR 共 振 化學位移 多樣性 屮化學位 多樣性 (ppm) 移(ppm) 1.52 br d 4.70 m 1.57-1.67 m 5.06 d 1.8 1 br d 6.46 b r 1.88 m 6.94 s 2.87 dd 7.29 s 2.90 m 7.99 d 3.12 dd 8.17 d 3.15 m 8,.3 0 m 3.65 m 8.57 br d 3.83 m 8.95 d 3.94 br d 9.06 br d 4.40 b r s 14.09 br 4.46 m 14.27 b r 4.50 dd -- — 21 312/發明說明書(補件)/92-02/91135061 200409816 表 V: GE 81112 因子 A 於 DMSO-ch + TFA 之 13C-NMR 共 振 13c化學位移 多樣性 13c化學位移 多樣性 (ppm) (ppm) 15.9 t 67.76 t 27.19 t 116.83 d 28.41 t 118.49 d 35.3 1 t 128.4 1 s 42.86 t 129.03 s 50.13 d 133.65 d 51.30 d 139.66 s 56.86 d 156.73 s * 59.7 1 d 167.39 s 64.07 d 170.16 s 65.11 d 17 1.29 s 66.88 d 171.65 s GE 8 1 1 1 2因子B之物理化學性質 A)質譜術 GE 81112因子B於配備有電噴霧來源之熱費尼根LCQ 戴卡儀器之MS實驗,使用熱費尼根校準混合物於m/z = 65 9 進行一質子化。電噴霧條件爲噴霧電壓:4.7千伏特;毛細 溫度:25 0 °C ;毛細電壓:9伏特;輸注模式5微升/分鐘。光 譜係由0.01毫克/毫升於乙腈:水5 0 :5 0(Wv)之溶液記錄。C ^ H-NMR and 13C-NMR with trifluoroacetic acid (TFA) were recorded at 25 ° C at DMS 0-d6. The spectrum of GE 81112 factor A was recorded at 100 ΜΗζΑ-ΝΜΙΙ (Figure 3) and 150 MHz 13C-NMR spectrum (Figure 4). The two-spectrum detection comes from the formate signal (1)] of the purification process (chemical shifts 8.13 and 7.07-7.25ppm; 13C chemical shift 163.0ppm). Tables IV and V report the 1Η and 13C NMR spectra observed for factor A. 20 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816 Table IV: 1H-NMR resonance chemical shift diversity 屮 chemical position diversity (ppm) shift (ppm) of GE81112 (factor A) in DMSO-ch + TFA ) 1.52 br d 4.70 m 1.57-1.67 m 5.06 d 1.8 1 br d 6.46 br 1.88 m 6.94 s 2.87 dd 7.29 s 2.90 m 7.99 d 3.12 dd 8.17 d 3.15 m 8, .3 0 m 3.65 m 8.57 br d 3.83 m 8.95 d 3.94 br d 9.06 br d 4.40 brs 14.09 br 4.46 m 14.27 br 4.50 dd--21 312 / Description of the Invention (Supplement) / 92-02 / 91135061 200409816 Table V: GE 81112 Factor A in DMSO-ch + TFA 13C-NMR resonance 13c Chemical shift diversity 13c Chemical shift diversity (ppm) (ppm) 15.9 t 67.76 t 27.19 t 116.83 d 28.41 t 118.49 d 35.3 1 t 128.4 1 s 42.86 t 129.03 s 50.13 d 133.65 d 51.30 d 139.66 s 56.86 d 156.73 s * 59.7 1 d 167.39 s 64.07 d 170.16 s 65.11 d 17 1.29 s 66.88 d 171.65 s GE 8 1 1 1 2 Physical and chemical properties of factor B A) Mass spectrometry GE 81112 factor B is equipped with an electrospray source MS experiment with Thermal Fernigan LCQ Dicastal instrument, calibrated with Thermal Fernigan A composition for protonated at m / z = 65 9. Electrospray conditions were spray voltage: 4.7 kV; capillary temperature: 25 0 ° C; capillary voltage: 9 volts; infusion mode 5 μl / min. The optical spectrum was recorded from a solution of 0.01 mg / ml in acetonitrile: water 50:50 (Wv).

圖5顯示GE 8 1 1 1 2因子B於使用規度化之碰撞能2 8 % 於m/z = 65 9之一質子化離子分選後之典型MS-MS光譜。GE 22 312/發明說明書(補件)/92-02/91135061 200409816 8Π12因子B於布克達通尼克APEX II,4.7泰思拉光譜儀 配備有電噴霧來源之實驗中,獲得於m/z = 6 5 9.22 95之一質 子化離子之確切質量。FTMS條件爲:電噴霧:分析來源,偏 軸噴霧,6 0微升/小時;乾燥氣體2 0 0 °C ;毛細電壓:7 0伏 ^ ’脫目曰益電壓:1 0伏特;累進:4 0掃描;寬帶模式:解析度 20,000 。 B)紅外線光譜術Figure 5 shows a typical MS-MS spectrum of GE 8 1 1 1 2 factor B after using a regularized collision energy of 28% at m / z = 65 9 to sort protonated ions. GE 22 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816 8Π12 Factor B was obtained in an experiment with a Baker Datonic APEX II, 4.7 Tesla spectrometer equipped with an electrospray source, obtained at m / z = 6 5 9.22 The exact mass of one of the protonated ions. FTMS conditions are: electrospray: analysis source, off-axis spray, 60 μl / h; dry gas at 200 ° C; capillary voltage: 70 volts ^ 'eye loss voltage: 10 volts; progressive: 4 0 scan; Broadband mode: Resolution 20,000. B) Infrared spectroscopy

GE 8 1 1 1 2因子B之紅外線光譜顯示於圖6。光譜係以溴 化鉀使用IFS-48富立葉轉換分光光度計測定。觀察得下列 主吸收帶(厘米 1:3359: 2958; 2852; 2258; 2129; 1681; 1591; 1450; 1385; 1347; 1122; 1072; 1025; 998; 765。 C^H-NMR 及 13C-NMR 添加三氟乙酸(TFA)後於25°C於DMS〇-d6記錄GE 81112 因子 B 之 SOOMHzj-NMR 光譜(圖 7)以及 150MHz13C-NMR 光譜(圖8)。二光譜檢測來自於純化過程之甲酸鹽信號(1 η 化學位移 8.13 及 7.07-7.25 ppm; 13C 化學位移 163.0 ppm)。 表VI及表VII報告對因子B觀察得之1Η及13C NMR光 譜。 23 312/發明說明書(補件)/92-〇2/91135061 200409816 表 VI: GE 81112 因子 B 於 DMS〇-cU + TFA 之1H-NMR 共 振 1 Η化學位移 多樣性 屮化學位移 多樣性 (ppm) (ppm) 1.52 br d 4.60 m 1.57-1.72 m 5.05 d 1.83 br d 6.46 br 1.90 m 6.48 s 2.63 dd 6.93 s 2.88 dd 7.40 b r s 2.92 m 7.84 d 3.13 br d 8.05 d 3.64 m 8.33 m 3.83 m 8.54 d 3.95 br d 9.00 br d 4.35 br s 11.72 b r s 4.46 m 11.75 b r s 4.50 dd -- -- 24 312/發明說明書(補件)/92-02/91135061 200409816 表 VII: GE 81112 因子 B 於 DMS〇-d6 + TFA 之 13C-NMR 共振 13c化學位移 多樣性 13C化學位移 多樣性 (ppm) (ppm) 15.9 t 67.77 t 27.36 t 110.3 d 28.40 t 117.85 d 35.47 t 122.5 s 42.87 t 128.4 s 50.1 d 139.66 s 5 1.20 d 146.7 s 56.78 d 156.7 s 59.73 d 167.4 s 64.09 d 17 0.5 s 65.14 d 17 1.3 s 66.90 d 17 1.38 s GE 8 1 1 1 2因子B!之物理化學性質 A)質譜術 GE 81112因子Β!於配備有電噴霧來源之熱費尼根LCQ 戴卡儀器之MS實驗,使用熱費尼根校準混合物於m/z = 65 8 進行一質子化。電噴霧條件爲噴霧電壓:4.7千伏特;毛細 溫度:250°C ;毛細電壓:9伏特;輸注模式5微升/分鐘。光 譜係由0.01毫克/毫升於乙腈:水5 0:5 0(v/v)之溶液記錄。 圖9顯示GE 81 1 12因子於使用規度化之碰撞能25% 於m/z = 658之一質子化離子分選後之典型MS-MS光譜。 25 312/發明說明書(補件)/92-02/91135061 200409816 GE 81112因子匕於布克達通尼克APEX II,4.7泰思拉 光譜儀配備有電噴霧來源之實驗中,獲得於m / z = 6 5 8.2 4 5 9 之一質子化離子之確切質量。FTMS條件爲:電噴霧:分析來 源,偏軸噴霧,60微升/小時;乾燥氣體200 °C ;毛細電壓:7〇 伏特;脫脂器電壓:10伏特;累進:40掃描;寬帶模式:解析 度 20,000 。The infrared spectrum of GE 8 1 1 1 2 factor B is shown in Figure 6. The spectrum was measured with potassium bromide using an IFS-48 Fourier transform spectrophotometer. The following main absorption bands were observed (cm 1: 3359: 2958; 2852; 2258; 2129; 1681; 1591; 1450; 1385; 1347; 1122; 1072; 1025; 998; 765. C ^ H-NMR and 13C-NMR addition Trifluoroacetic acid (TFA) was recorded at 25 ° C in DMS 0-d6. SoOMHzj-NMR spectrum of GE 81112 factor B (Figure 7) and 150MHz13C-NMR spectrum (Figure 8). Two-spectrum detection of formic acid from the purification process Salt signal (1 η chemical shift 8.13 and 7.07-7.25 ppm; 13C chemical shift 163.0 ppm). Table VI and Table VII report the 1Η and 13C NMR spectra observed for factor B. 23 312 / Description of the Invention (Supplement) / 92 -〇2 / 91135061 200409816 Table VI: 1H-NMR resonance of GE 81112 factor B at DMS〇-cU + TFA 1 Η Chemical shift diversity 屮 Chemical shift diversity (ppm) (ppm) 1.52 br d 4.60 m 1.57-1.72 m 5.05 d 1.83 br d 6.46 br 1.90 m 6.48 s 2.63 dd 6.93 s 2.88 dd 7.40 brs 2.92 m 7.84 d 3.13 br d 8.05 d 3.64 m 8.33 m 3.83 m 8.54 d 3.95 br d 9.00 br d 4.35 br s 11.72 brs 4.46 m 11.75 brs 4.50 dd--24 312 / Description of the Invention (Supplement) / 92-02 / 91135061 200409816 Table VII: GE 81112 13C-NMR resonance of DMS 0-d6 + TFA 13c Chemical shift diversity 13C Chemical shift diversity (ppm) (ppm) 15.9 t 67.77 t 27.36 t 110.3 d 28.40 t 117.85 d 35.47 t 122.5 s 42.87 t 128.4 s 50.1 d 139.66 s 5 1.20 d 146.7 s 56.78 d 156.7 s 59.73 d 167.4 s 64.09 d 17 0.5 s 65.14 d 17 1.3 s 66.90 d 17 1.38 s GE 8 1 1 1 2 Physical and chemical properties of factor B! A) Mass spectrometry GE Factor 81112! In a MS experiment with a thermal Fernigan LCQ Dicastal instrument equipped with an electrospray source, a thermal Fernigan calibration mixture was used to perform a protonation at m / z = 65 8. Electrospray conditions were spray voltage: 4.7 kV; capillary temperature: 250 ° C; capillary voltage: 9 volts; 5 microliters / minute in infusion mode. The optical spectrum was recorded from a solution of 0.01 mg / ml in acetonitrile: water 50:50 (v / v). Figure 9 shows a typical MS-MS spectrum of a GE 81 1 12 factor using a regularized collision energy of 25% at m / z = 658 after protonated ion sorting. 25 312 / Explanation of the invention (Supplement) / 92-02 / 91135061 200409816 GE 81112 factor dagger was used in the experiment of APEX II, 4.7 Tesla spectrometer equipped with electrospray source, obtained at m / z = 6 5 8.2 4 5 9 The exact mass of one of the protonated ions. FTMS conditions are: electrospray: analysis source, off-axis spray, 60 μl / h; dry gas 200 ° C; capillary voltage: 70 volts; degreaser voltage: 10 volts; progressive: 40 scans; broadband mode: resolution 20,000.

B) W-NMR 及 13C-NMR 於25°C於DMS〇-d6記錄GE 81 1 12因子B】之600 MHz j-NMR 光譜(圖 10)以及 150MHz13C-NMR 光譜(圖 11)。二 光譜檢測來自於純化過程之甲酸鹽信號ΓΗ化學位移 8.32 ; 13C 化學位移 1 65.2 8ppm)。 表VIII及表IX報告對因子B!觀察得之4及13C NMR 光譜。 26 312/發明說明書(補件)/92-02/91135061 200409816 表 VIII: GE 81112 因子匕於 DMS〇-d6 + TFA 之1H-NMR 共振 化學位移 多樣性 4化學位移 多樣性 (ppm) (ppm) 1.38 b r d 4.40 b r m 1.56-1.64 m 4.46 m 1.76 m 5.05 d 2.70 m 5.60 br s 2.82 b r s 6.21 br 2.92 m 6.52 br 3.01-3.06 m 6.78 b r s 3.49 b r m 7.13 br 3.57 b r s 7.80 br d 4.20 b r d d 7.90 br d 4.26 br 8.44 br 27 312/發明說明書(補件)/92-02/91135061 200409816 表ΙΧ:σβ81112因子心於DMS〇-d6 + TFA之13C-NMR老」辰 13c化學位移 多樣性 13C化學位移 多樣性 (ppm) (ppm) 17.95 t 66.88 d 27.97 t 111.07 d 29.8 t 118.97 d 一 36.54 t 122.47 s 43.75 t 127.88 s 45.65 d 148.08 s 50.52 d 159.18 s 51.9 d 169.44 s 57.75 d 171.53 s 61.0 d 171.81 s 64.03 d 173.08 s 66.7 d -- — 牛物活件 GE 8 1 1 1 2因子A、B及B i之抗微生物活性係使用微稀釋 法使用標準U字形底96孔孔板根據國家臨床實驗室標準 委員會之方法測定(Methods for Dilution Antimicrobial Susceptibility Tests for Bacteria that Grow Aerobically 一 Third edition; Approved Standard. NCCLS document M 7 - A 3 V o 1. 1 3 N o . 2 5 )。結果報告於表1 0。 使用之菌株爲臨床單離株或得自美國種型培養收集會 (ATCC)。GE 81 1 12因子溶解於DMS0 ;此溶液進一步以蒸 餾水稀釋。 28 312/發明說明書(補件)/92-02/91135061 200409816 使用之培養基爲經過陽離子調整之慕勒辛頓(Mueller Hinton)液態培養基(CAMHB)用於大腸桿菌(Escherichia coli)、金黃葡萄球菌(Staphylococcus aureus) '卡它莫氏菌 (Mo r axella catarrhalis)、糞腸球菌(Enterococcus faecalis); 塔得西威(Todd Hewitt)液態培養基(THB)用於產膿鏈球菌 (Streptococcus pyogenes)、肺炎鏈球菌(Streptococcus pneumoniae);抗生素培養基3號(AM3)以及基礎培養基戴 維思明吉利(Davis Mingioli)液態培養基+2%(w/v)葡萄糖 + 100微克/毫升天冬醯胺(MM)用於枯草桿菌(Bacillus sub till s);戴維思明吉利液態培養基+2 % (w/v)葡萄糖(MM) 用於大腸桿菌;RPMI 1 640 (RPMI)及最低必需培養基 40 + 0.1 %維生素(MM)用於白色念珠菌(Candida albicans)。除 非另行指示,否則接種物爲1〇4 CFU/毫升。全部菌株皆於 3 5 °C之空氣中培養。培養時間1 8 - 2 4小時。於培養後進行 目測讀取,MIC定義爲可完全抑制接受試驗之微生物生長 之低限値濃度。 29 312/發明說明書(補件)/92-02/91135061 200409816 表X G E 8 1 1 1 2因子A、B及B !之抗微生物活性 Μ I C (微克/毫升) 菌株(培養基) 81112 A 81112 B 81112 B1 819 金黃葡萄球菌 SMITH ATCC 1 9636(CAMHB) >5 12 >5 12 >5 12 49產膿鏈球菌cl.is.(ΤΗΒ) >5 12 5 12 5 12 44肺炎鏈球菌cl.is.(THB) 64 64 64 560 糞腸球菌 Van A(CAMHB) 32 32 5 12 102 枯草桿菌 ATCC6633(MM) 0.13 0.008 0.06 102 枯草桿菌 ATCC 6 6 3 3 (AM3) >5 12 256 5 12 3 2 9 2 卡它莫氏菌 cl.is.(CAMHB) 2 1 2 47大腸桿菌(MM) 0.06 0.03 0.13 47大腸桿菌(CAMHB) >5 12 5 12 5 12 145白色念珠菌(MM) >5 12 >5 12 >5 12 145白色念珠菌(RPMI) >5 12 >5 12 >5 12 GE81112因子六^及Bi可抑制卡它莫氏菌的生長,MIC 係於1-2微克/毫升之範圍。使用之菌株爲臨床單離株。 GE81112因子A、B及B!對肺炎鏈球菌臨床單離株顯示 邊際活性(MIC 64微克/毫升)。此外因子a及B對萬古黴 素(Vancomycin)(VanA)有抗藥性之糞腸球菌具有MI032微 克/毫升,因子至濃度512微克/毫升爲止不具有活性。 已知卡它莫氏菌及肺炎鏈球菌爲人類主要病原菌。其爲 呼吸道感染特別兒童中耳炎以及老人下呼吸道感染的常見 起因。卡它莫氏菌及肺炎鏈球菌晚近已知爲呼吸道的最常 見病原囷(M.C· Enright and H. McKenzy, Moraxella 30 312/發明說明書(補件)/92-02/91135061 200409816 (Branhamella) c a t a r r h a 1 i s - Clinical and molecular aspect of a rediscovered pathogen, J. Med. Microbiol. 16., 3 6 0-7 1, 1997)。 萬古黴素抗藥性腸球菌(VRE)變成造成嚴重人類感染(例 如心內膜炎、腦膜炎及敗血症)的主要醫院感染病原菌,逐 漸構成臨床挑戰(Y. Cetinkaya,P. Falk,C.G. Mayhall, Vancomycin-resistant enterococci, Clin. Microbiol. Rev. 13, 686-707, 2000; L.B. Rice Emergence of vancomycin-resistant enterococci, Emerg. Infec· Dis.l,183-7,2001) o GE 81 1 12因子A、B及B!於極低濃度(確切定義爲少於1 微克/毫升)可抑制大腸桿菌及枯草桿菌的生長,此處此等 細菌係培養於最低必需培養基(MM)。當該等細菌係生長於 豐富培養基時,因子A、B及^之MIC係於256-512微克/ 毫升或以上之範圍。 GE 81112因子A、B及於最低必需培養基或於豐富培 養基不會抑制白色念珠菌的生長。 GE 8 Π 1 2因子A、B及B !對細菌例如大腸桿菌及枯草桿 菌相對於對真核生物例如白色念珠菌之差異表現,提示GE 8 1 1 1 2化合物對原核生物具有特異性作用機轉。 根據晚近抗微生物治療之趨勢,趨向於使用具有較窄抗 微生物範圍其對單離之病原菌具有選擇性活性之藥劑來替 代具有寬廣活性範圍之藥劑較爲有利,如此可降低出現抗 藥性的選擇性壓力(J.C. Gyssens:”Quality Measures of Antimicrobial Drug Use” in Int. J. Antimicrobial Agents, 17, 2001, 9-19; J. Chopra “Research and Development of 31 312/發明說明書(補件)/92-02/91135061 200409816B) W-NMR and 13C-NMR were recorded at 25 ° C in DMS 0-d6 at 600 MHz j-NMR spectrum (Figure 10) and 150 MHz 13C-NMR spectrum (Figure 11). 2 Spectral detection comes from the formate signal of the purification process (the chemical shift ΓΗ is 8.32; the 13C chemical shift is 165.2 8ppm). Tables VIII and IX report the observed 4 and 13C NMR spectra for Factor B !. 26 312 / Description of the Invention (Supplement) / 92-02 / 91135061 200409816 Table VIII: GE 81112 Factor DMS 1-D6 + TFA 1H-NMR Resonance Chemical Shift Diversity 4 Chemical Shift Diversity (ppm) (ppm) 1.38 brd 4.40 brm 1.56-1.64 m 4.46 m 1.76 m 5.05 d 2.70 m 5.60 br s 2.82 brs 6.21 br 2.92 m 6.52 br 3.01-3.06 m 6.78 brs 3.49 brm 7.13 br 3.57 brs 7.80 br d 4.20 brdd 7.90 br d 4.26 br 8.44 br 27 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816 Table IX: Factor of σβ81112 focusing on DMS 0-d6 + 13C-NMR of TFA + 13C chemical shift diversity 13C chemical shift diversity (ppm) (ppm) 17.95 t 66.88 d 27.97 t 111.07 d 29.8 t 118.97 d-36.54 t 122.47 s 43.75 t 127.88 s 45.65 d 148.08 s 50.52 d 159.18 s 51.9 d 169.44 s 57.75 d 171.53 s 61.0 d 171.81 d 031.81 -— Bovine living parts GE 8 1 1 1 2 The antimicrobial activity of factors A, B and B i was determined using the micro-dilution method using a standard U-shaped bottom 96-well plate according to the method of the National Committee for Clinical Laboratory Standards (Methods for Dilutio n Antimicrobial Susceptibility Tests for Bacteria that Grow Aerobically a Third edition; Approved Standard. NCCLS document M 7-A 3 V o 1. 1 3 N o. 2 5). The results are reported in Table 10. The strains used were clinically isolated or obtained from the American Type Culture Collection (ATCC). GE 81 1 factor 12 is dissolved in DMS0; this solution is further diluted with distilled water. 28 312 / Invention (Supplement) / 92-02 / 91135061 200409816 The culture medium used is cation-adjusted Mueller Hinton liquid medium (CAMHB) for Escherichia coli, Staphylococcus aureus ( Staphylococcus aureus) 'Moraxella catarrhalis, Enterococcus faecalis; Todd Hewitt liquid medium (THB) for Streptococcus pyogenes, pneumonia chain Streptococcus pneumoniae; antibiotic medium 3 (AM3) and basal medium Davis Mingioli liquid medium + 2% (w / v) glucose + 100 μg / ml asparagine (MM) for Bacillus subtilis (Bacillus sub till s); Davis Siming Geely liquid medium + 2% (w / v) glucose (MM) for E. coli; RPMI 1 640 (RPMI) and minimum required medium 40 + 0.1% vitamin (MM) for white Candida (Candida albicans). Unless otherwise indicated, the inoculum is 104 CFU / ml. All strains were cultured in air at 35 ° C. Incubation time is 18-24 hours. After visual inspection, the MIC is defined as the lower limit radon concentration that can completely inhibit the growth of the microorganisms under test. 29 312 / Instruction of the invention (Supplement) / 92-02 / 91135061 200409816 Table XGE 8 1 1 1 2 Antimicrobial activity of IC A (micrograms / ml) Strain (medium) 81112 A 81112 B 81112 B1 819 S. aureus SMITH ATCC 1 9636 (CAMHB) > 5 12 > 5 12 > 5 12 49 Streptococcus pyogenes cl.is. (ΤΗΒ) > 5 12 5 12 5 12 44 Streptococcus pneumoniae cl. is. (THB) 64 64 64 560 Enterococcus faecalis Van A (CAMHB) 32 32 5 12 102 Bacillus subtilis ATCC6633 (MM) 0.13 0.008 0.06 102 ATCC 6 6 3 3 (AM3) > 5 12 256 5 12 3 2 9 2 Moraxella catarrhalis cl.is. (CAMHB) 2 1 2 47 E. coli (MM) 0.06 0.03 0.13 47 E. coli (CAMHB) > 5 12 5 12 5 12 145 Candida albicans (MM) > 5 12 > 5 12 > 5 12 145 Candida albicans (RPMI) > 5 12 > 5 12 > 5 12 GE81112 factor VI ^ and Bi can inhibit the growth of Moraxella catarrhalis, MIC is at 1- 2 μg / ml range. The strain used was a clinical single isolate. GE81112 Factors A, B, and B! Showed marginal activity against clinical isolates of Streptococcus pneumoniae (MIC 64 μg / ml). In addition, factors a and B are resistant to Vancomycin (VanA). Enterococcus faecalis has MI032 µg / ml, and the factor is not active until the concentration is 512 µg / ml. Moraxella catarrhalis and Streptococcus pneumoniae are known to be the main human pathogens. It is a common cause of otitis media in children with respiratory infections and lower respiratory tract infections in the elderly. Moraxella catarrhalis and Streptococcus pneumoniae were recently known as the most common pathogens of the respiratory tract (MC · Enright and H. McKenzy, Moraxella 30 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816 (Branhamella) catarrha 1 is-Clinical and molecular aspect of a rediscovered pathogen, J. Med. Microbiol. 16., 3 6 0-7 1, 1997). Vancomycin-resistant enterococci (VRE) become major hospital infections that cause severe human infections (such as endocarditis, meningitis, and sepsis), and gradually pose clinical challenges (Y. Cetinkaya, P. Falk, CG Mayhall, Vancomycin -resistant enterococci, Clin. Microbiol. Rev. 13, 686-707, 2000; LB Rice Emergence of vancomycin-resistant enterococci, Emerg. Infec · Dis.l, 183-7, 2001) o GE 81 1 12 factors A, B And B! Can inhibit the growth of E. coli and Bacillus subtilis at very low concentrations (exactly defined as less than 1 μg / ml), and these bacteria are cultured in the minimum necessary medium (MM). When these bacterial lines are grown in rich media, the MICs of factors A, B, and ^ are in the range of 256-512 μg / ml or more. GE 81112 Factors A and B will not inhibit the growth of Candida albicans in the minimum necessary medium or in rich culture medium. GE 8 Π 1 2 factors A, B, and B! Differential expression of bacteria such as E. coli and B. subtilis compared to eukaryotes such as Candida albicans, suggesting that GE 8 1 1 1 2 compounds have specific effects on prokaryotes turn. According to the recent trend of antimicrobial treatment, it is advantageous to use agents with a narrow antimicrobial range that have selective activity against isolated pathogens instead of agents with a wide range of activity, which can reduce the selectivity of resistance Pressure (JC Gyssens: "Quality Measures of Antimicrobial Drug Use" in Int. J. Antimicrobial Agents, 17, 2001, 9-19; J. Chopra "Research and Development of 31 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816

Antibacteiial Agents” in Current Opinion in Microbiology, 1998,1,49 5 - 5 0 1 )。因此本發明之GE 81112化合物特別適 合用作爲卡它莫氏菌造成呼吸道感染之選擇性治療劑。 本發明化合物可呈藥物可接受性組成物、就此、或與藥 物可容許性載劑混合投予,也可組合其它抗微生物劑例如 青黴素類、頭孢子菌素類、胺基糖苷類以及糖肽類一起投 藥。組合治療也包括循序、同時及分開投予活性化合物, 讓初次投予的藥劑療效未完全消失即做隨後投藥。 本發明化合物可用作爲藥物;單一因子A、B及L可單 獨或呈兩種或兩種以上之混合物以任一種比例使用。該混 合物可經由混合預定量之兩種或兩種以上之因子獲得。另 外因子混合物可根據前述方法直接得自鏈絲菌 DSMZ 14386之釀酵產物之分離。 較佳本發明化合物係根據業界已知且報告於參考文獻 之程序調配成適合供腸道外及/或經口及/或局部投藥用之 調配物。 供腸道外投藥用於治療任何涉及對抗生素敏感之微生 物感染,藥物調配物爲例如於水中帶有適當增溶劑如聚丙 烯乙二醇或二甲基乙醯胺以及界面活性劑例如聚氧伸乙基 山梨糖醇一油酸酯或聚乙氧化蓖麻油於無菌注射用水。較 佳注射用調配物之pH爲7 ±0 .5。若有所需也推薦使用適當 緩衝劑調整製劑之pH。方便地也可使用磷酸鹽作爲緩衝 劑。 另外,活性成分可製備成供重新調製用之凍乾粉末。視 情況需要地,若有所需可添加常見凍乾助劑來獲得粉末形 32 312/發明說明書(補件)/92_〇2/91135061 200409816 式之凍乾材料。 抗生素也可用於適當藥物劑型例如膠囊劑、錠劑或水溶 液劑或懸浮液劑(例如糖漿劑)供經口投藥;或摻混成爲習 知乳膏劑或凍膠劑供局部施用;或調配成爲適合吸入治療 用之液體調配物。 活性成分之劑量係依據多項因素決定,該等因素包括病 人類別、年齡及情況、選用於投藥之特定活性成分及配方、 投藥計劃等。通常對每一單位劑型使用有效抗微生物劑 量。通常以重覆施用/投藥例如每日2至6次爲較佳。有效 劑量通常係於0.5-50毫克/千克/體重/日之範圍。較佳局部 製劑爲含有1 %至1 0 %本發明化合物之軟膏劑。 總而g之處方醫生將可對特定情況的特定病人決定最 理想的劑量。 下列實施例進一步說明本發明但非限制性。 實施例1 :鏈絲菌DSMZ 1 4 3 8 6之發酵以及由收穫之培養 液回收G E 8 1 1 1 2化合物 種子培養菌儲存於-8 之小瓶,用以接種含1 0 0毫升 V6培養基(V6)之5 0 0毫升錐形瓶,V6組成如後(克/升” 葡萄糖20、肉萃取物5、酵母萃取物5、蛋白觫5、水解酪 蛋白3及氯化鈉1 .5。培養基係使用蒸餾水製備,pH以氫 氧化鈉調整至7.5,隨後於12CTC滅菌20分鐘。接種燒瓶 於28°C於旋轉振搖器以200 rpm培養40-4 8小時,然後用 於接種含3升V6培養基之4升生物反應器。培養菌最初 30小時係於27 °C溫度生長,隨後18小時於24 °C生長至接 種時。維持於700 rpm攪拌,通入氣流0.5 v/v/分鐘。此培 33 312/發明說明書(補件)/92-02/91 ] 3 5061 200409816 養菌(1.5升)接種於含200升製造培養基至300升發酵槽, 培養基組成如後(克/升):甘油30、大豆粉15、碳酸鈉5及 氯化鈉2。培養基係使用去離子水製備,pH以氫氧化鈉調 整至7.3,加入30毫升哈戴(Hodag)AFM-5作爲消泡劑。此 培養於28 °C發酵62小時,最初18小時通入氣流60升/分 鐘,然後提高至100升/分鐘(0.5 v/W分鐘)至收穫時。採用 之攪動爲180 rpm。 然後收穫之培養液使用蒸餾水稀釋至200升,加入高福 羅(Hyflo)過濾助劑之後過濾。排出鏈絲菌,濾液藉加入約 600毫升3.25M鹽酸調整至pH3.5。然後GE81112抗生素 混合物以酸形式吸附於2.5升朵威司50W x2陽離子交換樹 脂(陶氏化學公司)於逐批攪拌隔夜後,藉過濾回收樹脂, 排出培養液。二發酵槽如前述平行處理,然後匯集來自各 別操作回合的朵威司樹脂。樹脂(5升)載於管柱(直徑12.5 厘米;床高45厘米)上,使用6升20mM磷酸鈉pH3.5緩 衝液以90毫升/分鐘流速洗滌;然後使用10升20 mM磷酸 鈉pH 3.5緩衝液:甲醇8:2(Wv)混合物洗滌。然後使用257 mM氨水以磷酸緩衝至pH 10進行洗提。收集1升洗提分, 其即刻藉加入磷酸調整至約pH 6。各洗提分之抗生素內容 物係藉生物檢定分析亦即抑制於最低必需培養基(MM)培 養之大腸桿菌及枯草桿菌的生長,以及藉分析HPLC,根 據實施例2所述方法評級。由朵威司樹脂洗提出之洗提分 5 · 1 0匯集,獲得5 . 8升富含GE 8 1 1 1 2化合物混合物之溶 液。溶液樣本(50毫升)經真空濃縮,然後凍乾,獲得1.48 克GE 8 1 1 1 2化合物製劑粗產物。 34 312/發明說明書(補件)/92-02/91135061 200409816 實施例2 G E 8 1 1 1 2因子A、B及B !之分離及純化 如實施例1所得之溶液與1 ·2升聚苯乙烯樹脂HP 20(三 井化學公司)逐批攪拌隔夜。然後藉過濾回收樹脂,載荷於 長7.5厘米、床高27厘米之管柱。然後管柱使用6升l:9(v/v) 甲醇:蒸餾水然後4升3:7(v/x〇混合物,以40毫升/分鐘流 速洗提。收集1升洗提分,藉HP LC分析。最初三洗提分 顯示含有富含因子A之GE 8 1 1 1 2因子混合物,經匯集。 隨後三洗提分富含因子Βι及B,也經匯集。二匯集物經真 空濃縮成小量容積,然後凍乾,獲得分別富含因子A及因 子1加B之3.8克及1.7克固體。 然後藉製備性HPLC(鼻津-LC8A)於西伯理可索(莫克公 司)25 x 2 5 0毫米管柱RP8(7微米粒徑),使用40 mM甲酸銨 且以甲酸調整至pH 4.5,以3.5毫升/分鐘之流速洗提獲得 各別純洗提分。前述抗生素製劑約毫克溶解於3 5 0微 米洗提相,且接受層析術處理。因子A、B!及B典型係於 約9.5、12.4及13.4分鐘後洗提。匯集顯示抗生素含量均 質之重覆層析回合之洗提分,真空濃縮至水殘餘物。然後 將溶液凍乾,再度溶解於40毫升蒸餾水,再度凍乾獲得 116、13、10 毫克抗生素 GE81112 因子 Α、Β!* B。 於配備有S P D - Μ 1 0 A二極體陣列檢測器及Si 1 · 9 A自動注 入器之島津LC 10-AS儀器進行HP LC分析。層析術管柱爲 「阿帝瑪」R P 1 8、5微米’ 2 5 0 X 4 · 6毫米內徑,購自全科 技公司使用40 mM甲酸銨緩衝液藉添加甲酸調整至PH 4.5,以1毫升/分鐘流速進行等梯度方式(Isocratic)洗提。 紫外光檢測係於23 0奈米進行。 35 312/發明說明書(補件)/92-02/91135061 200409816 三種因子係於前述分析HPLC條件下試驗,顯示下列滯 留時間:因子A、14.1分鐘,因子B!、18.4分鐘及因子B、 2 1 . 6分鐘。 【圖式簡單說明】 圖1表示帶有規度化碰撞能25 %於m/z = 644之一質子化 離子於分段後之抗生素GE 81112因子A之MSMS光譜。 圖2表示抗生素GE 81112因子A於潤滑劑糊之I.R.吸收 光譜。 · 圖3表示抗生素GE81112因子A於600MHz於DMSO-d6 及TFA(數滴)測得之UMR光譜。 圖4表示抗生素GE81112因子A於150MHz於DMS〇-d6 及TFA(數滴)測得之質子解除耦合13C-NMR光譜。 圖5表示帶有規度化碰撞能28%於m/z = 65 9之一質子化 離子於分段後之抗生素GE 81112因子B之MS MS光譜。 圖6表示抗生素GE81112因子B於溴化鉀之I.R.吸收光. 譜。 圖7表示抗生素GE81112因子B於600MHz於DMS〇-d6 及TFA(數滴)測得之'H-NMR光譜。 圖8表示抗生素GE81112因子B於150MHz於DMSO-d6 及TFA(數滴)測得之質子解除耦合13C-NMR光譜。 圖9表示帶有規度化碰撞能25 %於m/z = 65 8之一質子化 離子於分段後之抗生素GE 81112因子心之MSMS光譜。 圖10表示抗生素GE 81112因子Βι於600MHz於DMS〇-d6 測得之1 Η - N M R光譜。 圖11表示抗生素GE81112因子Βι於150MHz於DMS〇-d6 36 312/發明說明書(補件)/92-02/91135061 200409816 測得之質子解除耦合]3C-NMR光譜 312/發明說明書(補件)/92-02/91135061 37Antibacteiial Agents "in Current Opinion in Microbiology, 1998, 1,49 5-50 1). Therefore, the GE 81112 compound of the present invention is particularly suitable as a selective therapeutic agent for respiratory infections caused by Moraxella catarrhalis. The compounds of the present invention can be It may be administered as a pharmaceutically acceptable composition, or it may be administered in admixture with a pharmaceutically acceptable carrier. It may also be administered in combination with other antimicrobial agents such as penicillins, cephalosporins, aminoglycosides, and glycopeptides. Combination therapy also includes sequential, simultaneous and separate administration of the active compound, so that the efficacy of the first-administered drug does not completely disappear, and subsequent administration. The compounds of the present invention can be used as drugs; single factors A, B and L can be used alone or in two or Two or more mixtures are used in any ratio. The mixture can be obtained by mixing a predetermined amount of two or more factors. In addition, the factor mixture can be directly obtained from the fermentation product of Streptomyces DSMZ 14386 according to the aforementioned method. Preferred compounds of the present invention are formulated for parenteral administration according to procedures known in the industry and reported in references. And / or oral and / or topical formulations. For parenteral administration for the treatment of any infection involving microorganisms that are sensitive to antibiotics, the formulations are, for example, water with a suitable solubilizer such as polypropylene glycol or Dimethylacetamide and a surfactant such as polyoxyethylene sorbitol monooleate or polyethoxylated castor oil in sterile water for injection. The pH of the formulation for injection is preferably 7 ± 0.5. If If necessary, it is recommended to adjust the pH of the preparation with a suitable buffer. Conveniently, phosphate can also be used as a buffer. In addition, the active ingredient can be prepared as a lyophilized powder for reconstitution. If necessary, if necessary Common freeze-drying auxiliaries can be added to obtain lyophilized materials in powder form 32 312 / Invention Specification (Supplement) / 92_〇2 / 91135061 200409816. Antibiotics can also be used in appropriate pharmaceutical dosage forms such as capsules, lozenges or aqueous solutions Or suspensions (such as syrups) for oral administration; or blended into conventional creams or gels for topical application; or formulated as a liquid formulation suitable for inhalation therapy. Dosage is determined based on a number of factors including patient type, age and condition, specific active ingredients and formulations selected for administration, dosing schedule, etc. Effective antimicrobial doses are usually used for each unit dosage form. Usually repeated administrations / Administration is preferably, for example, 2 to 6 times a day. The effective dose is usually in the range of 0.5-50 mg / kg / body weight / day. The preferred topical formulation is an ointment containing 1% to 10% of the compound of the present invention. The doctor in g will determine the optimal dosage for a specific patient in a specific situation. The following examples further illustrate the invention without limitation. Example 1: Fermentation of Streptomyces DSMZ 1 4 3 8 6 Recovery of GE 8 1 1 1 2 Compound seed culture bacteria was stored in a vial of -8 for inoculation of a 500 ml Erlenmeyer flask containing 100 ml of V6 medium (V6). The composition of V6 is as follows (g / l "Glucose 20, meat extract 5, yeast extract 5, peptone 5, hydrolyzed casein 3, and sodium chloride 1.5. The culture medium was prepared using distilled water, the pH was adjusted to 7.5 with sodium hydroxide, and then sterilized at 12 CTC for 20 minutes. Inoculation flasks were incubated at 28 ° C on a rotary shaker at 200 rpm for 40-4 8 hours, and then used to inoculate a 4 liter bioreactor containing 3 liters of V6 medium. The cultured bacteria were grown at 27 ° C for the first 30 hours, and then grown at 24 ° C for 18 hours until the time of inoculation. Stir at 700 rpm and allow a flow of 0.5 v / v / min. This culture 33 312 / Invention specification (Supplement) / 92-02 / 91] 3 5061 200409816 Inoculate bacteria (1.5 liters) in a fermentation tank containing 200 liters of production medium to 300 liters. The composition of the medium is as follows (g / liter): Glycerin 30, soy flour 15, sodium carbonate 5 and sodium chloride 2. The culture medium was prepared using deionized water, the pH was adjusted to 7.3 with sodium hydroxide, and 30 ml of Hodag AFM-5 was added as an antifoaming agent. This culture was fermented at 28 ° C for 62 hours. The air flow was 60 liters / minute for the first 18 hours, and then increased to 100 liters / minute (0.5 v / W minutes) to harvest time. The agitation used was 180 rpm. The harvested culture solution was then diluted to 200 liters with distilled water, and a Hyflo filter aid was added, followed by filtration. Streptomyces was discharged, and the filtrate was adjusted to pH 3.5 by adding about 600 ml of 3.25 M hydrochloric acid. Then the GE81112 antibiotic mixture was adsorbed in acid form to 2.5 liters of Dowitz 50W x2 cation exchange resin (The Dow Chemical Company), and after stirring overnight in batches, the resin was recovered by filtration and the culture solution was discharged. The two fermentation tanks were processed in parallel as described above, and then Dowes resins from the respective operation rounds were pooled. The resin (5 liters) was loaded on a column (12.5 cm diameter; bed height 45 cm) and washed with 6 liters of 20 mM sodium phosphate pH 3.5 buffer at a flow rate of 90 ml / min; then 10 liters of 20 mM sodium phosphate pH 3.5 Buffer: methanol 8: 2 (Wv) mixture was washed. Elution was then performed with 257 mM ammonia in phosphate buffered pH 10. 1 liter of eluate was collected, which was immediately adjusted to about pH 6 by adding phosphoric acid. The antibiotic content of each elution fraction was graded according to the method described in Example 2 by bioassay analysis, that is, inhibition of growth of E. coli and Bacillus subtilis cultured in the minimum necessary medium (MM), and by analytical HPLC. The eluted fractions 5.10 from Elvis resin were pooled to obtain 5.8 liters of a solution rich in a mixture of GE 8 11 12 compounds. A sample of the solution (50 ml) was concentrated in vacuo and then lyophilized to obtain 1.48 g of a crude product of a GE 8 1 1 12 compound preparation. 34 312 / Invention (Supplement) / 92-02 / 91135061 200409816 Example 2 GE 8 1 1 1 2 Separation and purification of factors A, B and B! The solution obtained in Example 1 and 1.2 liters of polybenzene Vinyl resin HP 20 (Mitsui Chemical Co., Ltd.) was stirred overnight in batches. The resin was then recovered by filtration and loaded on a string of 7.5 cm long and 27 cm bed height. The column was then eluted with 6 liters of 1: 9 (v / v) methanol: distilled water and then 4 liters of 3: 7 (v / x0 mixture) at a flow rate of 40 ml / min. 1 liter of eluate was collected and analyzed by HP LC The initial three-elution fractions showed a factor 8-rich GE 8 1 1 1 2 factor mixture and were pooled. The subsequent three-elution fractions were enriched with factors Bι and B and also pooled. The second pool was concentrated in vacuo to a small amount. The volume was then lyophilized to obtain 3.8 grams and 1.7 grams of solids enriched with factor A and factor 1 plus B, respectively. Then preparative HPLC (Ninjin-LC8A) was used in Sibelico (Mock) 25 x 2 5 0 mm column RP8 (7 micron particle size), using 40 mM ammonium formate, adjusted to pH 4.5 with formic acid, and eluted at a flow rate of 3.5 ml / min to obtain individual pure elution fractions. About mg of the aforementioned antibiotic preparation was dissolved in 3 50 micron eluent phase, and subjected to chromatography. Factors A, B !, and B are typically eluted after about 9.5, 12.4, and 13.4 minutes. Pooled fractions of repeated chromatography rounds showing homogeneous antibiotic content , And concentrated in vacuo to a water residue. The solution was then lyophilized, dissolved again in 40 ml of distilled water, and lyophilized again to obtain 116 13. 10 mg antibiotics GE81112 factor A, B! * B. HP LC analysis was performed on a Shimadzu LC 10-AS instrument equipped with an SPD-M 1 0 A diode array detector and a Si 1 · 9 A autoinjector. Chromatography column was "Adima" RP 18.5, 5 micrometers' 2 5 0 X 4 · 6 mm inner diameter, purchased from All-Technology Company. Use 40 mM ammonium formate buffer to adjust pH to 4.5 by adding formic acid. Isocratic elution was performed at a flow rate of 1 ml / min. UV detection was performed at 230 nm. 35 312 / Instruction Manual (Supplement) / 92-02 / 91135061 200409816 The three factors are under the aforementioned analytical HPLC conditions The following test shows the following retention times: factor A, 14.1 minutes, factor B !, 18.4 minutes, and factor B, 2 1.6 minutes. [Simplified illustration of the figure] Figure 1 shows a regularized collision energy of 25% in m / z = MSMS spectrum of antibiotic GE 81112 factor A after protonation of one of the 644 protonated ions. Figure 2 shows the IR absorption spectrum of antibiotic GE 81112 factor A in lubricant paste. · Figure 3 shows antibiotic GE81112 factor A at 600 MHz. UMR spectra measured on DMSO-d6 and TFA (several drops). Figure 4 shows the resistance Proton decoupling 13C-NMR spectrum of biotin GE81112 factor A measured at 150 MHz in DMS 0-d6 and TFA (several drops). Figure 5 shows one with a regularized collision energy of 28% at m / z = 65 9 MS MS spectrum of protonated ion GE 81112 factor B after segmentation. Figure 6 shows the I.R. absorption spectrum of antibiotic GE81112 factor B on potassium bromide. Figure 7 shows the 'H-NMR spectrum of the antibiotic GE81112 factor B measured at 600 MHz on DMS 0-d6 and TFA (several drops). Fig. 8 shows the 13C-NMR spectrum of proton decoupling measured for antibiotic GE81112 factor B at 150 MHz in DMSO-d6 and TFA (several drops). Figure 9 shows the MSMS spectrum of the antibiotic GE 81112 factor heart with a regularized collision energy of 25% at m / z = 65 8 and a protonated ion. FIG. 10 shows a 1 Η -N M R spectrum of the antibiotic GE 81112 factor B1 at 600 MHz and DMS 0-d6. Figure 11 shows the antibiotic GE81112 factor Bι at 150 MHz at DMS 0-d6 36 312 / Invention specification (Supplement) / 92-02 / 91135061 200409816 Detected proton measurement] 3C-NMR spectrum 312 / Invention Specification (Supplement) / 92-02 / 91135061 37

Claims (1)

200409816200409816 1. 一種抗生素GE 81112因子A,具有下列特徵: A) 質譜係由0.01毫克/毫升於乙腈:水50:50(v/v)之溶液 記錄,於熱費尼根(Thermofinnigan)LCQ戴卡(deca)儀益於 下述電噴霧條件下獲得於644 m/z之一質子化離子:噴霧電 壓:4.7千伏特;毛細溫度:2 5 0 °C ;毛細電壓:9伏特;輸注 模式5微升/分鐘; B) 紅外線光譜術(圖2),係使用以潤滑油糊(nujol mull) 使用IFS-48富立葉轉換分光光度計測定顯示如下主吸收帶 (厘米-丨)·· 3356; 2956; 2855; 2256; 2128; 1 663; 1 5 96 ; 1 45 5 ; 1378 ; 1345 ; 1123 ; 1050 ; 1026 ; 1002 ; 825 ; 764 ; CVH-NMR 光譜(圖 3),於 600 MHz 於 25°C 於 DMS〇-d6 三氟乙酸(數滴)記錄,顯^ 斤下列4信號: 化學位移(ppm) 多樣性 化學位移 (ppm) 多樣性 1.52 b r d 4.70 m 1.57-1.67 m 5.06 d 1.8 1 br d 6.46 br 1.88 m 6.94 s 2.87 dd 7.29 s 2.90 m 7.99 d 3.12 dd 8.17 d 3.15 m 8.30 m 3.65 m 8.57 b r d 3.83 m 8.95 d 312/發明說明書(補件)/92-02/91135061 38 200409816 3.94 b r d 9.06 b r d 4.40 b r s 14.09 b r 4.46 m 14.27 br 4.50 d d -- — D)13C-NMR 光譜(圖 4),於 150MHz 於 5°c 於 DMS〇-d6 及 三氟乙酸(數滴)記錄,顯示下列13C信號 化學位移 多樣性 化學位移 多樣性 (ppm) (ppm) 15.9 t 67.76 t 27.19 t 116.83 d 28.41 t 118.49 d 35.31 t 128.41 s 42.86 t 129.03 s 50.13 d 133.65 d 5 1.30 d 139.66 s 56.86 d 156.73 s 59.7 1 d 167.39 s 64.07 d 170.16 s 65.11 d 171.29 s 66.88 d 171.65 s E )滯留時間1 4 · 1分鐘,係使用分析η P L C島津L C 1 0 - A S 測定,儀器配備有「阿帝瑪」R P 1 8、5微米,2 5 0 X 4.6毫 米內徑管柱;使用4 0 m Μ甲酸銨緩衝液藉添加甲酸調整至 pH 4.5,以1毫升/分鐘流速進行等梯度方式(Isocratic)洗 提;紫外光檢測係於230奈米進行。 39 發明說明書(補件)/92-02/91135061 200409816 2.—種抗生素GE 81112因子B,具有下列特徵: A) 質譜係由0.01毫克/毫升於乙腈:水5 0:5 0(v/v)之溶液 記錄,於熱費尼根LC Q戴卡儀器於下述電噴霧條件下獲得 於65 9 m/z之一質子化離子:噴霧電壓:4.7千伏特;毛細溫 度:25(TC ;毛細電壓:9伏特;輸注模式5微升/分鐘; B) 紅外線光譜術(圖6),係使用溴化鉀使用IFS-48富立 葉轉換分光光度計測定顯示如下主吸收帶(厘米·1): 3 3 5 9 ; 2 9 5 8 ; 2 8 5 2 ; 22 5 8 ; 2 129; 1681 ; 1591 ; 1 45 0; 1 3 8 5; 1 3 4 7 ; 1122; 1072 ; 1025 ; 998 ; 765 〇 ; CVH-NMR 光譜(圖 7),於 600 MHz 於 25°C 於 DMS〇-d6 及三氟乙酸(數滴)記錄,顯ί B下列1H信號: 化學位移 多樣性 化學位移 多樣性 (ppm) (ppm) 1.52 br d 4.60 m 1.57-1.72 m 5.05 d 1.83 b r d 6.46 br 1.90 m 6.48 s 2.63 d d 6.93 s 2.88 dd 7.40 b r s 2.92 m 7.84 d 3.13 br d 8.05 d 3.64 m 8.33 m 3.83 m 8.54 d 3.95 br d 9.00 br d 4.35 br s 11.72 br s 312/發明說明書(補件)/92·02/91135061 40 200409816 4.46 m 11.75 b r s 4.50 dd D广C-NMR光譜(圖8),於150 MHz於 2 5〇C 於 DMS〇- 及三氟乙酸(數滴)記錄,顯示下列13 c信號 ]3c化學位移 多樣性 I3C化學位移 多樣性 (ppm) (ppm) 15.9 t 67.77 t 27.36 t 1 10.3 d 28.40 t 117.85 d 35.47 t 122.5 s 42.8 7 t 128.4 s 50.1 d 139.66 s 5 1.20 d 146.7 s 56.78 d 156.7 s 59.73 d 167.4 s 64.09 d 170.5 s 65.14 d 171.3 s 66.90 d 17 1.38 s E)滯留時間21.6分鐘,係使用分析HPLC島津LC10-AS 測定,儀器配備有「阿帝瑪」RP18、5微米,25 0 X 4.6毫 米內徑管柱;使用40 mM甲酸銨緩衝液藉添加甲酸調整至 PH 4.5,以1毫升/分鐘流速進行等梯度方式(Isocratic)洗 提;紫外光檢測係於23 0奈米進行。 3.—種抗生素GE 81112因子,具有下列特徵: A)質譜係由0.01毫克/毫升於乙腈:水50:5 0(v/v)之溶液 41 312/發明說明書(補件)/92-〇2/91135〇61 200409816 記錄,於熱費尼根LCQ戴卡儀器於下述電噴霧條件下獲得 於6 5 8 m/z之一質子化離子:噴霧電壓:4.7千伏特;毛細溫 度:2 5 0 °C ;毛細電壓:9伏特;輸注模式5微升/分鐘; B^H-NMR 光譜(圖 10),於 600 MHz 於 25°C 於 DMS〇-d6 記錄,顯示下列1 Η信號: 化學位移 多樣性 化學位移 多樣性 (ppm) (ppm) 1.38 br d 4.40 br m 1.56-1.64 m 4.46 m 1.76 m 5.05 d 2.70 m 5.60 b r s 2.82 br s 6.21 br 2.92 m 6.52 br 3.01-3.06 m 6.78 br s 3.49 br m 7.13 br 3.57 b r s 7.80 br d 4.20 b r d d 7.90 br d 4.26 br 8.44 br C)13C-NMR 光譜(圖 11),於 150 MHz 於 2 5°C 於 DMS〇- 記錄,顯示下 列13C信號 化學位移 多樣性 化學位移 多樣性 (ppm) (ppm) 17.95 t 6 6.86 d 27.97 t 111.07 d 29.8 t 118.97 d 312/發明說明書(補件)/92-02/91135061 42 200409816 36.54 t 122.47 s 43.7 5 t 127.88 s 45.65 d 148.08 s 50.52 d 159.18 s 5 1.9 d 169.44 s 57.75 d 171.53 s 61.0 d 171.81 s 64.03 d 173.08 s 66.7 d -- — 〇)滯留時間18.4分鐘,係使用分析^1^島津1^10-八3 測定,儀器配備有「阿帝瑪」R P 1 8、5微米,2 5 0 x 4.6毫 米內徑管柱;使用40 mM甲酸銨緩衝液藉添加甲酸調整至 pH 4.5,以1毫升/分鐘流速進行等梯度方式(iSQCratic)洗 提;紫外光檢測係於2 3 0奈米進行。 4 · 一種製造如申請專利範圍第1至3項中任一項之G E 81112抗生素之方法,該方法包含: -於需氧條件下,於包含可同化碳源、氮源及無機鹽類來 源之水性營養培養基’培養鏈絲菌種 (S t r e p t 〇 m y c e s sp.)DSMZ 1 43 8 6或其維持製造GE 81112抗生素之遺傳能 力之變異株或突變株; •由發酵液回收所得抗生素混合物; -純化回收之抗生素混合物,以及分離三種抗生素GE 81112 因子 A、B 及 B!。 5 · —種混合物’其包含兩種或兩種以上如申請專利範圍 第1至3項中任一項之抗生素GE 8 1 1 1 2因子以任一種比例 43 312/發明說明書(補件)/92-02/91135061 200409816 與其藥物可容許性鹽混合。 6 ·如申請專利範圍第5項之混合物,其爲抗生素ge 8 1 1 1 2 因子以任一種比例形成之混合物,該抗生素GE 8 111 2因子 混合物爲由鏈絲菌DSMZ 1 43 86或其維持可製造GE 81 1 12 抗生素之遺傳能力之GE 81丨12抗生素產生性變異株或突 變株之發酵液分離而得。 7 . —種製造如申請專利範圍第6項之抗生素GE 8 1 Π 2因 子混合物之方法,該方法包含: ' -培養鏈絲菌DSMZ 1 4 3 8 6或其維持可製造GE 81 1 12抗生 素之遺傳能力之突變株或變異株; -由液態培養基回收所得G E 8 1 1 1 2因子之抗生素混合 物;以及 -純化抗生素GE 81112因子混合物。 8.如申請專利範圍第4或7項之方法,其中該鏈絲菌 DSMZ 14386或其維持製造GE 81112抗生素遺傳能力之變 異株或突變株係經過前培養。 9 ·如申請專利範圍第4或7項之方法,其中該回收係於 離子交換樹脂進行,純化係於吸附基體,較好係於聚苯乙 烯或混合聚苯乙烯·二乙烯苯樹脂進行。 1 0 ·如申請專利範圍第4項之方法,其中該抗生素GE 8 1 1 1 2因子A、B及B !之分離係利用層析術進行。 1 1 .如申請專利範圍第1 0項之方法,其中該層析術爲製 備性HPLC技術。 1 2 · —種藥物組成物,包含如申請專利範圍第1至3及5 項中任一項之抗生素。 44 312/發明說明書(補件)/92-02/91135061 200409816 1 3 .如申請專利範圍第1 2項之藥物組成物,包含藥物可 容許性載劑。 1 4. 一種如申請專利範圍第1至3項及5項中任一項之抗 生素之用途,其係用於製造細菌感染治療用藥。 45 312/發明說明書(補件)/92-02/911350611. An antibiotic GE 81112 factor A, which has the following characteristics: A) The mass spectrum is recorded from a solution of 0.01 mg / ml in acetonitrile: water 50:50 (v / v), and it is recorded in Thermofinnigan LCQ ( Deca) Yiyi obtained one of the protonated ions at 644 m / z under the following electrospray conditions: spray voltage: 4.7 kV; capillary temperature: 2 50 ° C; capillary voltage: 9 volts; 5 μl infusion mode / Minute; B) Infrared spectroscopy (Figure 2), using the lubricating oil paste (nujol mull) using IFS-48 Fourier transform spectrophotometer to measure and display the following main absorption band (cm- 丨) · 3356; 2956; 2855; 2256; 2128; 1 663; 1 5 96; 1 45 5; 1378; 1345; 1123; 1050; 1026; 1002; 825; 764; CVH-NMR spectrum (Figure 3) at 600 MHz at 25 ° C at 25 ° C DMS〇-d6 trifluoroacetic acid (several drops) records, showing the following 4 signals: chemical shift (ppm) diversity chemical shift (ppm) diversity 1.52 brd 4.70 m 1.57-1.67 m 5.06 d 1.8 1 br d 6.46 br 1.88 m 6.94 s 2.87 dd 7.29 s 2.90 m 7.99 d 3.12 dd 8.17 d 3.15 m 8.30 m 3.65 m 8.57 b rd 3.83 m 8.95 d 312 / Invention Specification (Supplement) / 92-02 / 91135061 38 200409816 3.94 brd 9.06 brd 4.40 brs 14.09 br 4.46 m 14.27 br 4.50 dd-— D) 13C-NMR spectrum (Figure 4), in Recorded at 150 ° C at 5 ° C in DMS 0-d6 and trifluoroacetic acid (several drops), showing the following 13C signal chemical shift diversity chemical shift diversity (ppm) (ppm) 15.9 t 67.76 t 27.19 t 116.83 d 28.41 t 118.49 d 35.31 t 128.41 s 42.86 t 129.03 s 50.13 d 133.65 d 5 1.30 d 139.66 s 56.86 d 156.73 s 59.7 1 d 167.39 s 64.07 d 170.16 s 65.11 d 171.29 s 66.88 d 171.65 s E 4) 1) Analysis η PLC Shimadzu LC 1 0-AS measurement, the instrument is equipped with "Adima" RP 18.5, 5 micron, 250 X 4.6 mm inner diameter column; use 40 m mM ammonium formate buffer to adjust by adding formic acid Isocratic elution was carried out to pH 4.5 at a flow rate of 1 ml / min; UV detection was performed at 230 nm. 39 Description of the Invention (Supplement) / 92-02 / 91135061 200409816 2. An antibiotic GE 81112 factor B, which has the following characteristics: A) Mass spectrometry is from 0.01 mg / ml to acetonitrile: water 5 0:50 0 (v / v ) Solution records, protonated ions at 65 9 m / z were obtained under the conditions of electrospray on a thermal Fernigan LC Q Dicastal instrument: spray voltage: 4.7 kV; capillary temperature: 25 (TC; capillary Voltage: 9 volts; 5 μl / min in infusion mode; B) Infrared spectroscopy (Figure 6), using potassium bromide and IFS-48 Fourier transform spectrophotometer, shows the following main absorption band (cm · 1): 3 3 5 9; 2 9 5 8; 2 8 5 2; 22 5 8; 2 129; 1681; 1591; 1 45 0; 1 3 8 5; 1 3 4 7; 1122; 1072; 1025; 998; 765 〇 ; CVH-NMR spectrum (Figure 7), recorded at 600 MHz at 25 ° C in DMS 0-d6 and trifluoroacetic acid (several drops), showing the following 1H signals: Chemical shift diversity Chemical shift diversity (ppm) (ppm) 1.52 br d 4.60 m 1.57-1.72 m 5.05 d 1.83 brd 6.46 br 1.90 m 6.48 s 2.63 dd 6.93 s 2.88 dd 7.40 brs 2.92 m 7.84 d 3.13 br d 8.05 d 3.64 m 8.33 m 3.83 m 8.54 d 3.95 br d 9.00 br d 4.35 br s 11.72 br s 312 / Invention Specification (Supplement) / 92 · 02/91135061 40 200409816 4.46 m 11.75 brs 4.50 dd Dguang C-NMR spectrum (Figure 8), recorded at 150 MHz at 2 50 ° C in DMS 0- and trifluoroacetic acid (several drops), showing the following 13 c signal] 3c chemical shift diversity I3C chemical shift diversity (ppm) (ppm) 15.9 t 67.77 t 27.36 t 1 10.3 d 28.40 t 117.85 d 35.47 t 122.5 s 42.8 7 t 128.4 s 50.1 d 139.66 s 5 1.20 d 146.7 s 56.78 d 156.7 s 59.73 d 167.4 s 64.09 d 170.5 s 65.14 d 17 66.90 d 17 1.38 s E) Retention time 21.6 minutes, measured by analytical HPLC Shimadzu LC10-AS, equipped with "Adima" RP18, 5 micron, 25 0 X 4.6 mm id column; 40 mM ammonium formate The buffer was adjusted to pH 4.5 by adding formic acid, and the isocratic elution was performed at a flow rate of 1 ml / min; UV detection was performed at 230 nm. 3.—An antibiotic GE 81112 factor, which has the following characteristics: A) Mass spectrometry is from 0.01 mg / ml in acetonitrile: water 50:50 (v / v) solution 41 312 / Invention specification (Supplement) / 92-〇 2 / 91135〇61 200409816 record, one of the protonated ions obtained at 6 5 8 m / z under the conditions of electrospray on a thermal Fernigan LCQ Dicastal instrument: spray voltage: 4.7 kV; capillary temperature: 2 5 0 ° C; capillary voltage: 9 volts; infusion mode 5 μl / min; B ^ H-NMR spectrum (Figure 10), recorded at 600 MHz at 25 ° C in DMS 0-d6, showing the following 1 Η signal: Chemistry Displacement diversity Chemical displacement diversity (ppm) (ppm) 1.38 br d 4.40 br m 1.56-1.64 m 4.46 m 1.76 m 5.05 d 2.70 m 5.60 brs 2.82 br s 6.21 br 2.92 m 6.52 br 3.01-3.06 m 6.78 br s 3.49 br m 7.13 br 3.57 brs 7.80 br d 4.20 brdd 7.90 br d 4.26 br 8.44 br C) 13C-NMR spectrum (Figure 11), recorded at 150 MHz at 2 5 ° C in DMS 0-, showing the following 13C signal chemical shifts are various Chemical shift diversity (ppm) (ppm) 17.95 t 6 6.86 d 27.97 t 111.07 d 29.8 t 118.97 d 312 / Invention (Supplement) / 92-02 / 91135061 42 200409816 36.54 t 122.47 s 43.7 5 t 127.88 s 45.65 d 148.08 s 50.52 d 159.18 s 5 1.9 d 169.44 s 57.75 d 171.53 s 61.0 d 171.81 s 64.03 d s 66.7 d-〇) Retention time 18.4 minutes, measured by analysis ^ 1 ^ Shimadzu 1 ^ 10-Aug. 3, the instrument is equipped with "Adima" RP 1 8, 5 microns, 2 50 x 4.6 mm inner diameter Column; 40 mM ammonium formate buffer was used to adjust the pH to 4.5 with the addition of formic acid, and the eSQCratic elution was performed at a flow rate of 1 ml / min; UV detection was performed at 230 nm. 4 · A method for manufacturing a GE 81112 antibiotic such as any one of claims 1 to 3 in the scope of patent application, which method comprises:-under aerobic conditions, an assimilable carbon source, a nitrogen source, and an inorganic salt source Aqueous nutrient medium 'culture of Streptomyces sp. DSMZ 1 43 8 6 or its mutant strain or mutant strain which maintains hereditary ability to produce GE 81112 antibiotics; • antibiotic mixture obtained from fermentation broth;-purification Recovered antibiotic mixture, and separation of three antibiotics, GE 81112 Factor A, B, and B !. 5 · —A mixture 'which contains two or more antibiotics such as any one of claims 1 to 3 of the scope of patent application GE 8 1 1 1 2 factor at any ratio 43 312 / Invention Specification (Supplement) / 92-02 / 91135061 200409816 mixed with its drug tolerable salt. 6. The mixture of item 5 in the scope of the patent application, which is a mixture of the antibiotic ge 8 1 1 1 2 factors in any ratio, and the antibiotic GE 8 111 2 factor mixture is made of Streptomyces DSMZ 1 43 86 or maintained The GE 81 丨 12 antibiotic producing mutant strain or mutant strain which can produce the genetic ability of the GE 81 1 12 antibiotic is obtained by separation. 7. A method for manufacturing an antibiotic GE 8 1 Π 2 factor mixture as described in claim 6 of the scope of patent application, the method comprises: '-culture of Streptomyces DSMZ 1 4 3 8 6 or its maintenance can produce GE 81 1 12 antibiotics Mutants or mutants of heritability;-an antibiotic mixture of the factor GE 8 1 1 12 obtained from the liquid culture medium; and-a purified antibiotic GE 81112 factor mixture. 8. The method of claim 4 or 7, wherein the Streptomyces DSMZ 14386 or a mutant strain or mutant strain that maintains hereditary ability to produce the GE 81112 antibiotic is subjected to preculture. 9. The method according to item 4 or 7 of the scope of patent application, wherein the recovery is performed on an ion exchange resin, and purification is performed on an adsorption matrix, preferably on polystyrene or mixed polystyrene · divinylbenzene resin. 10 · The method according to item 4 of the scope of patent application, wherein the antibiotic GE 8 1 1 12 factor A, B and B! Are separated by chromatography. 11. The method of claim 10 in the scope of patent application, wherein the chromatography is a preparative HPLC technique. 1 2 · A pharmaceutical composition comprising an antibiotic such as any one of claims 1 to 3 and 5. 44 312 / Description of the Invention (Supplement) / 92-02 / 91135061 200409816 1 3. If the pharmaceutical composition in the scope of the patent application No. 12 contains a drug tolerable carrier. 1 4. A use of antibiotics according to any one of claims 1 to 3 and 5 of the scope of patent application, which is used for the manufacture of drugs for the treatment of bacterial infections. 45 312 / Invention Specification (Supplement) / 92-02 / 91135061
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