Preparation of androsta-1,4-diene-3,17-dione from sterols using Mycobacterium neoaurum VKPM As-1656 strain

A product of microbiological cleavage of the sterols side chain, androsta-1,4-diene-3,17-dione, is toxic for bacteria, in particular, actinobacteria of the genera Mycobacterium and Arthrobacter. Sterols were transformed into androsta-1,4-diene-3,17-dione by culturing the M. neoaurum VKPM An-1656 strain in a high yield, provided that a sorbent was used for elimination of contact between the bacterial cells and the product. Unlike the cholesterol side chain, the more branched chains of phytosterols were cleaved in the presence of M. neoaurum at a high rate only under turbulent stirring of the culture medium, which intensified the formation of hydrocarbonate ion from NaNI3 in situ.     

Identification of steroid C27 monooxygenase isoenzymes involved in sterol catabolism and stepwise pathway engineering of Mycobacterium neoaurum for improved androst-1,4-diene-3,17-dione production

Journal of Industrial Microbiology & Biotechnology - Cholesterol oxidase, steroid C27 monooxygenase and 3-ketosteroid-Δ1-dehydrogenase are key enzymes involved in microbial catabolism of...     

Spectrophotometric estimation of 4-androstene-3,17-dione and 1,4-androstadiene-3,17-dione during C-1(2)-dehydrogenation by Mycobacterium fortuitum NRRL B-8153

A spectrophotometric method for simultaneously estimating 4-androstene-3,17-dione (AD) and 1,4-androstadiene-3,17-dione (ADD) in a binary mixture has been developed using sulphuric acid chromogens. The method has been used to estimate both AD and ADD during C-1(2)-dehydrogenation by Mycobacterium fortuitum NRRL B-8153.The authors are with the School of Life Sciences, Devi Ahilya Vishwavidyalaya. Vigyan Bhawan, Khandwa Road, Indore-452 001, India.     

Production of androsta-1,4-diene-3,17-dione from cholesterol using two-step microbial transformation

A novel two-step transformation process for the production of androsta-l by microorganisms-diene-3,17-dione (ADD) from a high concetration of cholesterol by microorganisms is proposed. Cholesterol (20 g/l) was initially converted to cholest-4-en-3-one (cholestenone) by an inducible cholesterol oxidase-producing bacterium, Arthrobacter simplex U-S-A-18. The maximum productivity of cholestenone was 8 g/l per day and the molar conversion rate was 80%. Subsequently, a fine suspension of cholestenone (50 g/l), which was prepared directly from the fermentation broth of A. simplex, was converted to ADD by Mycobacterium sp. NRRL B-3683 in the presence of an androstenone adsorbent, Amberlite XAD-7. The maximum productivity of ADD was 0.91 g/l per day and the molar conversion rate was 35%. Correspondence to: W.-H. Liu     

Mycobacterium sp．高效转化植物甾醇为雄甾-1，4-二烯-3，17-二酮的诱变选育

采用紫外线、亚硝基胍复合诱变雄甾-4-烯-3,17-二酮（AD）和雄甾-1,4-二烯-3,17-二酮（ADD）的转化产生菌Mycobacterium sp．,结合平板筛选,获得一株遗传性状稳定单产ADD的突变菌株Mycobacterium sp．-11,其ADD质量浓度达到1246ms／L,比原始菌株（484mg／L）提高了150％,经初步优化后发酵液中ADD最高达到1430mg／L,发酵液中ADD质量占ADD、AD两产物质量总和的比例由70％提高到99．1％。     

Bile acid catabolites accumulated by transposon-induced mutants ofPseudomonas putida: Production of hydroxylated 1,4-androstadiene-3,17-diones

Summary Transposon mutagenesis of a bile acid-utilizingPseudomonas putida strain generated 5 classes of mutants based on their ability to accumulate steroild catabolites. Bile acids (up to 5%) could be fermented using mutant strains, to the appropriate hydroxy-1,4-androstadiene-3,17-dione type product in yields close to theoretical.     

Production of androsta-1,4-diene-3,17-dione from cholesterol using immobilized growing cells of Mycobacterium sp. NRRL B-3683 adsorbed on solid carriers

Summary Living cells of Mycobacterium sp. NRRL B-3683 were immobilized by adsorption on different types of solid carriers in order to produce androsta-1,4-diene-3,17-dione (ADD) from cholesterol. Activated alumina proved to be the most preferred carrier for long-term operation when glucose and peptone were added to the reaction medium. In a repeated-batch process, the maximum productivity of ADD was about 0.19 g/l per day with a molar conversion rate of 77% when 1.0 g/l of cholesterol was added to the reaction medium. The half-life of the immobilized cells was more than 45 days and the system could be reactivated by incubating the immobilized cells in a cell growth medium.     

氨茶碱与柠檬酸盐协同作用促进环磷酸腺苷发酵生产

目的:探究通过抑制磷酸二酯酶活性促进cAMP发酵合成的工艺方法.方法:在7 L发酵罐上进行添加氨茶碱的发酵实验,通过对发酵主要参数、关键酶活性、能量代谢水平等进行分析,针对性提出了氨茶碱与柠檬酸盐协同作用促进cAMP合成的发酵工艺.结果:与对照相比,添加5 mg/L氨茶碱批次的cAMP产量提高25.9％,副产物腺苷浓度...     

里氏木霉液体发酵产纤维素酶的研究

在摇瓶试验基础上,采用里氏木霉(Trichoderma reesei)HC-415菌株进行5L自控罐产纤维素酶深层发酵试验。在通气量为 0.2—0.6vvm、搅拌速度为 400r/min、发酵液pH控制在5.8—6.1的条件下,发酵液的羧甲基纤维素(CMC)酶酶活最高为325.0mg糖/ml,滤纸糖酶(FPA)酶活最高达17.9mg糖/ml。发酵周期为108h。所得冻干纤维素酶粉CMC酶活最高3111IU/g,FPA最高135IU/g ,对发酵液得率平均6.7g/L。酶活总收率CMC酶活平均78.2％,FPA酶活平均73.5％。     

黑曲霉A3木聚糖酶固体发酵研究

筛选了一株高产木聚糖酶的黑曲霉Ａ３菌株,研究了其在固体培养基中的发酵条件。该菌最适培养条件为：起始ｐＨ４．６。２８℃,１ｍｌ孢子悬液接种量,蔗渣粉：麸皮为１．５：１,发酵３天,木聚糖酶活力可达５１４７ＩＵ／ｇ培养基干重。氮源组成,温度、ｐＨ及发酵时间对曲中木聚糖酶和纤维素酶的比例有较大影响。与液体发酵相比,粗酶的最适反应温度均为５５℃,最适反应ｐＨ值分别为４．６和４．２,在不同温度下保温１ｈ,测得     

Large-Scale Production of Coenzyme F420-5,6 by Using Mycobacterium smegmatis

Production of coenzyme F₄₂₀ and its biosynthetic precursor FO was examined with a variety of aerobic actinomycetes to identify an improved source for these materials. Based on fermentation costs, safety, and ease of growth, Mycobacterium smegmatis was the best source for F₄₂₀-5,6. M. smegmatis produced 1 to 3 μmol of intracellular F₄₂₀ per liter of culture, which was more than the 0.85 to 1.0 μmol of F₄₂₀-2 per liter usually obtained with Methanobacterium thermoautotrophicum and ~10-fold higher than what was previously reported for the best aerobic actinomycetes. An improved chromatography system using rapidly flowing quaternary aminoethyl ion-exchange material and Florisil was used to more quickly and easily purify F₄₂₀ than with previous methods.     

Production of Acetylacetoin by Bacterial Fermentation

Bacillus sp. YUF-4 did not produce acetylacetoin with general culture media, such as bouillon medium containing glucose or acetoin. When diacetyl was added to a medium cultured for 18–20 h in the presence of glucose or acetoin, AAC was produced as culture continued. AAC was assayed by GLC with a Carbowax 20M capillary column. The AAC produced was purified by several steps: the final HPLC using a Shodex E411 column was effective. The yield of AAC was 346 mg per liter of the medium (7.5% recovery) and the purity was 97%. AAC was identified by ¹H-NMR and ¹³C-NMR.     

Strategy for the Improvement of Prodigiosin Production by a Serratia marcescens Mutant through Fed-Batch Fermentation

A Serratia marcescens mutant for prodigiosin production was obtained by u.v. mutation with rational screening methods and a two-step feeding strategy was used to increase its productivity. In flasks, the mutant strain B6 gave a 2.8-fold higher prodigiosin production than that of the parent strain with glycerol as a carbon source. In a 5-l bioreactor, with a two-step feeding strategy in which glucose was selected as the initial carbon source in the fermentation media and glycerol was fed as a ‘prodigiosin inducer’, it gave a 7.8 times higher prodigiosin production (583 mg/l) than the parent stain with the original cultivation mode.     

酿酒酵母L610利用菊糖生产乙醇发酵条件的研究

以1株能够直接利用菊糖产乙醇的酿酒酵母L610为出发菌株,对其利用菊糖生产乙醇的发酵条件进行了一系列研究。结果表明,L610最适乙醇发酵温度为37℃,且40℃高温发酵对其产乙醇能力无显著影响;L610对酸性发酵环境有良好的耐受性,当发酵液p H值降至3.5时,其糖醇转化率及乙醇产量仍保持较高水平;以0.025~0.10 vvm的通气量通气12 h有利于L610发酵菊糖产乙醇;L610对350 g/L的高浓度菊糖有良好的转化率,乙醇浓度和生产强度分别达到129 g/L和1.35 g/(L·h);当直接以300 g/L菊芋粗粉为唯一底物进行发酵时,L610发酵产乙醇浓度达到89.6 g/L,为理论产量的78.1%。本研究所取得的成果为酿酒酵母一步法发酵菊芋生产乙醇的工业化发展提供参考。     

不同甲醇流加策略对重组毕赤醇母高密度发酵生产水蛭素的影响

考察了不同甲醇流加策略对毕赤酵母高密度发酵生产水蛭素的影响。溶氧控制法不能有效地防止甲醇的过量流加。气相色谱离线检测法虽然防止了甲醇流加过量 ,但甲醇浓度的波动较大。利用甲醇传感器在线检测控制甲醇的流加可维持较恒定的甲醇浓度。在流加甲醇的同时 ,以限制性速率流加甘油可以增加表达期间的能量供应 ,提高产物的表达量。经优化后 ,采用甲醇甘油混合流加时细胞干重达到 16 2g L ,水蛭素活性达到 2 4×10 4ATU mL ,即 1 7g L。     

不同甲醇流加策略对重组毕赤酵母高密度发酵生产水蛭素的影响

考察了不同甲醇流加策略对毕赤酵母高密度发酵生产水蛭素的影响。溶氧控制法不能有效地防止甲醇的过量流加。气相色谱离线检测法虽然防止了甲醇流加过量,但甲醇浓度的波动较大。利用甲醇传感器在线检测控制甲醇的流加可维持较恒定的甲醇浓度。在流加甲醇的同时,以限制性速率流加甘油可以增加表达期间的能量供应,提高产物的表达量。经优化后,采用甲醇甘油混合流加时细胞干重达到162g/L,水蛭素活性达到24×10⁴ATU/mL,即1.7 g/L。      

利用肌苷发酵废液生产单细胞蛋白的研究

我国在利用微生物降解酒精废液、造纸厂废液和味精厂废液等方面已有许多报道,但是,利用肌苷发酵废液作为底物进行单细胞生产还未见报道。同时,提取肌苷后的发酵废液,其营养成份仍很丰富,其中,还原糖含量约为2％,总氮含量为300mg/L～400mg/L,以及一些无机盐。COD值高达186276mg/L。目前,一般肌苷生产厂都将废液排放掉,这不仅严重地污染了环境,而且造成很大的浪费。有鉴于此,本课题进行了菌种的筛选和驯化以及工艺方面的试验。     

氨水流加用于粪产碱杆菌热凝胶发酵

热凝胶是粪产碱杆菌(Alcaligenes faecalis)在氮源限制条件下生成的水不溶性胞外多糖,分泌到胞外后就附着在菌体外壁,因此在细胞生长期提高生物量对促进热凝胶合成有重要意义。热凝胶分批发酵时, 起始NH4Cl浓度提高到3.6 g/L时能促进菌体生长和热凝胶合成,但是过量NH4Cl会抑制热凝胶合成,且生物量提高不是很明显。为了进一步提高菌体浓度, 在菌体生长期, 氨水取代NaOH溶液进行流加控制pH为7.0, 随后又用2 mol/L NaOH控制pH 5.6。实验表明, 氨水流加使菌体浓度大大提高,流加24 h使菌体浓度达到18.8 g/L。但是菌体浓度过高也会抑制热凝胶的合成,在氨水流加14 h时,菌体浓度在11.9 g/L左右, 热凝胶产量最高（72 g/L）。     

氨水流加用于粪产碱杆菌热凝胶发酵

热凝胶是粪产碱杆菌(Alcaligenes faecalis)在氮源限制条件下生成的水不溶性胞外多糖,分泌到胞外后就附着在菌体外壁,因此在细胞生长期提高生物量对促进热凝胶合成有重要意义。热凝胶分批发酵时, 起始NH4Cl浓度提高到3.6 g/L时能促进菌体生长和热凝胶合成,但是过量NH4Cl会抑制热凝胶合成,且生物量提高不是很明显。为了进一步提高菌体浓度, 在菌体生长期, 氨水取代NaOH溶液进行流加控制pH为7.0, 随后又用2 mol/L NaOH控制pH 5.6。实验表明, 氨水流加使菌体浓度大大提高,流加24 h使菌体浓度达到18.8 g/L。但是菌体浓度过高也会抑制热凝胶的合成,在氨水流加14 h时,菌体浓度在11.9 g/L左右, 热凝胶产量最高（72 g/L）。