中药内的生物制药——固体发酵工程系列及其真菌药物

概述了我国古今中药内的生物制药工程中唯一的固体发酵生产真菌药物的情况,以神曲、猴头菌及槐耳菌质等为代表说明由"制曲工艺"、"固体培养"到固体发酵的理念与工艺的变化与发展,从"普通型固体发酵"发展到"双向型固体发酵"的范例可推断分析古代制曲工艺在基质中应用中药材的作用,说明其貌似粗糙而可能有潜在深刻的内涵亟待整理发掘。现已存在建立固体发酵系列工程的可能性,更显示了中药宝库的丰富内容和菌物药的价值,对指导研发新真菌药物有一定理论与实际意义。     

灵芝真菌液体发酵及其产物应用的研究进展

灵芝作为一种白腐真菌,同时也是珍稀的食药用真菌,富含多种生物活性成分。液体发酵技术生产周期短、效率高、产量大、品质稳定,是开发利用灵芝资源的重要途径。近年来,灵芝属真菌菌丝体液体发酵技术的开发与应用取得了较大进展。本文对灵芝属真菌液体发酵产物的主要活性成分及其药用效果、液体发酵工艺优化和发酵产物的应用进行综述,并对本领域的未来进行展望。     

生防用枯草芽孢杆菌固态发酵工艺的研究

目的:提高一株生防用枯草芽孢杆菌固体发酵生产过程中的芽孢产量。方法:研究通过优化固体发酵培养基及发酵生产工艺条件等方法提高了固体发酵枯草芽孢杆菌的芽孢产量。结果:固体发酵过程中,豆饼粉作用显著,能显著提高固体发酵枯草芽孢杆菌的芽孢数,可达到7.1×1010CFU/g。结论:该枯草芽孢杆菌的最优培养基为:麸皮84.4%、稻壳粉10%、豆饼粉5%、硫酸铵0.5%、硫酸镁0.1%、硫酸锰0.05%。生产工艺为料水比为1:1.2,发酵温度为37℃,发酵培养时间为52 h。     

食药用真菌寡糖研究进展及展望

食药用真菌中多糖和寡糖独特的生物学活性引起了广泛的关注。寡糖一般通过多糖降解获得,与多糖相比,寡糖分子量低、结构相对简单、易于吸收。挖掘高活性寡糖链,阐明寡糖结构和活性的构效关系,有助于突破解析多糖复杂结构的技术瓶颈,揭示食药用真菌药理活性的作用机制。目前,人（乳）、动物和微生物（细菌）源的寡糖开发利用已有大量研究报道,而食药用真菌寡糖的研究还相对较少。文中系统总结了国内外食药用真菌寡糖的最新研究进展,详细评述了寡糖活性评价与结构鉴定的相关研究手段及成果。我国食药用真菌资源丰富,构建食药用真菌寡糖库,高通量筛选活性寡糖,阐明寡糖活性的作用机制对食药用真菌的产品开发,研发及临床应用食药用真菌相关保健品、药品,具有重要意义。     

先进固体发酵技术(ASSF)生产甜高粱乙醇

介绍了利用高产能源作物甜高粱生产燃料乙醇的先进固态发酵(ASSF)技术,从甜高粱茎秆保存、菌种、反应器,到固体发酵过程的数学模拟和工程放大进行了系统研究。筛选出高效产乙醇的菌种CGMCC1949,固体发酵时间低于30 h,乙醇收率高于92%;优选出贮存甜高粱茎秆的有效方法,通过抑菌处理,厌氧贮存200 d糖分损失小于5%;对固态发酵过程进行了数学模拟,设计并优化了固体发酵设备,成功进行了工程放大试验,并且基于ASPEN软件对该技术进行了技术经济评价,结果表明ASSF法生产甜高粱乙醇在技术、工程和经济上均具有充分的可行性和明显优势。     

海洋真菌Diaporthe sp.产真菌环氧二烯发酵条件的优化

从海洋木栖真菌HLY-2分离得到的真菌环氧二烯(Mycoepoxydiene)是新发现的高抗肿瘤活性化合物。通过正交设计,改良普通半海水PD培养基的配方,比较固体和液体两种发酵方法,得到了使该化合物产量大幅提高的最佳培养条件:在固体发酵条件下土豆250g/L,海水300mL/L,葡萄糖30g/L,乳糖50g/L,磷酸二氢钾0·65mmol/L,硫酸铵1g/L,产量高达543mg/L,比普通的PD培养基提高了43倍,也比液体发酵的最高产量提高了近15倍。同时还对固体发酵和液体发酵造成的产量差异进行了分析。并检验了发酵产物的抗肿瘤活性。     

海洋真菌Diaporthe sp.产真菌环氧二烯发酵条件的优化*

从海洋木栖真菌HLY-2分离得到的真菌环氧二烯(Mycoepoxydiene)是新发现的高抗肿瘤活性化合物。通过正交设计,改良普通半海水PD培养基的配方,比较固体和液体两种发酵方法,得到了使该化合物产量大幅提高的最佳培养条件:在固体发酵条件下土豆250g/L,海水300mL/L,葡萄糖30g/L,乳糖50g/L,磷酸二氢钾0·65mmol/L,硫酸铵1g/L,产量高达543mg/L,比普通的PD培养基提高了43倍,也比液体发酵的最高产量提高了近15倍。同时还对固体发酵和液体发酵造成的产量差异进行了分析。并     

食品上的应用

<正> 现在固体基质发酵正在用于生产各种食品、饮料及有关的产品,利用真菌的固体基质发酵产品包括酱油、日本豆酱、temPe、 ontjorn(印尼一种花生饼发酵食品)、日本清酒和面包,己生产了几个世纪。固体发酵也应用于动物性产品如:山牛奶生产的     

内生真菌产紫杉醇研究的回顾与展望

紫杉醇是一种高效、低毒、广谱的天然抗癌药物,是人类未来20年间最有效的抗癌药物之一。近年来的研究发现,从植物内生真菌中发酵生产紫杉醇被证明是解决药源问题的有效途径。本文概述了微生物发酵生产紫杉醇的研究进展,包括产紫杉醇内生真菌的分离、多样性和真菌产紫杉醇的优势,紫杉醇的提取和检测技术,同时对如何提高内生真菌紫杉醇产量进行了比较全面的综述。随着现代分子生物学技术和微生物发酵工程的发展,工业上大规模发酵生产紫杉醇将有望实现。     

食药用真菌降血脂作用的研究及应用

综述了食药用真菌降血脂药物的研究方法、食药用真菌降血脂的机制以及应用前景。食药用真菌从抑制胆固醇的生物合成、阻止胆固醇或胆酸的吸收或促进其排出以及促进脂类代谢等方面发挥降血脂的作用。     

模拟青霉素分批补料发酵过程的细胞自动机模型

根据青霉素产生菌的生长机理和青霉素分批补料发酵过程的动力学特性,在Paull等建立的形态学结构动力学模型的基础上,建立了模拟青霉素分批补料发酵过程的细胞自动机模型。模型采用三维细胞自动机作为菌体生长空间,采用Moore型邻域作为细胞邻域,其演化规则根据青霉素分批补料发酵过程中菌体生长机理和简化动力学结构模型设计。模型中的每一个细胞既可代表单个产黄青霉菌体细胞,又可代表特定数量的这种菌体细胞,它具有不同的状态。对模型进行的仿真实验结果表明：模型不但能一致地复现形态学结构动力学模型所描述的青霉素分批补料发酵过程的演化特性,而且较形态学结构动力学模型更加直观地刻画了青霉素分批补料发酵过程的演化行为。最后,对所建模型在实际生产过程中的应用问题进行了分析,指出了需要进一步研究的问题。     

Potential of the waste from beer fermentation broth for bio-ethanol production without any additional enzyme, microbial cells and carbohydrates

The potential of the waste from beer fermentation broth (WBFB) for the production of bio-ethanol using a simultaneous saccharification and fermentation process without any extra additions of saccharification enzymes, microbial cells or carbohydrate was tested. The major microbial cells in WBFB were isolated and identified. The variations in compositions of WBFB with stock time were investigated. There was residual activity of starch hydrolyzing enzymes in WBFB. The effects of reaction modes e.g. static and shaking on bio-ethanol production were studied. After 7 days of cultivation using the supernatant of WBFB at 30 °C the ethanol concentration reached 103.8 g/L in shaking culture and 91.5 g/L in static culture. Agitation experiments conducted at a temperature-profile process in which temperature was increased from 25 to 67 °C shortened the simultaneous process time. The original WBFB was more useful than the supernatant of WBFB in getting the higher concentration of ethanol and reducing the fermentation time. From this whole study it was found that WBFB is a cheap and suitable source for bio-ethanol production.     

表面展示工程在酒精发酵方面的应用

目前,表面展示工程作为一种新型的极具应用潜力的技术手段,在组合文库的筛选、蛋白质工程、燃料乙醇的生产和生物修复等技术中已经扮演了极其重要的角色.介绍了表面展示工程在酒精发酵方面的应用,重点阐述酒精发酵过程中酶类展示原理和全细胞催化的应用前景.     

棘孢曲霉固态发酵柚皮产柚苷酶的条件优化

【目的】以柚皮为原料,优化棘孢曲霉利用柑橘加工副产物固态发酵柚苷酶的条件。【方法】采用高效液相色谱法检测酶活力,通过单因素试验考察固水比、装样量、接种量、温度对柚苷酶发酵的影响,用正交试验优化发酵条件。【结果】单因素试验结果的显著性分析表明培养基的固水比、装样量和培养温度对柚苷酶产量有显著性影响,而接种量影响不显著;经正交试验确定的优化条件是：固水比1:1 (质量体积比),装样量5 g/250 mL三角瓶,温度为30 °C,接种1 mL孢子悬浮液,发酵8 d。在此优化条件下,柚苷酶酶活力为8.19 IU/g干物质,比初始培养基产柚苷酶活力提高7.38倍。【结论】通过对固水比、装样量和发酵温度进行优化,大幅度提高了棘孢曲霉固态发酵柑橘加工副产物的柚苷酶产量,为柚苷酶的生产提供了一种高产发酵工艺。     

一株高产脯氨酸的嗜醋酸棒杆菌的选育及发酵条件优化

以嗜醋酸棒杆菌为出发菌株,经过片段化全基因组体外诱变、重组和连续的磺胺胍抗性筛选,获得一株L-脯氨酸的高产菌株。摇瓶发酵优化结果表明,葡萄糖、生物素和硫胺素的最适用量分别为16%、300μg/L、400μg/L,最适pH为6.8~7.0,装液量为25ml/500ml摇瓶,发酵培养72h后L-脯氨酸产率高达到75.6g/L,与对照相比提高了5%。考察了50L发酵罐中细胞生长对L-脯氨酸产量的影响,补料分批发酵结果表明(比生长速率分别为0.06/h、0.08/h和0.1/h),比生长速率在0.08/h左右时L-脯氨酸的产率最高,L-脯氨酸的比生产速率Q_P达到0.091 g/(g.h),产率高达82.1 g/L,比优化前提高了14%。     

固态间歇补料乙醇生料发酵新工艺

浓醪发酵是酒精生产的发展方向。与现行酒精厂普遍采用的热蒸煮工艺相比, 生料发酵技术的发展使得浓醪发酵更容易进行。本研究首次在生料发酵中直接采用固态原料间歇补料, 比较了STARGENTM生淀粉水解酶间歇补料工艺和传统无补料工艺, 并对不同补料方式进行了研究。结果表明: 与传统无补料生料发酵工艺相比, 在相同的干基配料浓度30%、相同的生料酶添加量0.22%(W/W)的条件下, 采用15%的起始配料浓度、发酵15~25 h进行间歇补料的新工艺, 酒精产量从17.06%提高到18.50%。该间歇补料优化工艺的建立, 丰富了生料发酵技术的应用。     

Yeast cell-free enzyme system for bio-ethanol production at elevated temperatures

A yeast cell-free enzyme system containing an intact fermentation assembly and that is capable of bio-ethanol production at elevated temperatures in the absence of living cells was developed to address the limitations associated with conventional fermentation processes. The presence of both yeast glycolytic and fermentation enzymes in the system was verified by SDS-PAGE and LC–MS/MS Q-TOF analyses. Quantitative measurements verified sufficient quantities of the co-factors ATP (1.8 mM) and NAD⁺ (0.11 mM) to initiate the fermentation process. Bio-ethanol was produced at a broad temperature range of 30–60 °C but was highly specific to a pH range of 6.0–7.0. The final bio-ethanol production at 30, 40, 50, and 60 °C was 3.37, 3.83, 1.94, and 1.60 g/L, respectively, when a 1% glucose solution was used, and the yield increased significantly with increasing cell-free enzyme concentrations. A comparative study revealed better results for the conventional fermentation system (4.46 g/L) at 30 °C than the cell-free system (3.37 g/L); however, the efficacy of the cell-free system increased with temperature, reaching a maximum (3.83 g/L) at 40 °C, at which the conventional system could only produce 0.48 g/L bio-ethanol. Successful bio-ethanol production using a single yeast cell-based enzyme system at higher temperatures will lead to the development of novel strategies for efficient bio-ethanol production through SSF.     

Characterization of technological features of dry yeast (strain I-7-43) preparation, product of electrofusion between Saccharomyces cerevisiae and Saccharomyces diastaticus, in industrial application

The aim of the study was to verify the technological usability and stability of biotechnological features of active dry distillery yeast preparation (strain I-7-43 with amylolytic abilities) applied to full-scale production of agricultural distillery. Various reduced doses of glucoamylase preparation (San-Extra L) were used for starch saccharification, from 90% to 70% in relation to the full standard dose of preparation. The dry distillery yeast I-7-43 were assessed positively in respect to fermentation activity and yield of ethanol production. Application of the dry yeast I-7-43 preparation in distillery practice lowers the costs of spirit production by saving the glucoamylase preparation (up to 30%) used in the process of mash saccharification. Concentrations of the volatile fermentation by-products in raw spirits obtained from fermentations with application of I-7-43 strain were on the levels guaranteeing good organoleptic properties of distillates.     

医学院校生物技术专业发酵工程实验体系的构建

为建设有特色的生物技术专业和培养创新复合型人才,本研究结合医学院校特点,充分利用"医"和"药"的资源,合理安排实验项目,构建了科学的发酵工程实验教学体系。结果表明该实验教学体系教学效果良好。学生的操作能力显著提高。为强化发酵工程教学,探索产学研联合培养模式将成必然。     

Generalised additive modelling approach to the fermentation process of glutamate

In this work, generalised additive models (GAMs) were used for the first time to model the fermentation of glutamate (Glu). It was found that three fermentation parameters fermentation time (T), dissolved oxygen (DO) and oxygen uptake rate (OUR) could capture 97% variance of the production of Glu during the fermentation process through a GAM model calibrated using online data from 15 fermentation experiments. This model was applied to investigate the individual and combined effects of T, DO and OUR on the production of Glu. The conditions to optimize the fermentation process were proposed based on the simulation study from this model. Results suggested that the production of Glu can reach a high level by controlling concentration levels of DO and OUR to the proposed optimization conditions during the fermentation process. The GAM approach therefore provides an alternative way to model and optimize the fermentation process of Glu.