响应面法优化普鲁兰多糖发酵培养基

以出芽短梗霉IFO 4464为实验菌种,采用响应面法(RSM)优化了出芽短梗霉IFO 4464产普鲁兰多糖的发酵培养基。通过实验得到出芽短梗霉最佳发酵培养基为蔗糖59.8g/L,硫酸铵0.7 g/L,硫酸镁0.3 g/L,磷酸二氢钾5.0g/L,氯化钾0.5g/L,氯化钠1.5g/L,酵母浸膏2.5 g/L,多糖产量可达21.92 g/L。     

出芽短梗霉新菌株RM1603产普鲁兰多糖条件优化及多糖分析

目的:出芽短梗霉RM1603是一株高产胞外多糖新菌株,通过优化其产糖条件,鉴定其多糖结构,为进一步开发利用RM1603产胞外多糖奠定理论基础。方法:以RM1603为出发菌株,在单因素分析确定最佳氮源与无机盐的基础上,利用正交试验探究RM1603最佳发酵产糖条件;薄层层析及红外光谱分析确定胞外多糖产物结构。结果:出芽短梗霉菌RM1603的初始多糖产量为28.91g/L,发酵条件优化后产糖量达到65.213g/L,提高了约2.3倍;结构分析表明RM1603的多糖产物为普鲁兰多糖。结论:出芽短梗霉RM1603是一株具有较大产糖优势,极具开发潜力的高产普鲁兰糖新菌株;奠定了开发利用RM1603生产普鲁兰多糖的理论基础。     

出芽短梗霉发酵过程溶氧控制的研究

在搅拌罐式生物反应器中,通过控制DO（溶氧浓度）的变化,对出芽短梗霉（Aureobasidium pullulans）发酵过程的控制进行了研究。以100g/L玉米粉水解液做碳源,比较了不同溶氧控制条件下发酵参数的变化及其对出芽短梗霉发酵结果的影响。结果表明,过低的DO对菌体生长和多糖生产都不利,过高的DO使培养液中糖大部分消耗在菌体的生长上,也不利于多糖的生产,通过控制搅拌速度和通气量能将DO维持在较合适的水平。     

表面活性剂对绿色木霉产纤维素酶影响

利用绿色木霉,以稻草为唯一碳源,采用液态发酵的方法,分别加入生物表面活性剂鼠李糖脂和化学表面活性剂Tween 80,重点研究了生物表面活性剂对绿色木霉产纤维素酶的影响。实验分析了加入不同浓度的表面活性剂时滤纸酶活、羧甲基纤维素酶活、微晶纤维素酶活及酶液的表面张力随时间的变化情况。结果表明,添加鼠李糖脂能够促进绿色木霉产酶,分别使滤纸酶活、羧甲基纤维素酶活、微晶纤维素酶活最大提高了1.08倍,1.6倍和1.03倍。与Tween 80相比,鼠李糖脂促进产酶的效果明显优于Tween 80。     

出芽短梗霉A5产胞外多糖发酵条件的优化及产物结构鉴定

基于筛选获得能够生产分子量较高且无色素的普鲁兰多糖酵母菌株,对其进行菌株鉴定、产多糖发酵条件优化和多糖产物鉴定,旨在为工业上普鲁兰多糖发酵提供新的菌株来源。以YPD固体培养基为筛选培养基,氯霉素为筛选压力,曲利苯蓝为筛选指示剂;通过形态学,ITS间隔序列分析对筛选出的A5菌株进行鉴定。采用单因子优化A5菌株的最佳发酵条件;利用普鲁兰酶酶解并结合薄层层析法、红外光谱以及凝胶渗透色谱进行结构鉴定和分子量的测定。A5菌株鉴定为出芽短梗霉属,并被命名为出芽短梗霉A5。最优的发酵条件8%(w/v)麦芽糖,1%(w/v)酵母粉,2%(w/v)蛋白胨,0.5%(w/v)K_2HPO_4,0.06%(w/v)(NH_4)_2SO_4,0.03%(w/v)CaCl_2,pH6,7%(v/v)接种量;经过结构鉴定得知:该菌株的胞外产物是普鲁兰多糖,分子量为63.84 kDa。由此获得了一株生产普鲁兰多糖的出芽短梗霉菌株A5,产物无色素且分子量较高。经过初步的发酵条件优化,在最佳发酵条件下发酵培养后,获得普鲁兰多糖的产量为22.9 g/L。综合上述结果可知,菌株A5能够作为工业上生产普鲁兰多糖的重要候选菌株。     

几株出芽短梗霉在不同发酵条件下产生多糖的比较

将已有的４株出芽短梗霉在摇瓶中于不同发酵条件下进行比较,考察了它们的生长情况,不同的碳源、氮源、磷酸盐、初始ｐＨ和通气量等对短梗霉多糖合成的影响,获得一株产短梗霉多糖的高产菌株,为以后工作打下良好基础。     

出芽短梗霉产聚苹果酸发酵条件的优化

【背景】出芽短梗霉可发酵葡萄糖生成聚苹果酸,但存在转化率和转化效率低等瓶颈,阻碍其实现商业化生产。【目的】通过优化发酵培养条件,提高出芽短梗霉的聚苹果酸产量、糖酸转化率和生产强度。【方法】采用单因素试验优化适宜出芽短梗霉BK-10菌株产生聚苹果酸的培养条件,通过Plackett-Burman法对培养基组分筛选显著性影响因素,并对其培养基中无机盐进行正交试验优化,最后进行5 L发酵罐验证。【结果】最优培养基配方和培养条件:100 g/L葡萄糖,1.5 g/L尿素,0.20 g/L KH_2PO_4,0.20 g/L ZnSO_4,0.05 g/L MgSO_4,0.75 g/L KCl,30 g/L CaCO_3,0.01%吐温-80,发酵温度26°C,250 mL摇瓶装液量50 mL。【结论】通过优化,聚苹果酸的糖酸转化率达到0.71 g/g,生产强度达到0.89 g/(L·h),较优化前分别提高了18.33%和71.15%,为发酵葡萄糖合成聚苹果酸进而生产L-苹果酸工艺的工业化生产奠定经济性基础。     

卜多糖发酵条件试验

卜多糖(Pullulan)也称短梗霉多糖。我们从11株产卜多糖的出芽短梗霉中选出3.2756号菌株,经亚硝基胍处理,得到变异株N28,并对其产卜多糖的发酵条件进行试验,现报道如下。     

二价阳离子对短梗霉多糖发酵的影响

就二价阳离子对短梗霉多糖和黑色素的影响进行了分析和研究。结果表明 ,二价阳离子对短梗霉多糖的合成和黑色素的形成均有较大的影响。通过对培养基中二价阳离子含量和种类的控制不仅可以抑制细胞黑色素的形成 ,而且还保持了很高的多糖发酵水平 ,在 30L生物反应器中短梗霉多糖的产量和转化率分别达到了 59 8g/L和 61 5%。     

出芽短梗霉Aureobasidium sp. SRF的菌株特性分析及胞外多糖结构鉴定

菌株SRF是1株从意大利树莓(Rubus corchorifolius)果实表面分离、可产胞外多糖的新菌株。在鉴定其分类归属的基础上,对其产生的胞外多糖进行了结构分析和发酵条件优化,为寻找微生物多糖提供新的菌株,为开发利用资源微生物提供借鉴。通过形态学和ITS序列对比分析进行菌株鉴定;通过薄层层析和红外光谱分析,确定胞外多糖结构;通过单因素检测试验,确定影响产糖量的主要因素;响应面Plackett-Burman和Box-Behnken设计筛选发酵产胞外多糖的最优条件。结果表明,出发菌株SRF隶属于出芽短梗霉属,命名为Aureobasidium sp. SRF;SRF所产胞外多糖为普鲁兰多糖;单因素检测表明,对多糖产量影响最大的因素为碳源浓度、氮源浓度、无机离子浓度,其次是碳源、氮源、无机离子、pH值;根据响应面结果确定最优发酵条件为麦芽糖8%(质量分数)、酵母提取物3%(质量分数)、钙离子0.3 g/L、pH 6,产糖量达5.93 g/L。SRF是1株来源于树莓浆果表面,可产胞外普鲁兰多糖的出芽短梗霉新菌株,是1株产微生物多糖的候选菌株。     

Tween 80 enhanced TNT mineralization by Phanerochaete chrysosporium

The effect of a nonionic surfactant (Tween 80) on 2,4,6-trinitrotoluene (TNT) mineralization by the white-rot fungus Phanerochaete chrysosporium strain BKM-F-1767, was investigated in a liquid culture at 20, 50, and 100 mg TNT.L-1. The presence of 1% (w/v) Tween 80, at 20 mg.L-1 TNT, added to a 4-d-old culture, allowed the highest TNT mineralization level, that is 29.3% after 24 d, which is two times more than the control culture, without Tween 80 (13.9%). The mineralization of TNT resumed upon additional Tween 80 supplementation, consequently, 39.0% of the TNT was respired on day 68. Orbital agitation of the fungal culture was found detrimental to TNT mineralization, with or without Tween 80 in the culture medium. The surfactant also stimulated the growth of P. chrysosporium without any notable effect on either the glycerol consumption rate or the extracellular LiP and MnP activity levels. Respirometric assays highlighted some differences between the oxygen uptake rate of the fungal culture supplemented with or without Tween 80.     

Toxicity of phenanthrene dissolved in nonionic surfactant solutions to Pseudomonas putida P2

The fraction in which direct contact occurs between micellar-phase phenanthrene and the bacterial cell surface was estimated by measuring the toxicity of nonionic surfactant (Tween 80 and Triton X-100) solutions to the phenanthrene-degrading bacterium, Pseudomonas putida P2. Cell viability of completely dissolved phenanthrene decreased by 30% at concentrations greater than 0.3 mg L(-1), which is equal to approximately one third of its solubility. Both nonionic surfactants had no effect on cell viability up to 5 g L(-1). Cell viability increased with increasing surfactant concentration at a fixed phenanthrene concentration, due to the decreased concentration of aqueous-pseudophase phenanthrene and the reduced fraction of direct contact. The fraction of direct contact was c. 20% or more below 3 g L(-1) of Triton X-100. The fraction of direct contact for Tween 80 was estimated to be lower than Triton X-100.     

The stimulatory effects of surfactants on composting of waste rich in cellulose

The chemical surfactant Tween 80 and biosurfactant rhamnolipid were respectively added to the composting substrate, a mixture of rice straw and bran, and their effects on the composting process were investigated. Samples were analysed for microbial communities of bacteria, actinomycetes and fungi, carboxymethylcellulose hydrolysis (CMCase) and xylanase activities, cellulose and hemicellulose fractions, water-soluble carbon (WSC) contents in the substrates, organic matter contents and pH values during the composting process. The results showed that both Tween 80 and rhamnolipid had slight stimulatory effects on the microbial populations of bacteria, actinomycetes and fungi. In addition, rhamnolipid increased the peak xylanase activity 15% higher than that of the control, while Tween 80 increased the maximum CMCase activity 35% higher than that of the control. As a result of the increased enzyme activities, treatments with Tween 80 and rhamnolipid were of higher WSC contents than the control during the whole composting process. Accordingly, the composting process was accelerated by the surfactants, since the organic matter was decomposed more quickly and the breakdown of cellulose and hemicellulose was better in the treatments with Tween 80 and rhamnolipid.     

Benefits from tween during enzymic hydrolysis of corn stover

Corn stover is a potential substrate for fermentation processes. Previous work with corn stover demonstrated that lime pretreatment rendered it digestible by cellulase; however, high sugar yields required very high enzyme loadings. Because cellulase is a significant cost in biomass conversion processes, the present study focused on improving the enzyme efficiency using Tween 20 and Tween 80; Tween 20 is slightly more effective than Tween 80. The recommended pretreatment conditions for the biomass remained unchanged regardless of whether Tween was added during the hydrolysis. The recommended Tween loading was 0.15 g Tween/g dry biomass. (The critical relationship was the Tween loading on the biomass, not the Tween concentration in solution.) The 72-h enzymic conversion of pretreated corn stover using 5 FPU cellulase/g dry biomass at 50 degrees C with Tween 20 as part of the medium was 0.85 g/g for cellulose, 0.66 g/g for xylan, and 0.75 for total polysaccharide; addition of Tween improved the cellulose, xylan, and total polysaccharide conversions by 42, 40, and 42%, respectively. Kinetic analyses showed that Tween improved the enzymic absorption constants, which increased the effective hydrolysis rate compared to hydrolysis without Tween. Furthermore, Tween prevented thermal deactivation of the enzymes, which allows for the kinetic advantage of higher temperature hydrolysis. Ultimate digestion studies showed higher conversions for samples containing Tween, indicating a substrate effect. It appears that Tween improves corn stover hydrolysis through three effects: enzyme stabilizer, lignocellulose disrupter, and enzyme effector. Copyright 1998 John Wiley & Sons, Inc.     

Enzymatic production of glycerol carbonate from by-product after biodiesel manufacturing process

Glycerol carbonate is one of the higher value-added products derived from glycerol. In this study, glycerol carbonate (GC) was synthesized by transesterification of glycerol and dimethyl carbonate (DMC) using Novozym 435 (Candida antarctica Lipase B) at various conditions. For the enzymatic production of GC, the optimum conditions were the amount of enzyme (75 g/L), DMC/glycerol molar ratio (2.00), reaction temperature (60°C) and organic solvent (acetonitrile). Experimental investigation of the effect of water content revealed that the conversion of GC was maximized with no added water. The addition of surfactant such as Tween 80 increased the GC conversion, which finally reached 96.25% under the optimum condition and with surfactant addition.     

Enhanced lycopene production in Escherichia coli engineered to synthesize isopentenyl diphosphate and dimethylallyl diphosphate from mevalonate

To increase expression of lycopene synthetic genes crtE, crtB, crtI, and ipiHP1, the four exogenous genes were cloned into a high copy pTrc99A vector with a strong trc promoter. Recombinant Escherichia coli harboring pT-LYCm4 produced 17 mg/L of lycopene. The mevalonate lower pathway, composed of mvaK1, mvaK2, mvaD, and idi, was engineered to produce pSSN12Didi for an efficient supply of the lycopene building blocks, isopentenyl diphosphate (IPP) and dimethylallyl diphosphate (DMAPP). Mevalonate was supplied as a substrate for the mevalonate lower pathway. Lycopene production in E. coli harboring pT-LYCm4 and pSSN12Didi with supplementation of 3.3 mM mevalonate was more than threefold greater than bacteria with pT-LYCm4 only. Lycopene production was dependent on mevalonate concentration supplied in the culture. Clump formation was observed as cells accumulated more lycopene. Further clumping was prevented by adding the surfactant Tween 80 0.5% (w/v), which also increased lycopene production and cell growth. When recombinant E. coli harboring pT-LYCm4 and pSSN12Didi was cultivated in 2YT medium containing 2% (w/v) glycerol as a carbon source, 6.6 mM mevalonate for the mevalonate lower pathway, and 0.5% (w/v) Tween 80 to prevent clump formation, lycopene production was 102 mg/L and 22 mg/g dry cell weight, and cell growth had an OD(600) value of 15 for 72 h.     

Surfactant-enhanced anaerobic acidogenesis of Canna indica L. by rumen cultures

Polyoxyethylene sorbitan monoolate (Tween 80) was used to enhance the anaerobic acidogenesis of Canna indica L. (canna) by rumen culture in this study. Dose of Tween 80 at 1 ml/l enhanced the volatile fatty acids (VFA) production from the acidogenesis of canna compared to the control. However, Tween 80 at higher dosages than 5 ml/l inhibited the rumen microbial activity and reduced the VFA yield. Response surface methodology was successfully used to optimize the VFA yield. A maximum of VFA yield of 0.147 g/g total solids (TS) added was obtained at canna and Tween 80 concentrations of 6.3g TS/l and 2.0 ml/l, respectively. Dosage of Tween 80 at 1-3.75 ml/l reduced the unproductive adsorption of microbes or enzymes on the lignin part in canna and increased microbial activity. A high VFA production was achieved from canna presoaked with Tween 80, suggesting that the structure of canna was disrupted by Tween 80.     

Effect of surfactants on ethanol fermentation using glucose and cellulosic hydrolyzates

The effect of the non-ionic surfactants on the ethanol fermentation was greatly dependent on the surfactant added. While Tween 20 and Tween 80 slightly enhanced ethanol fermentation, Triton X-100 which exhibited the inghest increase in the enzymatic saccharification had a negative effect on the ethanol fermentation. The negative effect of Triton X-100 on ethanol production was the most pronounced when the cellulosic hydrolyzates were used. Tween 80 showed the best performance for the ethanol production from steam exploded wood hydrolyzate.     

Ascorbic acid stimulation of production of a highly branched ,beta-1,3-glucan by Aureobasidium pullulans K-1--oxalic acid, a metabolite of ascorbic acid as the stimulating substance

The production of a highly branched beta-1,3-glucan by Aureobasidium pullulans K-1 in Czapek's medium has been found to be stimulated by ascorbic acid. When the culture supernatant, after removal of polysaccharide from the culture filtrate by ethanol precipitation, was concentrated, then added to a new medium and this strain was cultured in the medium, the polysaccharide production was stimulated the same as when L-ascorbic acid was added to the medium. The stimulating substance was partially purified from the supernatant, and was found to be oxalic acid; 0.03% oxalic acid was the most effective concentration for the stimulation of polysaccharide production. The stimulating substance, oxalic acid, was proved to be derived from ascorbic acid added to a medium in an experiment using L-[1-14C]ascorbic acid. We suggest that oxalic acid generated from the metabolism of ascorbic acid in cells of Aureobasidium pullulans K-1 participated in the stimulation of the polysaccharide production by ascorbic acid.     

Parameters affecting spore recovery from wipes used in biological surface sampling

The need for the precise and reliable collection of potential biothreat contaminants has motivated research in developing a better understanding of the variability in biological surface sampling methods. In this context, the objective of this work was to determine parameters affecting the efficiency of extracting Bacillus anthracis Sterne spores from commonly used wipe sampling materials and to describe performance using the interfacial energy concept. In addition, surface thermodynamics was applied to understand and predict surface sampling performance. Wipe materials were directly inoculated with known concentrations of B. anthracis spores and placed into extraction solutions, followed by sonication or vortexing. Experimental factors investigated included wipe material (polyester, cotton, and polyester-rayon), extraction solution (sterile deionized water [H(2)O], deionized water with 0.04% Tween 80 [H(2)O-T], phosphate-buffered saline [PBS], and PBS with 0.04% Tween 80 [PBST]), and physical dissociation method (vortexing or sonication). The most efficient extraction from wipes was observed for solutions containing the nonionic surfactant Tween 80. The increase in extraction efficiency due to surfactant addition was attributed to an attractive interfacial energy between Tween 80 and the centrifuge tube wall, which prevented spore adhesion. Extraction solution significantly impacted the extraction efficiency, as determined by statistical analysis (P < 0.05). Moreover, the extraction solution was the most important factor in extraction performance, followed by the wipe material. Polyester-rayon was the most efficient wipe material for releasing spores into solution by rank; however, no statistically significant difference between polyester-rayon and cotton was observed (P > 0.05). Vortexing provided higher spore recovery in H(2)O and H(2)O-T than sonication, when all three wipe materials and the reference control were considered (P < 0.05).