斜卧青霉转录调控因子BglR的缺失对纤维素酶生产的影响

【目的】斜卧青霉(Penicillium decumbens)作为高效分泌纤维素酶的重要丝状真菌,其纤维素酶的合成与分泌在转录水平上被调控。进一步研究纤维素酶基因表达的转录调控,构建高效高产纤维素酶的工业菌株。【方法】根据斜卧青霉114-2在不同碳源生长条件下基因组表达谱的差异,发现新的转录调控因子BglR(PDE-01706),该蛋白与产黄青霉(Penicillium chrysogenum)Pc20g04780的锌指结构蛋白具有59%同源性。通过基因同源双交换,得到BglR缺失突变株ΔbglR-1,对突变株ΔbglR-1的表型、营养生长、产纤维素酶活、蛋白分泌能力及发酵液pH变化进行研究。【结果】转录调控因子BglR的缺失可导致突变株ΔbglR-1的β-葡萄糖苷酶活力提高40%,并造成其滤纸酶活、内切葡聚糖酶及木聚糖酶活明显降低。【结论】结果表明转录调控因子BglR对于斜卧青霉纤维素酶的调控有重要作用。     

青霉PT95菌固态发酵产生类胡萝卜素的研究

本文对青霉Ｐｅｎｉｃｉｌｌｉｕｍｓｐ．ＰＴ９５菌株在固态发酵条件下菌核内产生类胡萝卜素进行了初步研究。结果表明,在３种固态发酵培养基中,玉米粉培养基（ＳＭＡ）比麸皮２基和棉籽壳培养基更适合于ＰＴ９５菌株固态发酵产生类胡萝卜素。为了增加菌核干重和提高类胡萝卜素产率,ＳＭＡ中需要添加氮源、碳源和植物油。在所度的各种氮、碳源中,以硝酸钠和麦芽糖效果最佳。通过我试验确定了在培养基盐溶液中添加硝酸钠３ｇ／Ｌ     

折流元件对环流反应器性能影响及用于苏云金茅杆菌发酵的效果

本文讨论了折流元件对环流反应器的流体力学性能的影响及用作生物反应器的研究结果。实验是在外筒规格Φ0 .2 19( 0 .2 10 )× 1.6m ,内筒规格Φ0 .153( 0 .150 )× 1m反应器内进行的 ,材质为不锈钢 ,括号内表示的是导流筒的内径。内筒装有具有强化传递过程作用的折流元件。BT发酵实验表明折流元件可改善环流反应器的发酵性能。将研究结果放大到 2 0m3的气升式环流反应器中 ,与工厂同等规模的搅拌式发酵罐相比 ,在完全省去搅拌功耗又不增加无菌空气用量的条件下 ,发酵液毒力效价高于在机械搅拌式发酵罐内的发酵结果约 10 %并且节电 30 %以上。     

斜卧青霉L-06内切葡聚糖酶Ⅰ基因的克隆与表达

【目的】克隆斜卧青霉L-06的内切葡聚糖酶Ⅰ基因(egI),并实现其在大肠杆菌内的高效表达。【方法】利用RT-PCR技术克隆了斜卧青霉L-06的内切葡聚糖酶Ⅰ基因(egI),并将egI基因克隆到原核表达载体中,构建了重组质粒pET32a-egI。【结果】转化至大肠埃希菌Rosetta(DE3),经IPTG诱导重组蛋白表达,SDS-PAGE检测结果表明:重组表达产物的相对分子质量约为80 kD,与预期相符。重组表达的菌悬液,经破碎离心,取其上清液,进行纤维素酶活性染色,获得了活性条带。DNS法测得内切酶活力为2.56 IU/mL。【结论】构建了斜卧青霉L-06内切葡聚糖酶Ⅰ的原核表达系统。     

生物反应器工程

本文在外界周期刺激强化生物反应和细胞膜传质速率新理论指导下,根据生态学的思维方式,提出了生物反应器工程的新概念,阐明了它的发展过程,并提出了生物反应器工程研究的新方法。     

生物反应器工程

本文在外界周期刺激强化生物反应和细胞膜传质速率新理论指导下,根据生态学的思维方式,提出了生物反应器工程的新概念,阐明了它的发展过程,并提出了生物反应器工程研究的新方法。     

蝉拟青霉液体发酵条件优化

采用液体发酵蝉拟青霉,对蝉拟青霉的发酵条件进行优化,以提高蝉拟青霉胞外多糖产量及生物量。摇瓶发酵条件下,在单因素基础上设计正交实验确定各因素的最佳组合。优化后得最佳发酵培养基:蔗糖8%,牛肉膏0.75%,酵母膏0.125%,MgSO_4·7H_2O 0.3%,KH_2PO_4 0.2%,麸皮0.5%。该条件下胞外多糖产量为5.96 g/L,生物量为42 g/L,较优化前提高了1倍。采用发酵罐进行扩大培养,对分批发酵时的初糖浓度进行了优化,并分析了补料分批发酵对发酵过程的影响。发酵罐培养时最适初糖浓度为5%,此时生物量最高为38 g/L,多糖含量最高为5.5 g/L;采用补料分批发酵时,多糖产量最高为5.89 g/L,生物量最高为40 g/L,效果优于分批发酵。     

用氨基葡萄糖含量的测定值间接表示红曲菌固态发酵过程中生物量的研究

【目的】为准确快速地了解紫色红曲菌固态发酵中生物量的变化,【方法】采用理化方法测定菌体量和氨基葡萄糖含量,研究了不同培养时间、培养基组成、培养方式下菌体量与氨基葡萄糖含量的关系,建立生物量和氨基葡萄糖含量的换算关系式;构建关联该菌固态培养物近红外光谱数据与实测氨基葡萄糖含量的PLS模型。【结果】建立了可通过近红外光谱法测定氨基葡萄糖来快速预测固态发酵生物量的方法,其中最优近红外模型的校正集内部交叉验证均方根误差(RMSECV)为0.209 4,预测集相关系数(Rp)和均方根误差(RMSEP)分别为0.993 4和0.217 3;同时利用所建的换算关系式也大大提高了生物量计算的准确性。【结论】基于所建立的生物量和氨基葡萄糖的换算关系式,利用近红外光谱法可以快速并且较准确地测定紫色红曲菌固态发酵过程中生物量的变化。     

青霉PT95菌株固态发酵产生类胡萝卜素的研究

本文对青霉Penicillium sp. PT95菌株在固态发酵条件下菌核内产生类胡萝卜素进行了初步研究。结果表明,在3种固态发酵培养基中,玉米粉培养基(SMA)比麸皮培养基和棉籽壳培养基更适合于PT95菌株固态发酵产生类胡萝卜素。为了增加菌核干重和提高类胡萝卜素产率,SMA中需要添加氮源、碳源和植物油。在所试的各种氮、碳源中,以硝酸钠和麦芽糖效果最佳。通过正交试验确定了在培养基盐溶液中添加硝酸钠3g/L,麦芽糖10g/L,豆油2.5g/L能使菌核干重由536g/100g提高到970g/100g(干料);类胡萝卜素产率由2149μg/100g提高到5260μg/100g(干料);β-胡萝卜素在类胡萝卜素中的含量由614%提高到71.3%。     

超高压对灵芝生长及其漆酶合成的影响

研究了超高压处理对灵芝生长及其漆酶合成的影响,试验结果表明:灵芝致死率随处理压力的增大而增加,在150MPa下处理30min获得了一株生物量和漆酶产量都大幅增加的菌株G1502,其最大生物量及酶活分别比出发菌株提高了19.34%和282.67%,发酵时间也缩短了1d。     

以麦秸为基质豌豆根瘤菌的压力脉动固态发酵

生物肥料的常规生产方法是经液态发酵后 ,再以固态基质吸附[1 ] 。其工艺繁琐 ,吸附时易引入大量杂菌 ,从而降低生物肥料的施用效果。而由于静止浅盘固态发酵存在着较大的氧气浓度和温度梯度[2 ,3 ] ,及易染菌等因素 ,所以利用固态发酵成功生产生物肥料的研究较少。近年来 ,固态发酵以其优于液态发酵的特点而成为人们研究的热点[4] ,但至今仍未能普遍应用于工业生产。其主要原因是固态发酵反应器在放大过程中传质、传热困难[3 ] 。Ｂａｊｒａｃｈａｒｙａ＆Ｍｕｄｇｅｔｔ[5 ] 指出 ,解决上述弊端的唯一可行的方法是对反应器中的气相进行控…     

Effects of air pressure amplitude on cellulase productivity by Trichoderma viride SL-l in periodic pressure solid state fermenter

Air pressure amplitude serves as a critical control parameter of periodic pressure solid state fermentation process. Effects of different air pressure amplitudes on cellulase production by Trichoderma viride-SL were investigated. Experiments were carried out in the same fermenter as reported earlier. Under the optimum periodic pressure amplitude, 1400 IU/g CMCase activity can be obtained in the system against 450 IU/g compared with the tray fermenter.     

Operating characteristics of solid-state fermentation bioreactor with air pressure pulsation

The development of solid state fermentation (SSF) technology is very important to the production of cellulase and ultimately to the utilization of natural cellulose. However, inadequate dissipation of heat generated by biological activities has prevented solid state fermentation from large-scale applications. The paper deals with the development of a novel SSF bioreactor with air pressure pulsation. By developing a measurement and control system under Virtual Instrument (VI) concept, performance of SSF bioreactor with pressure pulsation was studied by cultivating Trichoderma koningii in solid medium made of wheat bran and corncob. The cooling effects of pressure pulsation on solid porous beds are discussed. Experimental results show that pressure pulsation enhances medium moisture evaporation, and hence, heat dissipation. Furthermore, through changing the pressure pulsation directions, it is able to mitigate the temperature gradients in the bioreactor. To sum up, pressure pulsation can provide the microbes with a growing environment at optimal temperature and medium water content.     

Operating characteristics of solid-state fermentation bioreactor with air pressure pulsation

The development of solid state fermentation (SSF) technology is very important to the production of cellulase and ultimately to the utilization of natural cellulose. However, inadequate dissipation of heat generated by biological activities has prevented solid-state fermentation from large-scale applications. The paper deals with the development of a novel SSF bioreactor with air pressure pulsation. By developing a measurement and control system under the Virtual Instrument (VI) concept, the performance of the SSF bioreactor with pressure pulsation was studied by cultivating Trichoderma koningii in solid medium made of wheat bran and corncob. The cooling effects of pressure pulsation on solid porous beds are discussed. Experimental results show that pressure pulsation enhances medium moisture evaporation, and hence, heat dissipation. Furthermore, through changing the pressure pulsation directions, it is able to mitigate the temperature gradients in the bioreactor. To sum up, pressure pulsation can provide the microbes with a growing environment at optimal temperature and medium water content. The text was submitted by the authors in English.     

Effects of gas periodic stimulation on key enzyme activity in gas double-dynamic solid state fermentation (GDD-SSF)

The heat and mass transfer have been proved to be the important factors in air pressure pulsation for cellulase production. However, as process of enzyme secretion, the cellulase formation has not been studied in the view of microorganism metabolism and metabolic key enzyme activity under air pressure pulsation condition. Two fermentation methods in ATPase activity, cellulase productivity, weight lose rate and membrane permeability were systematically compared. Results indicated that gas double-dynamic solid state fermentation had no obviously effect on cell membrane permeability. However, the relation between ATPase activity and weight loss rate was linearly dependent with r = 0.9784. Meanwhile, the results also implied that gas periodic stimulation had apparently strengthened microbial metabolism through increasing ATPase activity during gas double-dynamic solid state fermentation, resulting in motivating the production of cellulase by Trichoderma reesei YG3. Therefore, the increase of ATPase activity would be another crucial factor to strengthen fermentation process for cellulase production under gas double-dynamic solid state fermentation.     

纤维素酶固态发酵过程中菌体生长量的测定

纤维素酶在植物再生资源的利用中占有重要地位,目前世界各地均在进行广泛而深入的研究。纤维素酶的生产有固态发酵和液体深层发酵两种方法,由于前者与后者相比具有许多优点,因此纤维素酶的生产主要采用固态发酵法。 根据Durand等给出的固态发酵定义,在固态发酵中微生物的菌丝体紧密地结合于固体基质上,这种情况给菌体生长量的测定带来了极大的困难。与液体深层发酵不同,其菌丝体无法定量地与固体基质相分     

Impact of operating conditions on performance of a novel gas double-dynamic solid-state fermentation bioreactor (GDSFB)

A self-designed novel solid-state fermentation (SSF) bioreactor named “gas double-dynamic solid-state fermentation bioreactor (GDSFB)” showed great success in processes for the production of several valuable products. For the present study, a simple GDSFB (2 L in volume) was designed to investigate the impact of exhaust time on SSF performance. Both air pressure and vent aperture significantly influenced the exhaust time. The production of cellulase by Penicillium decumbens JUA10 was studied in this bioreactor. When the vent aperture was maintained at 0.2 cm, the highest FPA activity of 17.2 IU/g dry solid-state medium was obtained at an air pressure of 0.2 MPa (gauge pressure). When the air pressure was maintained at 0.2 MPa, a vent aperture of 0.3 cm gave the highest FPA activity of 18.0 IU/g dry solid-state medium. Further analysis revealed that the exhaust time was a crucial indicator of good performance in GDSFB.     

Relationships between hydrodynamics and rheology of flocculating yeast suspensions in a high-cell-density airlift bioreactor

In this article a hydrodynamic and rheological analysis of a continuous airlift bioreactor with high-cell-density system is presented. A highly flocculating recombinant strain of Sacharomyces cerevisiae containing genes for lactose transport (lactose permease) and hydrolysis (beta-galactosidase) was exploited to ferment lactose from cheese whey to ethanol. The magnetic particle-tracer method was used to assess the effect of operational conditions (air-flow rate, biomass concentration) on hydrodynamic behavior of an airlift bioreactor during the fermentation process. Measurements of liquid circulation velocity showed the existence of a critical value of biomass concentration at which a dramatic deceleration of net liquid flow appeared with increasing biomass quantity. Rheological analysis revealed exponential increase of viscosity of the yeast floc suspension at the same biomass concentration of about 73 g/dm3 corresponding to 42.8% v/v of solid fraction. These facts have a particular importance for the successful processing of a high-cell-density airlift bioreactor as only a circulated flow regime will be favorable to keep the solid particles in suspension state and evenly distributed throughout the bioreactor.     

超高浓度培养基条件下酵母细胞生长及酒精生成的准稳态动力学研究

在1．5L搅拌式发酵罐中,使用葡萄糖质量浓度分别为120、200、280g／L的培养基进行酿酒酵母Saccharomyces cerevisiae连续发酵生成酒精的动力学研究。研究发现,当培养基中葡萄糖浓度为200和280g／L时,发酵液中残糖浓度、酒精浓度以及菌体生物量从小幅度波动的准稳态发展到大幅度波动的振荡状态。提出了伴有周期性振荡现象准稳态过程的概念,并针对该过程,建立了兼有底物和产物抑制的酵母细胞生长和产物酒精生成动力学模型。     

Rheology and Hydrodynamic Properties of Tolypocladium inflatum Fermentation Broth and Its Simulation

A physico-chemical, two phase simulated pseudoplastic fermentation (SPF) broth was investigated in which Solka Floc cellulose fibre was used to simulate the filamentous biomass, and a mixture of 0.1% (w/v) carboxymethyl cellulose (CMC) and 0.15 M aqueous sodium chloride was used to simulate the liquid fraction of the fermentation broth. An investigation of the rheological behaviour and hydrodynamic properties of the SPF broth was carried out, and compared to both a fungal Tolypocladium inflatum fermentation broth and a CMC solution in a 50 L stirred tank bioreactor equipped with conventional Rushton turbines. The experimental data confirmed the ability of the two phase SPF broth to mimic both the T. inflatum broth bulk rheology as well as the mixing and mass transfer behaviour. In contrast, using a homogeneous CMC solution with a similar bulk rheology to simulate the fermentation resulted in a significant underestimation of the mass transfer and mixing times. The presence of the solid phase and its microstructure in the SPF broth appear to play a significant role in gas holdup and bubble size, thus leading to the different behaviours. The SPF broth seems to be a more accurate simulation fluid that can be used to predict the bioreactor mixing and mass transfer performance in filamentous fermentations, in comparison with CMC solutions used in some previous studies.