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1.
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。  相似文献   

2.
【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。  相似文献   

3.
聚苹果酸的发酵培养条件优化   总被引:3,自引:0,他引:3  
对出芽短梗霉(Aureobasidium pullulans)BS02发酵制备生物降解材料聚苹果酸的摇瓶发酵条件进行研究,确定了出芽短梗霉发酵制备聚苹果酸的摇瓶培养条件。由实验结果可知:优化的培养基(g/L)为葡萄糖120.0、丁二酸铵3.0、丁二酸2.0、MnSO4.H2O 0.005、MgSO4.7H2O 0.1,另外每升发酵液加玉米浆0.5 mL,CaCO350 g/L,培养条件为pH4.0~4.5、24℃、500 mL摇瓶装发酵液100 mL、摇床转速220 r/min,在最优条件下,聚苹果酸产量可达到30 g/L。  相似文献   

4.
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。  相似文献   

5.
二价阳离子对短梗霉多糖发酵的影响   总被引:3,自引:0,他引:3  
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%。  相似文献   

6.
表面活性剂对出芽短梗霉多糖生产影响的研究   总被引:4,自引:0,他引:4  
研究了表面活性剂对出芽短梗霉细胞培养过程中多糖释放的影响。在摇瓶中,比较添加0.05%(w/v)的Tween 80、Tween 60、Tween 40,结果显示几种表面活性剂均能促进细胞释放多糖,其中以Tween 80的效果最佳。在5L发酵罐中,以100g/L玉米粉水解液做碳源的出芽短梗霉细胞培养液中分别添加了表面活性剂Tween 80 0.01%、0.05%、0.1%,其中以添加Tween 800.05%时的效果最好,与不添加表面活性剂相比多糖产量提高25%左右,发酵周期缩短了将近2d。  相似文献   

7.
采用溴乙锭对出芽短梗霉(Aureobasidium pullulans)进行诱变,得到一株不产色素的变异菌种BM2-5,液体发酵细胞全部呈酵母态,在以大米酶解葡萄糖为碳源的液体培养基中于27℃200 r/min摇瓶培养72 h得到白色的普鲁兰粗多糖,最高产量达68.06 g/L。  相似文献   

8.
出芽短梗霉色素变异菌株R45的普鲁蓝糖发酵研究   总被引:1,自引:0,他引:1  
用正交实验确定了出芽短梗霉(Aureobasidiumpullulans)色素变异菌株R45的发酵优化条件。在此条件下,摇瓶培养的普鲁蓝糖产量最高可达82.4g/L,转化率为54.9%。实验表明,CaCO3是多糖发酵的重要影响因素,多糖的合成与发酵pH值及细胞形态密切相关。  相似文献   

9.
发酵条件对短梗霉多糖产量的影响   总被引:4,自引:0,他引:4  
对短梗霉发酵培养基的初始pH,初始蔗糖浓度,酵母膏浓度,NH4^ 浓度,接种量和装液量等发酵条件对短梗霉多糖发酵影响进行了研究。结果表明,发酵条件对多糖发酵有显著的影响,当初始pH,初始蔗糖浓度,NH4^ 浓度,酵母膏浓度和装液量分别为6.5,5.0%,0.5g/L,0.2%和25ml时多糖的产量达到最大值;但接种量在2.0%-7.0%之间对多糖的产量影响不大,可见,通过对培养条件的调整,有助于短梗霉多糖的产量的提高。  相似文献   

10.
出芽短梗霉发酵过程溶氧控制的研究   总被引:3,自引:1,他引:2  
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。  相似文献   

11.
Pullulan with different molecular-weight could be applied in various fields. A UV-induced mutagenesis Aureobasidium pullulans UVMU6-1 was obtained from the strain A. pullulans CGMCC3.933 for the production of low-molecular-weight pullulan. First, the obtained polysaccharide from A. pullulans UVMU6-1 was purified and identified to be pullulan with thin-layer chromatography, Fourier transform infrared, and nuclear magnetic resonance. Then, culture medium and conditions for this strain were optimized by flask fermentation. Based on the optimized medium and culture conditions (pH 4, addition of 4?g/L Tween 80 for 96?hr of cultivation), continuously fermentation was performed. The highest pullulan production and dry biomass was 109 and 125?g/L after fermentation for 114?hr, respectively. The average productivity was about 1?g/L/hr, which was intensively higher than the previous reported. This study would lay foundations for the industrial production of pullulan.  相似文献   

12.
Based on intuitive analyses and statistical calculations using data from orthogonal array experiments, the optimal concentrations of K2HPO4, NaCl, MgSO4·7H2O, and (NH4)2SO4 in cell growth medium of Aureobasidium pullulans HP-2001 were measured as 7.5, 1.0, 0.1, and 2.4 g/L, respectively, whereas those for the production of pullulan were 2.5, 0.25, 0.8, and 0.3 g/L, respectively. The most important factor for cell growth and production of pullulan by A. pullulans HP-2001 was identified as K2HPO4. Optimal concentrations of glucose and yeast extract, along with the initial pH of the cell growth medium of A. pullulans HP-2001 containing optimized salt concentrations, were found to be 100.0, 10.0, and 6.0 g/L, respectively, whereas those for the production of pullulan were 100.0, 2.5, and 6.0 g/L, respectively. Conversion rates of pullulan from 10.0, 25.0, 50.0, 75.0, and 100.0 g/L of glucose in the presence of optimized salt concentrations were 26.0, 25.2, 22.4, 17.9, and 14.1%, respectively, whereas those in the presence of previously reported salt concentrations were 26.6, 25.2, 19.9, 14.3, and 11.7%, respectively. Optimal salt concentrations for the production of pullulan by A. pullulans HP-2001 varied according to the concentrations of the carbon and nitrogen sources, especially at higher concentrations.  相似文献   

13.
Abstract

Pullulan is an extracellular water-soluble polysaccharide with wide applications. In this study, we screened strains that could selectively produce high molecular weight pullulan for application in industrial pullulan production. A new fungus strain A4 was isolated from soil and identified as Aureobasidium melanogenum based on colony characteristics, morphology, and internally transcribed spacer analysis. Thin-layer chromatography, Fourier-transform infrared spectroscopy, and nuclear magnetic resonance analysis suggested that the dominant exopolysaccharide produced by this strain, which presented a molecular weight of 1.384?×?106 Dalton in in-gel permeation chromatography, was pullulan. The culture conditions for A. melanogenum A4 were optimized at 30?°C and 180?rpm: carbon source, 50?g/L maltose; initial pH 7; and 8?g/L Tween 80. Subsequently, batch fermentation was performed under the optimized conditions in a 5-L stirred-tank fermentor with a working volume of 3?L. The fermentation broth contained 303?g/L maltose, which produced 122.34?g/L pullulan with an average productivity of 1.0195?g/L/h and 82.32?g/L dry biomass within 120?h. The conversion efficiency of maltose to pullulan (Y%) and specific production rate (g/h/g dry cells) (Qs) reached 40.3% and 0.0251?g/L/g dry cells, respectively. The results showed strain A4 could be a good candidate for industrial production.  相似文献   

14.
手性拆分环氧氯丙烷菌株的筛选、鉴定及产酶条件研究   总被引:2,自引:0,他引:2  
从土壤中筛选到5株环氧化物水解酶生产菌,并通过ITS序列鉴定了其中的C375菌,结果为黑曲霉(Aspergillus nigerZJB-09103)。考察了培养基不同碳源、氮源、金属离子和pH等对产酶的影响,得到了较佳的培养基条件:淀粉16g/L,豆饼粉3g/L,蛋白胨3g/L,KH2PO4 0.4g/L,K2HPO4 0.8g/L,MgSO4 0.2g/L,ZnSO4 0.03g/L,pH6.5。采用优化后的培养基条件,酶活力达到156.1U/L,比优化前初始发酵培养条件下的酶活提高了252%,当环氧化物水解酶催化时间为10h时,(s)-环氧氯丙烷的对映体过量值(e.e.)可达99.0%。产率为18.6%。  相似文献   

15.
采用单因素优化法对环糊精葡萄糖苷转移酶(CGTase)合成糖基抗坏血酸(AA-2G)条件进行优化,AA-2G的产量为2.76 g/L,比未优化前0.46g/L提高了500%。再采用响应面法对AA-2G合成条件进行优化。由Plackett-Burman法筛选出三个主要因素为:pH、V_C和麦芽糊精浓度;由最陡爬坡实验得出最佳响应面区域;最后由Box-Behnken实验,得到最优条件为:pH 5.51,V_C36.16g/L,麦芽糊精28.54 g/L,转化时间24 h,温度37℃。在此条件下,AA-2G的理论产量为3.15 g/L,通过验证实验,得出AA-2G的产量为3.13 g/L,与预测的理论值接近,比单因素优化的结果(2.76g/L)提高了14%。  相似文献   

16.
黑曲霉固态发酵生产单宁酶的条件优化   总被引:1,自引:0,他引:1  
研究采用响应面法优化黑曲霉固态发酵生产单宁酶的培养条件。应用Plackett—Burman试验筛选出重要影响因子:五倍子粉含量、(NH4)2SO4浓度以及接种孢子量,最陡爬坡试验逼近最大响应区域。应用Box.Behnken响应面试验对重要影响因子进一步优化。得到最佳培养条件:每250mL三角瓶中装入1.0g五倍子粉、4.4g稻壳和0.5g麸皮、液固比(mL/g)2:1且营养盐溶液组成为(NH4)2s0421g/L、MgSO4·7H2O1g/L、NaCl1g/L,培养基pH自然,接种5.7×10^7个孢子后在30℃温度下培养4d。在此条件下,单宁酶产量从40U/g提高到114U/g,3次重复验证性试验平均值为115U/g,验证了模型的可靠性。  相似文献   

17.
为了使脯氨酸-4-羟化酶基因在重组大肠杆菌中得到高表达,通过调整大肠杆菌密码子偏好性以及mRNA二级结构,使得脯氨酸-4-羟化酶基因得到优化。将优化后的脯氨酸-4-羟化酶基因插入含有色氨酸串联启动子的p UC19质粒,构建重组质粒p UC19-ptrp2-Hyp,并导入大肠杆菌BL21(DE3)中。在摇瓶水平,重组菌以L-脯氨酸为底物发酵8 h,可积累(0.492±0.034)g/L的反式-4-羟脯氨酸。在发酵罐水平,通过补料分批发酵来提高反式-4-羟脯氨酸的产量,当补糖速率为18 g/h时,反式-4-羟脯氨酸的产量高达42.5 g/L,反式-4-羟脯氨酸产率为0.966 g/(L·h)。  相似文献   

18.
利用基于统计学的方法对不透明红球菌(Rhodococcus opacus)DSM 43250转化合成α-酮异己酸(KIC)的培养环境进行优化。采用Plackett-Burman(PB)设计筛选获得对KIC产量具有显著影响的关键营养因子:(NH4)2SO4、麦芽膏和NaNO3。通过最陡爬坡实验、Box-Behnken实验设计和SAS软件回归分析建立了KIC产量关于3个关键营养因子的二次多项式模型,并以模型求解确定最佳培养条件(g/L):(NH4)2SO4 0.23,麦芽膏2.42,NaNO3 1.43。在此培养条件下,KIC的理论最高产量为23.98 mg/L,在验证实验中KIC最高产量为23.93 mg/L,比优化前(3.72 mg/L)提高了6.43倍。  相似文献   

19.
本文对类球红细菌3757产SOD进行了发酵条件优化,结果得到了较优的培养基组成(g/L):苹果酸3,胰蛋白胨4,磷酸氢二钾0.9,磷酸二氢钾O.6,硫酸镁0.2,无水氯化钙0.075,硫酸亚铁0.012,EDATA 0.02,微量元素溶液10 mL,生长因子溶液10 mL,pH 7.5。其中,微量元素溶液配方(g/L):硼酸2.8,硫酸锰1.6,钼酸钠0.76,硫酸锌0.24,硫酸铜0.04;生长因子溶液配方(g/L):维生素B_1 1,烟酰胺(VPP)1,生物素0.016,对氨基苯甲酸1。较优培养条件为:接种量5%,转速150 r/min,种龄24 h,发酵温度32℃,发酵时间24 h。优化后酶活力较优化前提高了88.0%。  相似文献   

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