高产纤维素酶枯草芽胞杆菌S-16的筛选及其发酵工艺优化

利用刚果红鉴别培养基及基础液体筛选培养基进行菌种筛选,从新疆盐碱地分离得到的16株菌株中筛选获得一株产纤维素酶活力较高的菌株S-16,对该菌株进行16SrDNA鉴定,确定该菌为枯草芽胞杆菌(Bacillus subtilis)。对S-16发酵产纤维素酶的主要影响因素进行研究,分别考察了碳源、氮源、培养基初始pH和接种量等因素对发酵产纤维素酶的影响。结合单因素影响实验得到优化后的培养基配方为:羧甲基纤维素钠1.5%,酵母粉1%,NaCl 1%,MgSO_4·7H_2O 2‰,KH_2PO_4·3H_2_O 1‰。优化后的发酵条件为:初始pH为8,接种量1%,种龄8h,培养时间48h。经过发酵工艺优化,S-16产生的羧甲基纤维素酶活(CMCase)和滤纸酶活(FPase)分别达到4.64IU/mL和0.46IU/mL,与初始培养条件下的酶活相比分别提高了3.14倍和1.30倍。本研究得到的枯草芽胞杆菌S-16及其优化发酵工艺为秸秆的快速腐熟和高产纤维素酶的应用奠定了基础。     

Components of fermentation medium regulate bacteriocin synthesis by the recombinant strain Lactococcus lactis subsp. lactis F-116

The regulation of the synthesis of bacteriocin produced by the recombinant strain Lactococcus lactis subsp. lactis F-116 has been studied. The synthesis is regulated by the components of the fermentation medium, the content of inorganic phosphate (KH2PO4), yeast autolysate (source of amine nitrogen), and changes in carbohydrates and amino acids. The strain was obtained by fusion of protoplasts derived from two related L. lactis subsp. lactis strains, both exhibiting a weak ability to synthesize the bacteriocin nisin. Decreasing the content of KH2PO4 from 2.0 to 1.0 or 0.5% caused bacteriocin production to go down from 4100 to 2800 or 1150 IU/ml, respectively; the base fermentation medium contained 1.0% glucose, 0.2% NaCl, 0.02% MgSO4, and yeast autolysate (an amount corresponding to 35 mg % ammonium nitrogen). The substitution of sucrose for glucose (as the source of carbon) increased the antibiotic activity by 26%, and the addition of isoleucine, by 28.5%. Elevation of the concentration of yeast autolysate in the low-phosphate fermentation medium stimulated both the growth of the lactococci and the synthesis of bacteriocin. Introduction of 1% KH2PO4, yeast autolysate (in an amount corresponding to 70 mg % ammonium nitrogen), 2.0% sucrose, and 0.1% isoleucine increased the bacteriocin-producing activity of the strain by 2.4 times.     

细菌素发酵培养基的优化及动力学初步分析

用响应面方法对Lactococcus lactis生产细菌素乳链菌肽的培养基进行了优化。首先用部分重复因子实验对培养基组份蔗糖,大豆蛋白胨,酵母粉,KH₂PO₄,NaCl,MgSO₄·7H2O对乳链菌肽的影响进行评价,并找出主要影响因子为大豆蛋白胨和磷酸二氢钾,前者为负影响,后者为正效应,其它组份对乳链菌肽产量的影响不显著。第二步用最陡爬坡路径逼近最大响应区域。最后用中心组合设计及响应面分析确定主要影响因子的最佳浓度。菌株在优化培养基中的乳链菌肽产量增加1倍为2150(IU/mL)。动力学分析表明,菌株生长与细菌素的产生为部分耦联型,进入对数中期菌体比生长速率和细菌素比产率在优化培养基中均大于优化前培养基。     

Effects of fed-batch fermentation and pH profiles on nisin production in suspended-cell and biofilm reactors

A biofilm reactor not only shortens the lag phase of nisin production, but also enhances nisin production when combined with an appropriate pH profile. Due to the substrate inhibition that takes place at high levels of carbon source, fed-batch fermentation was proposed as a better alternative for nisin production. In this study, the combined effects of fed-batch fermentation and various pH profiles on nisin production in a biofilm reactor were evaluated. The tested pH profiles include 1) a constant pH profile at 6.8 (profile 1), 2) a constant pH profile with an autoacidification after 4 h (profile 2), and 3) a step-wise pH profile with pH adjustment every 2 h (profile 3). When profile 1 was applied, fed-batch fermentation enhanced nisin production for both suspended-cell (4,188 IU ml⁻¹) and biofilm (4,314 IU ml⁻¹) reactors, yielded 1.8- and 2.3-fold higher nisin titer than their respective batch fermentation. On the other hand, pH profiles that include periods of autoacidification (profiles 2 and 3) resulted in a significantly lower nisin production in fed-batch fermentation (2,494 and 1,861 IU ml⁻¹ for biofilm reactor using profile 2 and 3, respectively) due to toxicity of excess lactic acid produced during the fermentation. Overall, this study suggested that fed-batch fermentation can be successfully used to enhance nisin production for both suspended-cell and biofilm reactors.     

Production, purification and characterization of thermophilic lipase from Bacillus sp. THL027

A low-cost medium, MGRS, has been developed for growth and lipase production from Bacillus THL027 at 65 degrees C and pH 7.0. MGRS was composed of 2% (v/v) buffer solution (7.3% (w/v) Na(2)HPO(4), 3.2% (w/v) KH(2)PO(4), pH 7.2), 40 microg ml(-1) FeSO(4) and 40 microg ml(-1) MgSO(4), 0.1% (w/v) (NH(4))(2)SO(4) supplemented with 3% NaCl, 0.1% glucose, 1.0% rice bran oil and 0.5% (w/v) rice bran. The lipase was purified 2.6-fold to apparent homogeneity by ultrafiltration and gel filtration chromatography. Its molecular mass was 69 kDa. The purified enzyme was characterized for its general physical properties.     

A glycerol-inducible thermostable lipase from Bacillus sp.: medium optimization by a Plackett-Burman design and by response surface methodology

The production of a neutral lipase from a Bacillus sp. was improved tremendously (193-fold) following media optimization involving both the "one-at-a-time" and the statistical designing approaches. The present lipase was poorly induced by oils, instead its production was induced in the presence of sugars and sugar alcohols, mainly galactose, lactose, glycerol, and mannitol. A high inoculum density of 15% v/v (A550 = 0.8) led to maximum lipase production. Interestingly, the enzyme induction was growth independent, a property very different from most of the lipases investigated to date. The optimal composition of the growth medium to achieve maximum lipase production was determined to be as follows: NH4Cl, 35 g x L(-1); glycerol, 10 mL x L(-1); K2HPO4, 3 g x L(-1); KH2PO4, 1 g x L(-1); MgSO4.7H2O, 0.1 g x L(-1); glucose, 2 g x L(-1); MgCl2, 0.6 mmol x L(-1), with 15% inoculum density and an incubation period of 24 h. About 62 U x mL(-1) of enzyme production was achieved in the optimized medium.     

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.     

Resistance of Lactobacillus casei in plastic-composite-support biofilm reactors during liquid membrane extraction and optimization of the lactic acid extraction system

Lactic acid fermentations were performed with plastic-composite-support (PCS) disks in solvent-saturated media with Lactobacillus casei subsp. rhamnosus (ATCC 11443). The PCS disks contained 50% (w/w) polypropylene, 35% (w/w) ground soybean hulls, 5% (w/w) yeast extract, 5% (w/w) soybean flour, and 5% (w/w) bovine albumin. Bioassays were performed by growing L. casei in solvent-saturated media after soaking the PCS disks. Eighteen different solvent and carrier combinations were evaluated. Overall, L. casei biofilm fermentation demonstrated the same lactic acid production in solvent-saturated medium as suspended cells in medium without solvents (control). To evaluate PCS solvent-detoxifying properties, two bioassays were developed. When solvent-saturated medium in consecutive equal volumes (10 mL then 10 mL) was exposed to PCS, both media demonstrated lactic acid fermentation equal to the control. However, when solvent-saturated medium with two consecutive unequal volumes (10 mL then 90 mL) was exposed to PCS, some degree of toxicity was observed. Furthermore, iso-octane, tributylphosphate (TBP), and Span 80 were optimized for recovery as 91%, 5%, and 4% (v/v), respectively, with a 1:1 ratio of 1.2 M Na(2)CO(3) stripping solution. Also, recovery by emulsion liquid extraction in the hollow-fiber contactor was minimal due to low recovery at pH 5.0 and incompatibility of the solvent and hollow-fiber material. These results suggest that PCS biofilm reactors can benefit lactic acid fermentation by eliminating the toxic effect from solvent leakage into the fermentation medium from liquid-liquid extractive integrated fermentations.     

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).     

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.     

羊源丁酸梭菌HDRyYB1发酵工艺的优化

【目的】目前,国内外鲜有关于羊源丁酸梭菌的报道。本课题选用羊源丁酸梭菌HDRy YB1为研究对象,对其发酵工艺进行优化,为该菌株作为饲料添加剂应用于畜牧业生产奠定基础。【方法】采用Plackett-Burman(PB)试验设计法和响应面法分析并优化显著影响HDRy YB1菌株发酵液中芽胞数的培养基成分。【结果】发酵培养基中的面粉浓度、鱼粉浓度和米粉浓度显著影响发酵液中的芽胞数,优化后的发酵培养基组分(质量体积比)为:面粉3.72%、鱼粉0.90%、米粉3.96%、酵母粉0.60%、Na Cl 0.19%、Mg SO4·7H2O 0.19%、KH2PO4 0.01%、Na HCO3 0.01%、Ca CO3 0.48%;培养参数为:37°C,初始p H为7.2-7.4,瓶装量100/250,接种量3%。在此条件下,HDRy YB1菌株发酵完全(18 h)的芽胞数为1.478×108 CFU/m L,是优化前的2.7倍。【结论】HDRy YB1菌株发酵培养基得到了优化,优化后的培养基可用于后期的扩大发酵试验,验证其在实践生产中的应用价值。     

Efficient cellulase production by the filamentous fungus Acremonium cellulolyticus

Cellulase production was investigated in a culture of a strain of Acremonium cellulolyticus. The medium components were optimized for the improvement of cellulase production. The maximum production of cellulolytic enzymes was obtained in a medium containing (grams per liter) 50 Solka Floc, 5 (NH4)2SO4, 24 KH2PO4, 4.7 potassium tartrate hemihydrate, 1.2 MgSO4.7H2O, 1 Tween 80, 4 urea, 0.01 ZnSO4.7H2O, 0.01 MnSO4.6H2O, and 0.01 CuSO4.7H2O, with a pH of 4.0. In the flask culture, 15.5 filter paper units (FPU)/mL of maximum cellulase activity was obtained, 17.42 FPU/mL in a 7-L bioreactor, and 13.08 FPU/mL in a 50-L scale bioreactor for 4-8 d at 30 degrees C. Average production rates were 1.94 FPU/mL.d in flasks, 2.86 FPU/mL.d in the 7-L bioreactor, and 2.56 FPU/mL.d in the 50-L bioreactor. Cellulase production on a small scale was successfully reproduced in the 50-L pilot scale bioreactor. Saccharification activity from A. cellulolyticus was compared with cellulolytic enzymes produced by other strains. The A. cellulolyticus culture broth had a comparable saccharification yield in comparison with those of other Trichoderma enzymes (GC220 or Cellulosin T2) under the same total cellulase activity. Its saccharification yield (percent of released reducing sugar to used dried substrate) was 60%, and its glucose content was 83%.     

假丝酵母E-2产生物表面活性剂摇瓶发酵条件的优化

从扬子石化的废水淤泥中筛选到1株能发酵液体石蜡产脂肽类生物表面活性剂的假丝酵母Candida E-2.通过单因子实验和正交试验,得到了最佳发酵培养基组成(g/L):牛肉膏3.0,蔗糖2.0,酵母膏0.25,KH2PO4 12.5,MgSO4 0.3,NaCl 1.5,CaCl,0.05,尿素0.5 5;液体石蜡10％(体积分数).最佳培养条件:初始pH7.0,接种量0.12g/L,装液量为200mL三角瓶30mL,培养时间为5 d.最终产量提高了2.7倍,达1.582g/L.     

Production of fuel ethanol at high temperature from sugar cane juice by a newly isolated Kluyveromyces marxianus

Kluyveromyces marxianus DMKU 3-1042, isolated by an enrichment technique in a sugar cane juice medium supplemented with 4% (w/v) ethanol at 35 degrees C, produced high concentrations of ethanol at both 40 and 45 degrees C. Ethanol production by this strain in shaking flask cultivation in sugar cane juice media at 37 degrees C was highest in a medium containing 22% total sugars, 0.05% (NH(4))(2)SO(4), 0.05% KH(2)PO(4), and 0.15% MgSO(4).7H(2)O and having a pH of 5.0; the ethanol concentration reached 8.7% (w/v), productivity 1.45 g/l/h and yield 77.5% of theoretical yield. At 40 degrees C, a maximal ethanol concentration of 6.78% (w/v), a productivity of 1.13 and a yield 60.4% of theoretical yield were obtained from the same medium, except that the pH was adjusted to 5.5. In a study on ethanol production in a 5l jar fermenter with an agitation speed of 300 rpm and an aeration rate of 0.2 vvm throughout the fermentation, K. marxianus DMKU 3-1042 yielded a final ethanol concentration of 6.43% (w/v), a productivity of 1.3g/l/h and a yield of 57.1% of theoretical yield.     

Optimization of fermentation medium and conditions for mycelial growth and water-soluble exo-polysaccharides production by Isaria farinosa B05

The optimal fermentation medium and conditions for mycelial growth and water-soluble exo-polysaccharides production by Isaria farinosa B05 were investigated. The medium components and fermentation conditions were optimized according to the one at a time method, while the concentration of medium components was determined by the orthogonal matrix method. The results showed that the optimal fermentation medium was as follows: sucrose 3.5% (w/v), peptone 0.5%, yeast extract 0.2%, K(2)HPO(4) 0.1%, and MgSO(4) 0.05%. The suitable fermentation conditions were as follows: initial pH 7.0, temperature 25 degrees C, medium volume 75 mL/250 mL, inoculum volume 5% (v/v), time 5d. In such optimal nutrition and environmental conditions, the maximal mycelial yield was 2.124 g/100 mL after 4 day's fermentation, while maximal water-soluble exo-polysaccharides production reached 2.144 g/L after 5 day's fermentation.     

休哈塔假丝酵母HDYXHT-01利用木糖生产乙醇的发酵工艺优化

采用Plackett-Burman (PB) 方法和中心组合设计 (Ccentral composit design,CCD) 对休哈塔假丝酵母Candida shehataeHDYXHT-01利用木糖发酵生产乙醇的工艺进行优化。PB试验设计与分析结果表明：硫酸铵、磷酸二氢钾、酵母粉和接种量是影响木糖乙醇发酵的4个关键因素,以乙醇产量为响应目标,采用CCD和响应面分析法 (Response surface methodology,RSM),确定了木糖乙醇发酵的最佳工艺为：硫酸铵1.73 g/L、磷酸二氢钾3.56 g/L、酵母粉2.62 g/L和接种量5.66％,其他发酵条件为：木糖80 g/L,MgSO4·7H2O 0.1 g/L,pH 5.0,培养温度30 ℃,装液量100 mL/250 mL,摇床转速140 r/min,发酵时间48 h,在该条件下发酵液中乙醇产量可以达到26.18 g/L,比未优化前提高了1.15倍。     

Citric acid production using immobilized conidia of Aspergillus niger TMB 2022

Conidia of Aspergillus niger TMB 2022 were immobilized in calcium alginate for the production of citric acid. A 1-mL conidia suspension containing ca. 2.32 x 10(8) conidia were entrapped into sodium alginate solution in order to prepare 3% Ca-alginate (w/v) gel bead. Immobilized conidia were inoculated into productive medium containing 14% sucrose, 0.25% (NH(4))(2)CO(3), 0.25% KH(2)PO(4), and 0.025% MgSO(4).7H(2)O with addition of 0.06 mg/L CuSO(4).5H(2)O, 0.25 mg/L ZnCl(2), 1.3 mg/L FeCl(3).6H(2)O, pH 3.8, and incubated at 35 degrees C for 13 days by surface culture to produce 61.53 g/L anhydrous citric acid. Under the same conditions with a batchwise culture, it was found that immobilized conidia could maintain a longer period for citric acid production (31 days): over 70 g/L anhydrous citric acid from runs No. 2-4, with the maximum yield for anhydrous citric acid reaching 77.02 g/L for run No. 2. In contrast, free conidia maintained a shorter acid-producing phase, ca. 17 days; the maximum yield for anhydrous citric acid was 71.07 g/L for run No. 2 but dropped quickly as the run number increased.     

黑曲霉β-葡萄糖苷酶产酶条件的优化

本研究对AspergillusnigerGlu05生产β-葡萄糖苷酶的培养基组分及培养条件进行了优化。优化后的培养基组成和培养条件分别为：麸皮4％,tryptone4％,1gmolMnSO4,1／zmolNaCl,KH2PO40．2％,pH自然,摇床转速250r／r/min,培养温度30℃,培养周期5d。优化后发酵液中酶活力达到44．11IU／mL,与初始的产酶水平32．87IU／mL相比,提高了36％。     

重组谷氨酸棒杆菌发酵L-苯丙氨酸培养基的优化

【目的】提高重组谷氨酸棒杆菌发酵L-苯丙氨酸(L-phenylalanine,L-Phe)的产量。【方法】使用正交试验设计以及响应面优化法分别对种子培养基及发酵培养基进行优化,确定了重组谷氨酸棒杆菌发酵L-Phe的最佳种子培养基及最佳发酵培养基。【结果】重组谷氨酸棒杆菌发酵L-Phe最佳种子培养基(g/L):葡萄糖25.0,玉米浆25.0,硫酸铵15.0,硫酸镁1.0,磷酸二氢钾2.0,尿素2.0,p H 6.8-7.0;最佳发酵培养基(g/L):葡萄糖110.0,玉米浆7.0,硫酸铵25.0,硫酸镁1.0,磷酸二氢钾1.0,柠檬酸钠2.0,谷氨酸1.0,碳酸钙25.0,p H 6.8-7.0;在最佳培养基条件下L-Phe产量最高达到9.14 g/L,较优化前的7.46 g/L提高了22.5%。【结论】通过正交试验和响应面分析对重组谷氨酸棒杆菌发酵L-Phe培养基进行优化,明显提高了L-Phe的产量,并确定了葡萄糖、玉米浆和硫酸铵为发酵培养基中影响L-Phe产量的3个关键因子。研究结果为L-Phe的发酵放大提供了依据。     

An Improved Bioprocess for Extracellular l-Leucine Amino Peptidase Production Using Streptomyces gedanensis

A bioprocess was developed for the production of L-leucine aminopeptidase under solid-state fermentation (SSF) by cultivating Streptomyces gedanensis in an inert support impregnated with a minimal medium. Response surface methodology of Box Behnken design was used to derive the optimum level of significant factors (3 ml inoculum (1.2 × 10(9) CFU/ml); 0.275% w/v (NH(4))(2)SO(4); 0.275% w/v MgSO(4)·7H(2)O and 0.55% w/v Tryptone) for maximum LAP production (489 IU/g PUF) as compared to the initial level of 176.3 ± 0.02 IU/g PUF. The high level of extracellular aminopeptidase yield achieved in this work showed the technical feasibility of LAP production under SSF using inert support and is the first report of this kind. The ability of Streptomyces amino peptidase to release particular N-terminal amino acids made them interesting for controlling the degree of hydrolysis and flavor development for a wide range of substrates in food like industries.