假单胞菌胞外多糖发酵条件的研究

研究了假单胞菌（Ｐｓｅｕｄｏｍｏｎａｓｓｐ．６）利用木糖产胞外多糖的发酵条件。实验表明ＫＨ２ＰＯ４,Ｏ２和高碳氮比对多糖合成有促进作用,在发酵后期补加木糖有助于多糖产量的提高     

红曲多糖液态发酵工艺条件的优化

实验研究红曲多糖的液态发酵条件,得出优化后红曲菌ZKOA发酵工艺条件：蔗糖40g/L,酵母粉4．5g／L,KH2PO4·3H2O3．5∥L．MgSO40．4g／L,植物油2mL／L,接种量8％,种龄30h,发酵液起始pH5．0,发酵时间90h,在此条件下,摇瓶和中试发酵罐中的粗多糖质量浓度分别为7．6g／L和7．34g/L。     

牛肝菌液体发酵及产多糖的影响因素研究

牛肝菌(Boletused)属外生菌根菌,美味牛肝菌多糖有明显的抗肿瘤效果。采用液体培养方法对牛肝菌菌丝体的发酵及产多糖特性进行了研究,实验考察了培养基中葡萄糖浓度和培养基的初始pH对牛肝菌菌丝量及产多糖的影响。结果表明,实验条件下,该株牛肝菌在pH值5．5—6．0,葡萄糖含量为60mg/mL时,多糖产量为6．7mg/mL。实验考察了从发酵菌丝体中提取多糖的几种方法,其中研磨法效果较好,与对照相比,多糖提取量增加了20％。     

假蜜环菌固体发酵及其产物提取工艺的优化研究

在假蜜环菌固体发酵培养基中分别添加稻草、稻糠、花生壳等农副产品进行发酵,并以无添加物的培养基发酵作为对照。实验结果表明,添加了农副产品的培养基,菌丝生长速率及发酵完成后培养基中的多糖、蛋白质含量均比对照样有所提高。此外,还对假蜜环菌发酵多糖的提取工艺进行了探讨,结果显示最适提取条件为：温度85℃,时间3．0h,料液比为1：4,在此条件下,多糖的提取率为4．6％。     

响应面法优化微波辅助提取发酵虫草菌丝体多糖工艺

为优化发酵虫草菌粉多糖的微波辅助提取工艺,在单因素实验基础上,以液固比、微波功率以及提取时间为自变量,多糖提取率为响应值,采用中心组合设计的方法,研究各自变量及其交互作用对多糖提取率的影响。利用SAS软件和响应面分析相结合的方法对发酵虫草菌粉多糖的微波辅助提取工艺进行优化,确定了微波辅助提取多糖的最佳条件：液固比值12．2,微波功率650．5W,提取时间11．8min,在此条件下,多糖提取率达到6．41％。采用此法提取的虫草菌丝体多糖,当质量浓度为1mg／mL时,对二苯代苦味肼基自由基（DPPH）清除率达到76％。     

灵芝多糖液体发酵条件的研究

液体发酵灵芝是目前灵芝多糖开发的有效途径。以灵芝的生物量和胞外多糖为指标,对影响灵芝发酵的条件进行了研究。单因素实验表明灵芝发酵的最佳碳源、(?)源和生长因子分别是葡萄糖、酵母膏和维生素B1,最适温度、起始pH值和摇床转速分别是28℃、5．5和160 rpm。最佳培养方式是接种后静置4 h再振荡培养,其生物量和胞外多糖的产量最高,分别为7．743g/L和0．907g/L。     

普鲁兰菌发酵条件的研究

本文对普鲁兰菌的发酵条件进行了研究,并总结出其高产普鲁兰多糖的条件。实验结果,普鲁兰多糖产率由６％,提高并稳定在７０％左右,最高达７６％。本文对影响普鲁兰多糖高产的发酵条件进行了分析。     

玉米水解糖液体培养灵芝发酵条件的优化

目的：优化液体培养灵芝的发酵条件,提高多糖产量。方法：采用玉米水解糖为主要成分的培养基,通过单因素和正交实验,对赤芝G22菌株液体培养过程中影响多糖产量的发酵温度、摇床转速等工艺条件进行了研究。结果：经极差分析和方差分析确定了多糖高产的最佳发酵条件为：发酵温度27℃、摇床转速170r/min、培养基初始pH值6.5、发酵时间144 h。结论：通过优化液体发酵条件,可显著提高灵芝多糖的产量。在最佳发酵条件下液体培养G22菌株,灵芝总多糖产量由1.851g/L提高到2.439g/L,提高了31.0%。     

粘性嗜热链球菌ST-1产胞外多糖发酵条件优化

应用响应面法对一株粘性嗜热链球菌ST-1的产胞外多糖的发酵条件进行了优化.根据单因素的实验结果,选取接种量,发酵温度,发酵时间作为考察因素,以胞外多糖的产量作为响应值,利用Box-Behnken实验设计方法,建立了胞外多糖产量与三个考察因素之间的回归方程并得到最佳发酵条件为:接种量5%,发酵时间14 h,发酵温度42℃...     

利用扁桃斑鸠菊叶发酵高产粗毛纤孔菌胞外多糖的条件优化及其抗氧化活性研究

粗毛纤孔菌胞外多糖是粗毛纤孔菌液体发酵的重要活性代谢产物,但采用常规的发酵方法,粗毛纤孔菌胞外多糖的产量较低。为更好地获取粗毛纤孔菌胞外多糖,本文采用双向液体发酵的方法,通过向发酵培养基中添加适量的扁桃斑鸠菊叶粉末,来提高粗毛纤孔菌胞外多糖的产量,并对优化得到的胞外多糖抗氧化活性进行了研究。以发酵液中胞外多糖含量为指标,采用单因素实验和正交实验优化发酵条件;采用红外光谱对胞外多糖的结构特征进行分析;通过测定胞外多糖对ABTS、DPPH和羟基自由基的清除率来了解其抗氧化活性。结果表明,最优发酵条件为:扁桃斑鸠菊叶粉末添加量0.5g/L、发酵时间10d、pH 6.5、接种量5.0mL,在此条件下,粗毛纤孔菌胞外多糖的产量达到(2.34±0.25)mg/mL,与未添加扁桃斑鸠菊叶的空白组相比,其胞外多糖产量提高了约216.22%;红外分析与抗氧化活性实验结果表明,添加扁桃斑鸠菊叶后的胞外多糖与未添加扁桃斑鸠菊叶的胞外多糖红外主要吸收峰一致,并且对ABTS、DPPH以及羟基自由基清除能力相近。本研究结果表明扁桃斑鸠菊叶能够有效地提高粗毛纤孔菌胞外多糖的产量,为其他珍稀食药用菌胞外多糖的高效生产提供了新思路。     

Optimization of physico‐chemical and nutritional parameters for a novel pullulan‐producing fungus,Eurotium chevalieri

Aims: To isolate the novel nonmelanin pullulan‐producing fungi from soil and to optimize the physico‐chemical and nutritional parameters for pullulan production. Methods and Results: A selective enrichment method was followed for the isolation, along with development of a suitable medium for pullulan production, using shake flask experiments. Pullulan content was confirmed using pure pullulan and pullulanase hydrolysate. Eurotium chevalieri was able to produce maximum pullulan (38 ± 1·0 g l^?1) at 35°C, pH 5·5, 2·5% sucrose, 0·3% ammonium sulfate and 0·2% yeast extract in a shake flash culture medium with an agitation rate of 30 rev min^?1 for 65 h. Conclusions: The novel pullulan‐producing fungus was identified as E. chevalieri (MTCC no. 9614), which was able to produce nonmelanin pullulan at from poorer carbon and nitrogen sources than Aureobasidium pullulans and may therefore be useful for the commercial production of pullulan. Significance and Impact of the Study: Eurotium chevalieri could produce pullulan in similar amounts to A. pullulans. Therefore, in future, this fungus could also be used for commercial pullulan production, because it is neither polymorphic nor melanin producing, hence its handling during pullulan fermentation will be easier and more economical.     

茁霉多糖发酵及提取工艺条件研究

目的：茁霉多糖是一种新型多功能生物材料,该文拟对出芽短梗霉发酵茁霉多糖及其提取条件进行初步探索。方法：通过摇瓶培养确定了该菌株的发酵优化条件,在此条件下,获得了较高的多糖产量,同时通过醇提的方法对茁霉多糖的提取进也行了研究。结果：初步确定了茁霉多糖最佳发酵与提取条件。结论：摇瓶转速和发酵初始pH值是多糖发酵的重要影响因素,它们与多糖的合成密切相关。     

Pullulan Elaboration by Aureobasidium pullulans Protoplasts

Protoplasts of Aureobasidium pullulans are capable of producing pullulan. Biosynthesis of the polymer pullulan required induction with kinetics similar to those of whole cells. The protoplasts also produced a heteropolysaccharide component containing mannose, glucose, and galactose. The relative proportions of the pullulan and heteropolysaccharide fractions were a function of glucose concentration, with the pullulan content of the total polysaccharide rising from 20% at 2.5 mM glucose to 45% at 20 mM glucose. Elaboration of pullulan by both cells and protoplasts was sensitive to 0.6 M KCl, which was present as the osmotic stabilizer in protoplast experiments. The presence of KCl resulted in a shift in the pH optimum to a more acidic value. The molecular weight of the protoplast-derived pullulan was sharply reduced from the molecular weight of the whole-cell-derived product. Exposure of the protoplasts to proteolytic enzymes had no effect on polysaccharide elaboration.     

Pullulan-hyperproducing color variant strain of Aureobasidium pullulans FB-1 newly isolated from phylloplane of Ficus sp

The studies were carried out for the isolation of efficient pullulan producing strains of Aureobasidium pullulans. Five strains were isolated from phylloplane of different plants. Amongst these, three were producing black pigment melanin, while the remaining two produced pink pigment. These two color variant isolates of A. pullulans were designated as FB-1 and FG-1, and obtained from phylloplane of Ficus benjamina and Ficus glometa, respectively. The parameters employed for the identification of the isolates included morphology, nutritional assimilation patterns and exopolysaccharide (EPS) production. Isolates were compared with standard cultures for EPS production. A. pullulans FB-1 was the best producer of pullulan giving up to 1.9, 1.4 and 1.7 times more pullulan than the control of A. pullulans NCIM 976, NCIM 1048 and NCIM 1049, respectively. The IR spectra of the isolates and standard strains revealed that the polysaccharide was pullulan, but not aubasidan. The study also supported the fact that A. pullulans is a ubiquitous organism and phylloplane being the important niche of the organism.     

出芽短梗霉发酵产生普罗蓝糖的研究

对一株野生型的出芽短梗霉(Aureobasidium pullulans)Ft1和从Ft1出发经原生质体再生筛选出的菌株R45进行了摇瓶发酵产普罗蓝糖的比较研究,结果表明R45无论从形态,菌体生长情况,还是从普罗蓝糖的产量,黑色素的产生等方面都与亲株Ft1有明显的区别,说明R45是一株具有一定生产价值的变异菌株.     

Biosynthesis and hyper production of pullulan by a newly isolated strain of Aspergillus japonicus-VIT-SB1

The main focus of this study was to screen and characterize novel microbial strains isolated from culinary leaf samples, capable of producing high concentrations of pullulan. Hundred isolates were screened from the phylloplane of different plants. The results revealed that eight strains had the capability to produce exopolysaccharide (EPS) and only one potential strain (designated as VIT-SB1) could produce the significant amount of EPS (3.9 ± 0.02 %) on the 6th day of the fermentation without optimisation. The EPS synthesized by VIT-SB1 strain was confirmed to be pullulan on the basis of the results of FT-IR, HPLC and the enzymatic (Pullulanase) analysis. More than 91 % hydrolysis of pullulan by pullulanase enzyme also indicated the presence of α (1 → 6) glycosidic linkages of α (1 → 4) linked maltotriose units. This VIT-SB1 strain was identified as Aspergillus japonicus based on the nucleotide sequence of the D1/D2 domain of Large-Subunit rRNA gene. The sequence was submitted to the GenBank Nucleotide sequence database with Accession No: KC128815. This study has confirmed that pullulan production capacity of this novel strain and Aureobasidium pullulans are comparable. Hence Aspergillus japonicus-VIT-SB1 strain can be commercially exploited as a potential pullulan producing strain.     

Pullulan production by <Emphasis Type="Italic">Aureobasidium pullulans</Emphasis> cells immobilized in chitosan beads

Fungal cells of Aureobasidium pullulans ATCC 201253 were immobilized by entrapment in chitosan beads, and the immobilized cells were investigated for their ability to produce the polysaccharide pullulan using batch fermentation. The 1% chitosan-entrapped fungal cells were capable of producing pullulan for two cycles of 168 h using corn syrup as a carbon source. Pullulan production by the immobilized cells increased by 1.6-fold during the second production cycle (5.0 g/l) relative to the first production cycle (3.1 g/l) with the difference in production being statistically significant after 168 h. The productivity of the immobilized cells increased during the second production cycle while its pullulan content decreased. The level of cell leakage from the support remained unchanged for both production cycles.     

Cell wall integrity is required for pullulan biosynthesis and glycogen accumulation in Aureobasidium melanogenum P16

Background

Pullulan and glycogen have many applications and physiological functions. However, to date, it has been unknown where and how the pullulan is synthesized in the yeast cells and if cell wall structure of the producer can affect pullulan and glycogen biosynthesis.

Estimation of pullulan by hydrolysis with pullulanase

A novel method for the estimation of pullulan was developed in which pullulan was hydrolysed by pullulanase. The hydrolysed product was mainly maltotriose and was determined colorimetrically using 3,5-dimethylsalicylic acid. This gave good linearity with respect to the concentration of pullulan in the fermentation broth. The content of pullulan determined in this way was less than that determined by a coupled enzyme assay and was comparable to that determined by an HPLC method. The new method was specific for estimation of pullulan, demonstrated high accuracy, and could assay pullulan from up to 3.2 mg/ml.     

Conjugation of heparin into carboxylated pullulan derivatives as an extracellular matrix for endothelial cell culture

A carboxylated pullulan, for use as a structural material for a number of tissue engineering applications, was synthesized and conjugated with heparin. By immobilization of heparin to pullulan, endothelial cells (ECs) attached on the heparin-conjugated pullulan were more aggregated than when attached to other pullulan derivatives. Attachments were 50, 45, 49, and 90% for a polystyrene dish, pullulan acetate, carboxylated pullulan, and heparin-conjugated pullulan, respectively. Heparin-conjugated pullulan inhibited the proliferation of smooth muscle cells (SMCs) in vitro. Heparin-conjugated pullulan material can thus be used for the proliferation of vascular ECs and to inhibit the proliferation of SMCs.