利用响应面法优化L-组氨酸摇瓶发酵培养基

通过单因素实验对L-组氨酸产生菌LGS4的发酵培养基成分进行筛选,确定了3个影响较大的重要因素,即酵母膏、尿素、硫酸镁。在此基础上,采用二次响应面分析法进行回归分析,得到各因素的最佳水平值。经5批培养验证,预测值与验证试验平均值接近。优化后培养基组成为(g.L-1):蔗糖150,硫酸铵50,酵母膏10,尿素1.2,MgSO42.2,KH2PO41.5,K2HPO40.5,Na2HPO40.5。优化后的发酵培养基使LGS4菌株的L-组氨酸产量提高了15.25%。     

Selection of a strain of Aspergillus for the production of citric acid from pineapple waste in solid-state fermentation

Aspergillus foetidus ACM 3996 (=FRR 3558) and three strains of Aspergillus niger ACM 4992 (=ATCC 9142), ACM 4993 (=ATCC 10577), ACM 4994 (=ATCC 12846) were compared for the production of citric acid from pineapple peel in solid-state fermentation. A. niger ACM 4992 produced the highest amount of citric acid, with a yield of 19.4g of citric acid per 100g of dry fermented pineapple waste under optimum conditions, representing a yield of 0.74g citric acid/g sugar consumed. Optimal conditions were 65% (w/w) initial moisture content, 3% (v/w) methanol, 30°C, an unadjusted initial pH of 3.4, a particle size of 2mm and 5ppm Fe²⁺. Citric acid production was best in flasks, with lower yields being obtained in tray and rotating drum bioreactors.     

Production of penicillic acid by Aspergillus sclerotiorum CGF

The production of penicillic acid by Aspergillus sclerotiorum CGF for the biocontrol of Phytophthora disease was investigated in submerged fermentation using media composed of different nutrients. Soluble starch was found to be the most effective substrate among the carbon sources used, and produced the highest penicillic acid concentration of 2.98 mg ml(-1). When organic nitrogen sources were used, pharmamedia, yeast extract, and polypeptone-S were found to be suitable organic nitrogen sources (2.46-2.71 mg ml(-1)). The production of penicillic acid was not detected in when inorganic nitrogen sources were used. Only Na2HPO4, among the metal ions and phosphate salts tested, increased the production of penicillic acid (approximately 20%). When A. sclerotiorum CGF was cultured in optimal medium [8.0% (w/v) soluble starch, 0.6% (w/v) yeast extract, and 0.3% (w/v) Na2HPO4], maximum penicillic acid concentration (approximately 9.40 mg ml(-1)) and cell mass (approximately 17.4 g l(-1)) were obtained after 12 days.     

大豆根瘤菌HH103菌株培养基的筛选与优化

以快生型大豆根瘤菌HH103菌株为供试菌株,采用单因素碳氮源利用试验和正交设计试验,确定最佳培养基及其配方。结果表明：该菌株在YMA中生长良好,最佳碳源为蔗糖,最佳氮源为酵母膏,最佳培养基成分配方（g/L）：蔗糖11,酵母膏0.9,K2HPO4 0.5,MnSO4 0.005,CaCl2 0.1,KH2PO4 0.5,MgSO4 0.2,KNO30.77,（NH4）2HPO4 0.33,FeCl3 0.005,pH 7.2。     

Optimization of a cultural medium for bacteriocin production by Lactococcus lactis using response surface methodology.

The medium composition for bacteriocin production by Lactococcus lactis ATCC 11454 was optimized using response surface methodology. The selected six factors based on CM medium were sucrose, soybean peptone, yeast extract, KH(2)PO(4), NaCl, and MgSO(4).7H(2)O. Fractional factorial designs (FFD) and the path of steepest ascent were effective in searching for the main factors and approaching the optimum region of the response. By a 2(6-2) FFD, sucrose, soybean peptone, yeast extract, KH(2)PO(4) were found to be significant factors and had positive effects on cell growth, however, only soybean peptone and KH(2)PO(4) were shown to be the two significant factors for bacteriocin production and had negative and positive effects, respectively. The effects of the two main factors on bacteriocin production were further investigated by a central composite design and the optimum composition was found to be 1% sucrose, 0.45% soybean peptone, 1% yeast extract, 2.84% KH(2)PO(4), 0.2% NaCl, and 0.02% MgSO(4) x 7H(2)O. The optimal medium allowed bacteriocin yield to be doubled compared to CM medium.     

4-丁内酰胺水解酶法制备γ-氨基丁酸

以吡咯烷酮为唯一碳源,从采集的土样中分离、筛选得到具有4-丁内酰胺水解酶活性的菌株.采用响应面分析法对该菌株的产酶培养基组分进行了优化研究并对酶促转化反应条件也进行了研究.结果表明:编号为HHSW-16的菌株水解活性最高.优化后的培养基组成为:葡萄糖11.50 g·L-1,牛肉膏6.35 g·L-1,酵母粉5.58 g...     

Acetobacter xylinum生产纤维素的最适培养基成分

探索出胶醋杆菌在摇瓶培养最适培养基成分为蛋白胨浓度１．０％、酵母膏０．５％、葡萄糖浓度２．０％、柠檬酸０．１１５％、乙醇１％、Ｎａ２ＨＰＯ４０．５％,ｐＨ６．０,１６０ｒ／ｍｉｎ的条件下进行摇瓶培养,细菌纤维素最大产量为７．５５ｇ／ｌ。     

Response surface methodology for the optimization of keratinase production in culture medium containing feathers produced by Kocuria rosea

A 43-fold increase in keratinase production by Kocuria rosea was achieved in batch fermentation using response surface methodology. Factorial designs were used to select the components of a culture medium that showed a significant effect on keratinase production. An orthogonal-central composite experimental design was performed, with only two (feathers and magnesium) from nine initial compounds being further analyzed by response surface methodology. An optimum keratinase production of 14 886.9 U/mg was obtained with the following medium composition (per litre): NH4Cl, 0.3 g; NaCl, 0.3 g; K2HPO4, 3.2 g; KH2PO4, 4.0 g; MgSO4.6H2O, 0.5 g; yeast extract, 0.1 g; and finely milled feathers, 30 g. The medium was shaken at 400 r/min with an incubation period of 14 h at 40 degrees C.     

Optimal fermentation conditions for enhanced glutathione production by Saccharomyces cerevisiae FF-8

The influence of feedstock amino acids, salt, carbon and nitrogen sources on glutathione production by Saccharomyces cerevisiae FF-8 was investigated. Glucose, yeast extract, KH2PO4, and L-cysteine were found to be suitable feedstock. Highest glutathione production was obtained after cultivation with shaking for 72 h in a medium containing glucose 3.0% (w/v), yeast extract 3.0%, KH2PO4 0.06% and L-cysteine 0.06%. The glutathione concentration achieved using this medium increased 2.27-fold to 204 mg/l compared to YM basal medium.     

拉曼被孢霉产γ-亚麻酸的发酵条件优化

对影响发酵产γ-亚麻酸的因素（温度、N源、P源等）进行单因素考察。结果发现,各因素对拉曼被孢霉（Mortierella ramanniana NBRC 8187）产γ-亚麻酸均有不同程度的影响。通过正交试验设计对KH2PO4、NaNO3、酵母膏和温度进行了L9（34）试验设计,以γ-亚麻酸产量为优化目标,直观分析得出影响产量的因素大小顺序为酵母膏、温度、KH2PO4、NaNO3,最终确定最佳的培养条件：酵母膏5 g/L、25℃、KH2PO41 g/L、NaNO33 g/L。在此条件下,检测得出在第5天γ-亚麻酸产量达到0.968 g/L,相比优化前（0.583 g/L）提高了66%。     

Utilization of prawn waste for chitinase production by the marine fungus Beauveria bassiana by solid state fermentation

Prawn waste, a chitinous solid waste of the shellfish processing industry, was used as a substrate for chitinase production by the marine fungus Beauveria bassiana BTMF S10, in a solid state fermentation (SSF) culture. Theprocess parameters influencing SSF were optimized. A maximum chitinase yield of 248.0 units/g initial dry substrate (U/gIDS) was obtained in a medium containing a 5:1 ratio (w/v) of prawn waste/sea water, 1% (w/w) NaCl,2.5% (w/w) KH2PO4, 425–600m substrate particle size at 27°C, initial pH 9.5, and after 5 days of incubation. The presence of yeast extract reduced chitinase yield. The results indicate scope for the utilization of shellfish processing (prawn) waste for the industrial production of chitinase by using solid state fermentation.     

Factors affecting mycelial biomass and exopolysaccharide production in submerged cultivation of Antrodia cinnamomea using complex media

Submerged cultures were used to identify growth-limiting nutrients by Antrodia cinnamomea strains. The mycelial biomass and EPS production by A. cinnamomea BCRC 35396 were markedly higher than other A. cinnamomea strains. A relatively high C/N ratio was favorable for both the mycelial growth (5.41 g/l) and EPS production (0.55 g/l); the optimum ratio was 40. The glucose was available utilized preferentially for mycelial growth, rather than for EPS production. Flushing the culture medium with nitrogen had a stimulating effect on both mycelial growth and EPS production. In addition, peptone, yeast extract and malt extract appeared to be important and significant component for EPS production. Phosphate ion, magnesium ion and thiamine were probably not essential for mycelial growth. By optimizing the effects of additional nutrition, the results showed that 5% (w/v) glucose, 0.8% (w/v) peptone, 0.8% (w/v) yeast extract, 0.8% (w/v) malt extract, 0.03% (w/v) KH2PO4, 0.1% (w/v) MgSO4 .7H2O and 0.1% (w/v) thiamine could lead to the maximum production of EPS (1.36 g/l).     

Production of l-Glutamine by a Penicillin-Resistant Mutant of Flavobacterium rigense

To establish a practical method for the fermentative production of l-glutamine, cultural conditions for the accumulation of a large amounts of l-glutamine were investigated by using Flavobacterium rigense 703, which was previously reported by us as a l-glutamine-producing mutant. As a result, a yield of 25 mg of l-glutamine per ml was obtained after a 48-h cultivation in a medium containing glucose, yeast extract, (NH(4))(2)-fumarate, KH(2)PO(4), K(2)HPO(4), MgSO(4).7H(2)O, and CaCO(3) (pH 6.4). Accumulation of l-glutamine was dependent upon the concentration of (NH(4))(2)-fumarate, and a suboptimum growth at a relatively high concentration of (NH(4))(2)-fumarate was essential for the maximum production of l-glutamine. At the optimum conditions, glutamic acid was formed as a by-product at a concentration of less than 1 mg/ml, but accumulation of the other amino acids was negligible. The product was isolated from the culture broth and readily purified by anion-exchange chromatography. The pure crystals of l-glutamine obtained in an 80% yield were optically and chromatographically pure.     

Utilisation of fruits waste for citric acid production by solid state fermentation

A solid state fermentation method was used to utilise pineapple, mixed fruit and maosmi waste as substrates for citric acid production using Aspergillus niger DS 1. Experiments were carried out in the presence and absence of methanol at different moisture levels. In the absence of methanol the maximum citric acid was obtained at 60% moisture level whereas in the presence of methanol the maximum citric acid was obtained at 70% moisture level. The stimulating effect of methanol was less at lower moisture level. The inhibitory effect of metal ions was also not observed and maximum citric acid yield of 51.4, 46.5 and 50% (based on sugar consumed) was obtained from pineapple, mixed fruit and maosmi residues, respectively.     

Production and properties of the linamarase and amygdalase activities of Penicillium aurantiogriseum P35.

The effects of medium composition on the production of beta-glucosidase (amygdalase and linamarase) by Penicillium aurantiogriseum P35 were studied and the medium optimized as follows (g/l of deionized water): pectin, 10.0; (NH4)2SO4, 8.0; KH2PO4, 8.0; Na2HPO4, 2.8; MgSO4.7H2O, 0.5; yeast extract, 4.0; initial pH 6.0. When grown in a bench fermenter on this medium, the fungus produced 50.5 mU of amygdalase and 9.4 mU of linamarase per ml of culture broth. Two beta-glucosidases (PGI and PGII), each having amygdalase and linamarase activities, were recovered from the culture broth and purified; their relative molecular weights, as native enzymes, were estimated to be about 247,000 and 147,000, respectively. Both enzymes showed the same optimum pH (6.0) but different optimum temperatures (55 and 60 degrees C for PGI and PGII, respectively). Thermostability (10 min at 60 degrees C) and half-life of enzyme activity (7 hours at 60 degrees C) of PGII were higher than those of PGI (10 min at 50 degrees C and 2 hours at 55 degrees C, respectively). A wide range of cyanogenic glycosides (such as tetraphyllin B, epivolkenin, gynocardin, passibiflorin, prunasin, taxiphyllin, amygdalin, lucumin, sambunigrin, dhurrin, linamarin and cardiospermin sulfate) were hydrolyzed by both enzymes.     

Screening and optimization of nutritional factors for higher dextransucrase production by Leuconostocmesenteroides NRRL B-640 using statistical approach

To improve dextransucrase production from Leuconostocmesenteroides NRRL B-640 culture medium was screened and optimized using the statistical design techniques of Plackett-Burman and response surface methodology (RSM). Plackett-Burman design with six variables viz. sucrose, yeast extract, K2HPO4, peptone, beef extract and Tween 80 was performed to screen the nutrients that were significantly affecting dextransucrase production. The variables sucrose, K2HPO4, yeast extract and beef extract showed above 90% confidence levels for dextransucrase production and were considered as significant factors for optimization using response surface methodology. 2(4)-central composite design was used for RSM optimization. The experimental results were fitted to a second-order polynomial model which gave a coefficient of determination R2=0.95. The optimized composition of 30g/l sucrose, 18.9g/l yeast extract, 19.4g/l K2HPO4 and 15g/l beef extract gave an experimental value of dextransucrase activity of 10.7U/ml which corresponded well with the predicted value of 10.9U/ml by the model.     

桔青霉生产核酸酶的发酵条件研究

对通过紫外线和60Co两次育种得到的桔青霉W48高产菌株培养基的单组分和发酵条件进行了优化,最后又用正交实验对培养基的各组分的浓度进行了优化。得到了产酶量最高的培养基组分(质量分数)是:KH2PO40.05%,K2HPO40.03%,酵母膏+蛋白胨0.7%,CaCl20.02%,MgSO40.04%,ZnSO40.03%,葡萄糖5%,pH5.5。最佳发酵条件是:接种量10%,装液量50 mL,摇床转速180 r/min,温度30℃,发酵时间66 h。用最佳培养基和最佳发酵条件发酵生产核酸酶的酶活力为758.10 U/mL,原始菌种产核酸酶的酶活力为272.26 U/mL,提高了2.78倍。     

聚乙烯醇降解酶产生菌的分离的发酵条件

A bacterium D8 strain which high efficiently degrading PVA was isolated from waste water of factory. The strain possesses the abilities of completely degrading 0.5 per cent of PVA (500, 1700) included in the culture medium for four days. It was identified Pseudomonas pseudoalcaligenes. Fermentation conditions of the strain have been investigated. The suitable medium consisted of PVA 1.5% (NH4)2SO40.1%, K2HPO4 0.24%, KH2PO4 0.04%, MgSO4.7H2O 0.035%, NaCl 0.01%, FeSO4 0.001%, yeast extract 0.15%, pH 7.5. The optimal condition for enzyme production are as follows: 250 ml shake filled with 30 ml medium, 30 degrees C, 160n/min incubation period 72 h. Under such conditions enzyme activity is highest.     

Production of citric acid from starch-hydrolysate by Aspergillus niger

The present investigation explored the possible use of a rarely used agro-industrial by-product, maize starch-hydrolysate, for economic production of citric acid. To achieve this, seventeen strains of Aspergillus niger were screened for their capacity to produce citric acid using starch-hydrolysate as a substrate. The most efficient strain, ITCC-605 was selected for further improvement in citric acid content by mutation. Mutants developed by treatment with EMS and UV, singly and in combination, produced citric acid in the range of 0.51-64.7 g kg(-1) of glucose consumed. The mutant UE-1 produced the maximum citric acid which was about 130 times more than that produced by the parent strain, ITCC-605. For further increase in citric acid production from this substrate, the cultural conditions were optimized: concentration of starch-hydrolysate, 15% (glucose equivalent); ammonium nitrate, 0.25%; KH2PO4, 0.15%; nicotinic acid, 0.0001% and initial pH of 2.0. Under these conditions, the mutant strain UE-1 yielded 490 g citric acid kg(-1) of glucose consumed in 8 days of incubation at 30 degrees C. The productivity of 341 mgl(-1)h(-1) corresponded to 49% substrate conversion to citric acid.     

High-level production of astaxanthin by Xanthophyllomyces dendrorhous mutant JH1 using statistical experimental designs

Medium composition was optimized for high-level production of astaxanthin by Xanthophyllomyces dendrorhous mutant JH1 using statistical experimental designs. Glucose and yeast extract were the most important factors affecting astaxanthin production. Glucose 3.89%, yeast extract 0.29%, KH2PO4 0.25%, MgSO4 0.05%, MnSO4 0.02%, and CaCl2 0.01% were optimum for high-level production of astaxanthin. Under optimized conditions, the maximum concentration of astaxanthin obtained after 7 d of cultivation was 36.06 mg/l. The concentration of astaxanthin predicted by a polynomial model was 36.16 mg/l.