聚苹果酸的发酵培养条件优化

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。     

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。     

聚苹果酸生产菌出芽短梗霉CCTCC M2012223的全基因组测序及序列分析

【目的】解析出芽短梗霉CCTCC M2012223的基因组序列信息,分析其代谢产物聚苹果酸、黑色素、普鲁兰多糖合成相关基因,为深入研究遗传多样性和代谢工程改造提供序列背景信息。【方法】使用Illumina Hi Seq高通量测序平台对出芽短梗霉CCTCC M2012223菌株进行全基因组测序,并对测序数据进行序列拼接,基因预测与功能注释,COG/GO聚类分析,比较基因组学分析等。下载其他5株出芽短梗霉基因组序列,比较分析6株菌的种内同源基因、全基因组进化以及代谢产物合成相关基因。【结果】出芽短梗霉CCTCC M2012223基因组序列全长30756831 bp,GC含量47.49%,编码9452个基因。比较基因组分析表明出芽短梗霉CCTCC M2012223的基因组组装长度最长,6株菌的同源基因数达到7092个,普鲁兰多糖和聚苹果酸合成相关基因的蛋白序列有很高的保守性。出芽短梗霉CCTCC M2012223和Aureobasidium pullulans var.melanogenum亲缘关系最近,而这2株菌的黑色素合成相关基因的蛋白序列有一些插入和突变。【结论】本研究解析了出芽短梗霉CCTCC M2012223的基因组序列信息,获得黑色素、普鲁兰多糖和聚苹果酸合成相关基因,为后续的代谢机制解析和改造提供相关依据。     

聚苹果酸聚合途径中苹果酰辅酶A连接酶基因的克隆、表达及酶学性质

【目的】研究出芽短梗霉聚苹果酸聚合途径中苹果酰辅酶A连接酶基因及其酶学特性。【方法】通过设计兼并引物,采用IPCR技术从出芽短梗霉CCTCC M2012223的基因组中扩增得到苹果酰辅酶A连接酶基因的cDNA全长序列,构建表达载体,通过大肠杆菌异源表达,Ni-NTA柱层析纯化酶蛋白,分析其酶学特性。【结果】获得苹果酰辅酶A连接酶基因序列全长为1498 bp,编码440 aa,含有4个外显子和3个内含子。该重组酶最适反应温度为25℃,最适反应pH值为8.0,高浓度底物ATP明显对酶活性具有抑制作用,单体选择性表明对底物草酸、草酰乙酸、丁酸、丙二酸也具有很好催化活性。【结论】成功从出芽短梗霉CCTCC M2012223中克隆获得聚苹果酸聚合途径的苹果酰辅酶A连接酶基因,为聚苹果酸聚合途径解析及新型可降解材料创制奠定基础。     

农杆菌介导的出芽短梗霉遗传转化及高效筛选聚苹果酸高产菌株

建立根癌农杆菌介导的出芽短梗霉遗传转化方法及T-DNA突变库,高效筛选聚苹果酸高产菌株及功能基因。通过含潮霉素和草铵磷抗性基因的农杆菌转化出芽短梗霉,抗性压力筛选及PCR验证建立根癌农杆菌介导的出芽短梗霉遗传转化方法,结合发酵液p H与聚苹果酸含量响应变化,微孔板高效筛选高产聚苹果酸的T-DNA插入突变株,基因组步移确定T-DNA插入位点及功能基因。结果获得遗传稳定的抗性基因菌株,每107个细胞可获得80-120个转化子,出芽短梗霉H27号T-DNA突变株聚苹果酸摇瓶发酵产量提高24.5%,基因组步移证实糖酵解途径磷酸甘油酸变位酶基因被破坏。成功建立了根癌农杆菌介导的出芽短梗霉遗传转化方法和T-DNA插入突变库,结合高效筛选方法为聚苹果酸合成功能基因挖掘及高产机制解析奠定基础。     

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。     

解淀粉芽胞杆菌PC2产抑菌物质培养基及发酵条件优化

【目的】优化解淀粉芽胞杆菌PC2产抑菌活性物质发酵培养基及发酵条件。【方法】以马铃薯葡萄糖液体培养基为基础,依据发酵液对金黄色葡萄球菌抑菌圈的单因素试验结果,采用Box-Behnken响应面法优化发酵培养基,二次通用旋转组合设计,频率分析法优化发酵条件。【结果】影响发酵液抑菌活性的培养基主要组分为马铃薯、蔗糖和L-谷氨酸钠,最优发酵培养基配方为:马铃薯188.0 g/L,蔗糖22.0 g/L,L-谷氨酸钠1.80 g/L,培养基成本为0.81元/L;最佳发酵条件为:接种量6%、发酵温度30°C、装液量40 mL/250 mL、摇床转速185 r/min、发酵时间24 h、初始pH 7.0。优化后发酵液对金黄色葡萄球菌抑菌圈直径为30.82 mm,较优化前的18.22 mm增加了12.60 mm。【结论】优化后的培养基和发酵条件提高了解淀粉芽胞杆菌PC2发酵液的抑菌活性,为该菌株的工业化生产应用提供了依据。     

无载体固定化米根霉重复间歇发酵生产L-乳酸

通过研究影响米根霉菌丝体形态的培养基因素,初步构建了无载体固定化米根霉重复间歇发酵生产L-乳酸的工艺条件.研究结果表明,首批次发酵培养基采用120 g/L葡萄糖,3 g/L硝酸铵,K 和Na 浓度比为1:1,发酵72 h后,米根霉菌体形态为均匀的茵丝体小球,直径为1.0 mm～2.0 mm,此时L-乳酸产量可达100.8 g/L,葡萄糖转化率为84%.在此基础上,利用米根霉菌丝体小球重复间歇发酵16批次,每批次发酵24h,此时葡萄糖转化率均高于75%,L-乳酸产量保持在60.0 g/L以上,米根霉菌丝体小球形态保持稳定.     

米根霉两段式利用板栗栗苞生产富马酸

通过自水解预处理板栗栗苞,以预水解液组成增殖培养基培养米根霉,增殖的米根霉再利用栗苞酶解液生产富马酸。结果表明:220℃自水解预处理栗苞,有效疏解栗苞紧密的木质纤维结构,以50 FPIU(以1 g纤维素计)纤维素酶水解50 g/L预处理栗苞,酶解得率大于95%;经增殖培养基培养米根霉,菌体生物量达4.5 g/L;增殖的米根霉利用栗苞酶解液发酵产富马酸,富马酸质量浓度为15.78 g/L,糖酸转化率为0.34 g/g。通过两段式发酵工艺,米根霉有效利用板栗栗苞生产富马酸。     

寄生曲霉CICC40365利用木糖产L-苹果酸的发酵条件优化

【目的】为提高L-苹果酸产量及木糖利用率,以寄生曲霉(Aspergillus parasiticus CICC40365)为菌种,木糖为碳源,对其发酵工艺及木糖代谢途径进行初步研究。【方法】采用单因素试验和响应曲面法(Box-Behnken设计)对培养基和发酵条件进行优化。【结果】获得最佳培养基配方为:木糖100.0 g/L、硫酸铵2.0 g/L、酵母浸粉3.0 g/L、硫酸镁0.20 g/L、硫酸锰0.15 g/L、硫酸亚铁0.08 g/L、碳酸钙80.00 g/L,L-苹果酸的产量为53.58 g/L,较优化前提高40.5%。发酵条件较好组合为:接种量为8%(体积比)、摇瓶装液量60 mL/250 mL、发酵温度32°C、摇床转速170 r/min、发酵周期8 d,L-苹果酸的产量为55.47 g/L。Mg2+、Mn2+对木糖代谢中相关酶的影响研究结果表明,木酮糖激酶在该菌株代谢木糖过程中起着重要作用。【结论】寄生曲霉CICC40365能够较好地利用木糖发酵产L-苹果酸,其产量及木糖的利用效率均得到提高。     

Process optimization of continuous gluconic acid fermentation by isolated yeast-like strains of Aureobasidium pullulans

This study was focused on the optimization of a new fermentation process for continuous gluconic acid production by the isolated yeast-like strain Aureobasidium pullulans DSM 7085 (isolate 70). Operational fermentation parameters were optimized in chemostat cultures, using a defined glucose medium. Different optima were found for growth and gluconic acid production for each set of operation parameters. Highest productivity was recorded at pH values between 6.5 and 7.0 and temperatures between 29 and 31 degrees C. A gluconic acid concentration higher than 230 g/L was continuously produced at residence times of 12 h. A steady state extracellular gluconic acid concentration of 234 g/L was measured at pH 6.5. 122% air saturation yielded the highest volumetric productivity and product concentration. The biomass-specific productivity increased steadily upon raising air saturation. An intracellular gluconic acid concentration of about 159 g/L (0.83 mol) was determined at 31 degrees C. This is to be compared with an extracellular concentration of 223 g/L (1.16 mol), which indicates the possible existence of an active transport system for gluconic acid secretion, or the presence of extracellular glucose oxidizing enzymes. The new process provides significant advantages over the traditional discontinuous fungi operations. The process control becomes easier, thus offering stable product quality and quantity.     

海洋来源链霉菌MY0504产纤溶酶的发酵条件优化

【目的】以发酵液纤溶酶活力为指标,优化海洋来源的链霉菌菌株MY0504的发酵条件。【方法】在菌株生长曲线及单因素试验基础上,采用Plackett-Burman设计筛选影响纤溶酶活性的主要因素,进一步用最陡爬坡试验及Box-Behnken中心组合设计法优化发酵条件。【结果】纤溶酶活性最高的发酵条件为:葡萄糖21.68 g/L,酵母粉25.31 g/L,NaCl5.0 g/L,K_2HPO_4·3H_2O3.0 g/L,MgSO_4·7H_2O 0.5 g/L,FeSO_4·7H_2O 0.02 g/L,装液量50 mL(250 mL摇瓶),接种量10%(体积比),初始pH 7.5,温度24°C,转速200 r/min,培养时间4.5 d。发酵液纤溶酶活性可达2 190.6 U/mL。【结论】确定了MY0504菌株产纤溶酶的最优发酵条件,为该酶的进一步分离纯化及性质研究奠定基础。     

Production of polymalic acid and malic acid by Aureobasidium pullulans fermentation and acid hydrolysis

Malic acid is a dicarboxylic acid widely used in the food industry and also a potential C4 platform chemical that can be produced from biomass. However, microbial fermentation for direct malic acid production is limited by low product yield, titer, and productivity due to end‐product inhibition. In this work, a novel process for malic acid production from polymalic acid (PMA) fermentation followed by acid hydrolysis was developed. First, a PMA‐producing Aureobasidium pullulans strain ZX‐10 was screened and isolated. This microbe produced PMA as the major fermentation product at a high‐titer equivalent to 87.6 g/L of malic acid and high‐productivity of 0.61 g/L h in free‐cell fermentation in a stirred‐tank bioreactor. Fed‐batch fermentations with cells immobilized in a fibrous‐bed bioreactor (FBB) achieved the highest product titer of 144.2 g/L and productivity of 0.74 g/L h. The fermentation produced PMA was purified by adsorption with IRA‐900 anion‐exchange resins, achieving a ～100% purity and a high recovery rate of 84%. Pure malic acid was then produced from PMA by hydrolysis with 2 M sulfuric acid at 85°C, which followed the first‐order reaction kinetics. This process provides an efficient and economical way for PMA and malic acid production, and is promising for industrial application. Biotechnol. Bioeng. 2013; 110: 2105–2113. © 2013 Wiley Periodicals, Inc.     

Utilization of by-products derived from bioethanol production process for cost-effective production of lactic acid

The by-products of bioethanol production such as thin stillage (TS) and condensed distillers solubles (CDS) were used as a potential nitrogen source for economical production of lactic acid. The effect of those by-products and their concentrations on lactic acid fermentation were investigated using Lactobacillus paracasei CHB2121. Approximately, 6.7 g/L of yeast extract at a carbon source to nitrogen source ratio of 15 was required to produce 90 g/L of lactic acid in the medium containing 100 g/L of glucose. Batch fermentation of TS medium resulted in 90 g/L of lactic acid after 48 h, and the medium containing 10 % CDS resulted in 95 g/L of lactic acid after 44 h. Therefore, TS and CDS could be considered as potential alternative fermentation medium for the economical production of lactic acid. Furthermore, lactic acid fermentation was performed using only cassava and CDS for commercial production of lactic acid. The volumetric productivity of lactic acid [2.94 g/(L·h)] was 37 % higher than the productivity obtained from the medium with glucose and CDS.     

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。     

4-氯乙酰乙酸乙酯羰基还原酶产生菌的筛选及产酶条件研究

从实验室保藏的菌株中,筛选到一株立体选择性较高的产4-氯乙酰乙酸乙酯(COBE)羰基还原酶的菌株———出芽短梗霉(Aureobasidiumpullulans)SW0202,菌体产酶条件研究表明,最佳的发酵培养基配方为:麦芽糖30.0g/L,酵母膏20.0g/L,蛋白胨3.0g/L,(NH4)2SO45.0g/L,KH2PO42.0g/L,MgSO4.7H2O0.7g/L,最适发酵温度及初始pH分别为:28°C和pH6.0。该菌在此条件下发酵培养24h,产菌丝体生物量16.78g干菌体/L,COBE羰基还原酶酶活力达到1007U/L。在COBE的转化反应中,产物S-CHBE的浓度达到10.12g/L,光学纯度>97%e.e.。     

产D-阿拉伯醇菌株的筛选、鉴定及其产D-阿拉伯醇条件的优化

摘要：【目的】产D-阿拉伯醇的耐高渗酵母的筛选、鉴定和产D-阿拉伯醇条件的优化。【方法】通过电镜、Biolog GN、(G+C)含量和26S rDNA D1/D2区序列分析法对所获得的菌株进行了描述。通过红外光谱、核磁共振氢谱和碳谱、质谱以及旋光度实验鉴定纯化产物的结构。通过单因素实验优化产D-阿拉伯醇的发酵条件。【结果】本文筛选得到一株产D-阿拉伯醇的新型菌株,经鉴定属于假丝酵母属并命名为Candida sp. H2。200 mL摇瓶发酵生产D-阿拉伯醇的单因素优化实验表明,最适发酵条件为：葡萄糖250