积累L-苹果酸的米根霉突变株酶活性初探

对富马酸产生菌株—米根霉ME-F10进行诱变育种的过程中, 得到一株性能稳定的高效积累L-苹果酸的突变株ME-M15。该菌株发酵96 h平均L-苹果酸产量达16.3 g/L, 较出发菌株L-苹果酸积累量平均提高3倍, 而富马酸和乙醇的积累量大幅下降。对突变株代谢途径关键酶活研究表明, 突变株富马酸酶胞质途径同功酶和乙醇脱氢酶活力较之出发菌株酶活力明显减弱, 而丙酮酸羧化酶活力无明显差别。     

米根霉乙醇脱氢酶(ADH)突变菌株的诱变选育

米根霉发酵生产L-乳酸过程中,由于丙酮酸在丙酮酸脱羧酶、乙醇脱氢酶(ADH)催化下生成乙醇,使得丙酮酸向乳酸转化的流量减少。采用亚硝基胍(NTG)诱变米根霉AS3．3462孢子液,诱变剂量为0．15 mg/ mL时,致死率为70%～80%。在含丙烯醇的YPD筛选培养基上筛选获得两株ADH活力降低的突变株mut-1和mut-2,检测突变株mut-1和mut-2的最大ADH活力分别为35．67和43．09U/mL,是原始菌株的41．63%和50．29%。发酵72h后,原始菌株的乙醇与乳酸浓度分别为28．9g/L和40．31g/L,而mut-1和mut-2突变株的乙醇产量分别为4．87g/L和6．56g/L,乳酸产量为54．45g/L和44．07g/L。在相同的发酵条件下,米根霉ADH突变株mut-1和mut-2对还原糖的利用速率高于出发菌株,其生物量积累亦高于出发菌株。     

膜反应器固定化米根霉发酵产富马酸的工艺研究

以膜反应器固定化米根霉发酵产富马酸为研究对象,以Na2CO3为中和剂,考察固定化米根霉在5L搅拌式发酵罐中的发酵特征,采用智能可视化软件(IVOS)优化发酵工艺条件。结果表明,在80g/L初始糖浓及最优工艺下,富马酸产量、生产速率及转化率分别为21.1g/L、0.25g/(L·h)和28%;采用40g/L初始糖浓及连续批次发酵工艺时,富马酸产量、生产速率及转化率最高分别为10.8 g/L、0.36g/(L·h)和27%。搅拌式反应器中,固定化米根霉的膜反应器比表面积有限,以及菌膜的空间阻隔效应对传质传氧的限制作用,显著影响了富马酸的生产强度和转化率。因此,亟需发掘新的固定化方法及反应器形式,达到既解决米根霉形态控制问题,又有助于生产性状提升的目标。     

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。     

基于智能可视化优化上的米根霉发酵生产富马酸过程的优化

为提高米根霉发酵产富马酸的效率,对米根霉发酵过程进行了优化。通过单因素实验考察不同氮源对富马酸合成的影响,确定了米根霉ME-F14发酵产富马酸的最佳氮源为(NH4)2SO4;在此基础上采用均匀实验设计法进行试验设计,并利用智能可视化优化软件对发酵培养基的组分和培养条件进行优化。当接种龄为12 h、葡萄糖87.5 g/L、(NH4)2SO40.55 g/L、接种量27.5%时,富马酸产量达43.8 g/L,比对照组提高了31.81%。此结果可以为发酵法制备富马酸的工业化生产奠定基础。     

碱预处理玉米芯米根霉同步糖化发酵产富马酸

以碱预处理玉米芯渣为原料,采用单因素优化方法优化米根霉同步糖化发酵产富马酸。在此基础上,研究米根霉利用碱预处理玉米芯渣的同步糖化发酵,并与纯糖发酵进行对比。结果表明:在50 g/L底物、(NH4)2SO4质量浓度0.71 g/L、纤维素酶用量20 FPIU(以1 g纤维素计)、Ca CO3加入量30 g/L、接种量10%(体积分数)和装液量50 m L的条件下,米根霉同步糖化发酵过程产富马酸13.78 g/L,而纯糖发酵富马酸生成量仅6.21 g/L。     

一株产生L-乳酸的米根霉

为获得理想的L-乳酸产生菌,选择适合根霉属微生物生长的土样,利用溴甲酚绿平板结合摇瓶复筛的方法得到了一株有一定L-乳酸积累能力的米根霉Rhizopus oryzae CS323。摇瓶发酵试验显示,在未优化发酵条件的情况下发酵48h,米根霉CS323L-乳酸积累量达到50.1g/L,是一株有良好改造潜力的L-乳酸产生菌,适合作为进一步诱变育种的出发菌株。     

耐高糖高产2,3-丁二醇产酸克雷伯氏杆菌的选育

以产酸克雷伯氏杆菌(Klebsiella oxytoca) ME-UD-3为出发菌株,经紫外线及硫酸二乙酯复合诱变后分别在葡萄糖浓度逐渐提高的液体培养基中进行富集培养,筛选获得了一株耐高糖的2,3-丁二醇高产突变菌株K. oxytoca ME-UD-3-4;该菌株的初始葡萄糖耐受浓度从出发菌株的120g/L提高到300g/L以上,在初始葡萄糖浓度为95 g/L的条件下发酵培养,与出发菌株相比发酵时间缩短了8h,2,3-丁二醇的产量由原来的38.5g/L提高到43.0g/L,生产强度从0.80 g/L·h提高到1.08 g/L·h,转化率达到了理论值的91%。     

米根霉利用纯糖和不同预处理玉米秸秆酶解糖生产L-乳酸

通过单因素实验设计,优化米根霉摇瓶发酵产L-乳酸。在此基础上,以蒸气爆破和碱处理玉米秸秆酶解液为混合C源,与纯糖对比,研究不同预处理玉米秸秆混合C源对米根霉发酵产L-乳酸的影响。结果显示:在初始葡萄糖质量浓度100g/L、(NH4)2SO4质量浓度2g/L、接种量6%(体积分数)、转速170r/min、发酵12h后添加30g/LCaCO3的条件下,米根霉发酵产L-乳酸质量浓度为69.15g/L。米根霉发酵不同预处理玉米秸秆酶解混合C源,木糖的存在影响了米根霉的C代谢网络,降低L乳酸的产量。     

小克银汉霉γ-亚麻酸高产菌株的快速筛选和发酵条件研究

以小克银汉霉C0为出发菌株,经过5-氟尿嘧啶和紫外线复合诱变,采用抗失水苹果酰肼与抗低温(15℃)相结合的筛选方法,获得一株生产性能比出发菌株显著提高的突变株C23。采用5L全自动发酵罐对小克银汉霉C23发酵生产γ-亚麻酸的pH值控制和补料工艺进行研究,发现将发酵液pH值维持在5.5,当发酵进行到60h、84h、108h时,分别补糖15g/L,发酵192h后收获,结果生物量、油脂产量和γ-亚麻酸产量分别达到49.88g/L、21.93g/L、2.69g/L。     

Investigation of the mechanism of temperature sensitivity of the electroreceptors of ampullae of lorenzini

In experiments on Black Sea skates (Raja clavata), the potential of the receptor epithelium of the ampullae of Lorenzini and spike activity of single nerve fibers connected to them were investigated during electrical and temperature stimulation. Usually the potential within the canal was between 0 and –2 mV, and the input resistance of the ampulla 250–400 k. Heating of the region of the receptor epithelium was accompanied by a negative wave of potential, an increase in input resistance, and inhibition of spike activity. With worsening of the animal's condition the transepithelial potential became positive (up to +10 mV) but the input resistance of the ampulla during stimulation with a positive current was nonlinear in some cases: a regenerative spike of positive polarity appeared in the channel. During heating, the spike response was sometimes reversed in sign. It is suggested that fluctuations of the transepithelial potential and spike responses to temperature stimulation reflect changes in the potential difference on the basal membrane of the receptor cells, which is described by a relationship of the Nernst's or Goldman's equation type.I. P. Pavlov Institute of Physiology, Academy of Sciences of the USSR, Leningrad. I. M. Sechenov, Institute of Evolutionary Physiology and Biochemistry, Academy of Sciences of the USSR, Leningrad. Pacific Institute of Oceanology, Far Eastern Scientific Center, Academy of Sciences of the USSR, Vladivostok. Translated from Neirofiziologiya, Vol. 12, No. 1, pp. 67–74, January–February, 1980.     

Principles of organization and evolution of systems of regulation of functions

Evolution of living organisms is closely connected with evolution of structure of the system of regulations and its mechanisms. The functional ground of regulations is chemical signalization. As early as in unicellular organisms there is a set of signal mechanisms providing their life activity and orientation in space and time. Subsequent evolution of ways of chemical signalization followed the way of development of delivery pathways of chemical signal and development of mechanisms of its regulation. The mechanism of chemical regulation of the signal interaction is discussed by the example of the specialized system of transduction of signal from neuron to neuron, of effect of hormone on the epithelial cell and modulation of this effect. These mechanisms are considered as the most important ways of the fine and precise adaptation of chemical signalization underlying functioning of physiological systems and organs of the living organism