Streptoverticillium mobaraense分批发酵生产谷氨酰胺转胺酶:氨基酸代谢流分析及其初始淀粉浓度的影响

对Streptoverticilliummobaraense分批发酵合成谷氨酰胺转胺酶 (MTG)的氨基酸代谢流分布进行了理论分析 ;通过考察MTG分批发酵过程中的一些参数的变化情况 ,包括菌体干重 (DCW )、MTG酶活及残糖 (RSC)、菌体产率系数、MTG产率系数以及MTG的生产强度等 ,确定了适宜的初始淀粉浓度 ;对MTG发酵过程中氨基酸的代谢流分布进行了计算并作了较详细的分析 .研究结果表明 ,初始淀粉浓度 30g/L较适宜 ,DCW最高达 2 0 .9g/L ,酶活最高可达 2 .8UmL-1,菌体产率系数、MTG产率系数和MTG的生产强度分别为 0 .94g/g、12 5 .4U/g和 5 1.9UL-1h-1.氨基酸代谢流分布表明 ,只要发酵液中游离氨基酸充分 ,则细胞生长和产物形成就会活跃 ,限制细胞生长和产物的一个重要因素可能是MTG对氨基酸氮源的交联行为 ,表明可以采用不同氮源和控制氮源水平的方法改进菌体生长和MTG合成 .图 9表 2参 9     

温度对赤霉素发酵的影响及优化策略

温度是影响赤霉素发酵的重要因素,研究温度与菌丝生长和次级代谢物合成的关系将有助于发酵工艺优化.采用5 L全自动发酵罐,调控罐温在25-35℃范围内进行赤霉素发酵,分时记录菌体浓度、残糖浓度和产物赤霉素浓度变化情况.发酵过程数据经微分处理后,比较分析在不同温度下赤霉素发酵过程中菌比生长速率、菌得率及赤霉素比合成速率的变化特征.结果显示:最适菌丝生长温度是32℃,其比生长速率和得率分别为0.571/h和0.431 g/g;适宜GA3合成的温度是28℃,最大比合成速率为2.161 mg g~(-1) h~(-1).进而提出赤霉素发酵过程变温控制轨迹:发酵0-18 h,控温28℃;18-40 h,温度32℃;40-60 h控制温度为30℃;60 h后,控制温度28℃.采用此温度控制策略进行GA3发酵,赤霉素终浓度达到2 294 mg/L,比恒温28℃发酵浓度提高了11.14%.本研究表明赤霉素发酵过程分阶段变温控制策略能提高产量,具有产业应用前景.     

米曲霉产氨基酰化酶条件及部分酶学性质研究

通过单因子和多因子摇瓶正交优化试验,确定了米曲霉液态发酵产氨基酰化酶的最佳发酵条件.优化发酵培养基组成(ρ/gL-1):葡萄糖40,蔗糖10,可溶性淀粉20,蛋白胨2.5,马铃薯液1000mL,pH自然.培养基装量50mL/250mL三角瓶,接种量4%.培养温度30℃,转速100r/min,发酵时间42h.每50mL培养物的总酶活由优化前的2627u提高到7338u,是优化前的2.79倍.研究了米曲霉氨基酰化酶的部分酶学性质.该酶催化反应的最适pH为7.0,最适温度为40℃,低浓度的Co2 (5×10-4mol/L)对酶活激活作用显著.图5表2参8     

芽孢杆菌发酵产碱性果胶酶温度控制策略

采用自行筛选获得一株产碱性果胶酶芽孢杆菌WSH03-09,在小型发酵罐中研究了不同温度对碱性果胶酶分批发酵的影响,结果表明,在恒定39℃条件下,可获得最高酶活5．39u／mL,各温度条件下的菌体干重相差不多,最终均能达11．5g／L左右;在发酵前期,控制温度41℃时最有利于菌体的生长,而在产物合成期,控制37℃有利于获得较高的产物合成比速,在此基础上,提出分阶段温度控制策略,采用此温度控制策略进行碱性果胶酶的发酵,碱性果胶酶酶活达5．99u／mL,比采用单一温度下的最大值提高了11％,其它各项指标也有较大提高．图6表1参6     

维生素C二步发酵中L-山梨糖脱氢酶的性质及作用

从氧化葡萄糖酸杆菌细胞质中分离纯化出L 山梨糖脱氢酶 (SDH) ,其分子量为 46× 10 3 ,表观分子量为 190× 10 3 ;在测试范围内 ,最适pH是 7.4,温度为 5 5℃ ,最稳定的 pH是 7.0 ,温度为 30℃以下 ;FeCl3 促进酶活 ,CoCl2 抑制酶活 .该酶活力与发酵产物 2 酮基 L 古龙酸的合成呈正相关 ;伴生菌促进产酸菌生长和代谢 ,并使该酶比活力增加 ,从而提高发酵系统中该酶的总活力 .图 11表 5参 9     

运动发酵单胞菌共表达α-淀粉酶和葡萄糖淀粉酶发酵甘薯生产乙醇

运动发酵单胞菌是乙醇发酵的极佳菌种,但其所能利用的发酵底物范围狭窄,不能利用淀粉作为发酵底物.为增加其利用底物的范围使其能够水解淀粉,本研究构建了3种表达淀粉酶的运动发酵单胞菌菌株:1)Zymomonas mobilis(pAmyE)表达α-淀粉酶;2)Z.mobilis(pGA)表达葡萄糖淀粉酶;3)Z.mobilis(pAmyGA)共同表达α-淀粉酶和葡萄糖淀粉酶.DNS法测定淀粉酶活显示,每种转化菌株的胞外淀粉酶活性均高于胞内,且两种淀粉酶共表达的酶活高于这两种淀粉酶单独表达的酶活之和,说明这两种淀粉酶能够协同作用降解淀粉.对于重组菌株Z.mobilis(pAmyGA),约59.3%的淀粉酶活性都在胞外检测到.用淀粉含量高且耐贮存的徐薯18匀浆加少量葡萄糖作为培养基直接用上述3个菌株发酵生产乙醇.结果显示,共表达α-淀粉酶和葡萄糖淀粉酶的重组菌株Z.mobilis(pAmyGA)的乙醇产量为54.7 g/L,达到了理论值的83.2%,表明本研究得到了能够直接高效利用淀粉生产乙醇的运动发酵单胞菌的菌株.     

一株耐受糠醛的纤维素降解菌Bacillus siamensis BREC-11的分离与鉴定

糠醛是木质纤维素转化过程中产生的有毒的代谢抑制物,能阻碍菌株正常发酵,增加发酵成本.为提高发酵菌株耐受糠醛的能力,促进对木质纤维素的高效转化,以糠醛为耐受物添加到培养基中,竹虫幼虫肠道作为分离源,经刚果红染色法初步筛选,分离到一株可耐受糠醛的纤维素降解菌株BREC-11;通过形态学观察、生理生化分析、细胞化学分析、16S rDNA序列比对等多相分类学方法鉴定;进一步进行了不同浓度糠醛耐受试验研究,并测定菌株的滤纸酶活(FPA)、CMC酶活、纤维二糖酶活(β-G).确定菌株BREC-11属于芽孢杆菌属的一个种,将其定名为Bacillussiamensis BREC-11.菌株BREC-11在含3.5 g/L糠醛的培养基中可以生长;在3.5 g/L糠醛的耐受浓度下,在30℃、150 r/min培养2 d后,滤纸酶活达到0.1 U/m L,CMC酶活达到0.21 U/m L,纤维二糖酶活达到0.07 U/m L.本研究表明BREC-11是一株耐受糠醛的纤维素降解菌株,在生物炼制过程中具有一定的应用潜力.     

三相鼓泡塔生物反应器培养黄孢原毛平革菌合成木素过氧化物酶系

利用三相鼓泡塔反应器固定化培养黄孢原毛平革菌，可以高效地合成木素过氧化物酶系，固定化载体为聚氨酯泡沫塑料．实验表明，合成木素过氧化物酶和锰过氧化物酶的最佳通气量均是1．0vvm。在此通气量下，最大木素过氧化物酶的酶活达367U/L，最大锰过氧化物酶的酶活达4．72U／mL。在使用相同的培养基和固定化载体单位体积用量条件下，与摇瓶培养相比，酶活分别增大1倍和1．2倍．一定条件下，在三相鼓泡塔中可以进行重复间歇培养生产木素过氧化物酶，连续进行了5批培养，每批最大木素过氧化物酶的活力均在250U／L以上，最高酶活出现在第二批为480U／L，总培养时间达22d．图9参15     

隐球酵母Zwy-2-3循环利用油脂发酵废弃细胞产油

为提高资源利用效率,降低微生物油脂发酵成本,解决微生物油脂发酵中废弃酵母细胞和发酵废液处理排放的问题,研究隐球酵母(Cryptococcus podzolicus)Zwy-2-3利用栎类淀粉发酵产油情况,并探讨发酵废液和废弃酵母细胞酶解液作为氮源的循环利用.结果显示,以葡萄糖60 g/L和总氮0.18 g/L的废弃酵母细胞酶解液发酵时,循环3次其油脂产量分别达到6.79 g/L、6.66 g/L、6.72 g/L,均高于对照组;而将发酵废液回收用作废弃酵母细胞酶解的缓冲液时,其生物量、油脂产量同对照组相当;将该方法应用于栎类淀粉水解液同步糖化发酵产油脂的实验,循环3次后其生物量、油脂产量分别为13.04 g/L、7.13 g/L,比对照组提高了9.85%、10.03%,且3次循环的油脂含量较为稳定.油脂组分分析结果显示,菌株Zwy-2-3利用栎类淀粉同步糖化和废弃细胞循环酶解液发酵生产的微生物油脂不饱和脂肪酸的含量达到93%以上,与植物油组成相似.综上,酶解废弃酵母细胞可有效应用于酵母产油发酵,可为非粮淀粉生产的微生物油脂应用于生物柴油生产奠定基础.     

Optimization of fermentation process for saccharide-based fuel ethanol production by Saccharomyces cerevisiae北大核心CSCD

低成本、高产量的发酵工艺是实现工业燃料乙醇经济和环境可持续性发展的关键,而不需要重大基础设施改变或投资.为获得酿酒酵母(Saccharomyces cerevisiae)利用甘蔗汁生产燃料乙醇的最优发酵工艺,首先对发酵体系的氮源条件进行优化;其次,在单因素试验基础上,以乙醇发酵效率为响应值,通过响应面法优化了燃料乙醇生产的发酵工艺,并通过补料分批发酵技术在5 L发酵罐中进一步扩大发酵.结果表明,以1.0 g/L (NH)SO和1.0 g/L酵母提取物作为发酵氮源,乙醇发酵效率和得率比对照可分别提高4.80%、9.52%.响应面设计获得的最优发酵工艺条件为在总糖浓度150.0 g/L、酵母提取物浓度2.0 g/L、发酵时间24.5 h、pH5.0、外加(NH)SO浓度1.0 g/L时,最高乙醇发酵效率可达到91.10%.在5 L发酵罐中采用补料分批发酵获得的最终乙醇浓度达到98.92 g/L,发酵效率维持在90%左右,乙醇生产力最高达到3.81 g Lh.本研究获得了一种高效生产糖质燃料乙醇的发酵工艺,可在较短时间内获得高浓度乙醇且消耗较少氮源,结果可为进一步利用糖质原料进行高效生物炼制及高浓度乙醇工业化生产提供参考.(图6表6参30)     

谷氨酰胺转胺酶(MTG)分批发酵中温度对S.mobaraense生长及产酶影响的模型化

研究了2.5L小罐培养过程中控制温度为25℃～35℃时对细胞生长和MTG合成的影响.结果表明当控制相对较低的温度时,细胞生长的延滞期较长,当控制温度较高时,细胞生长的延滞期较短,达到最大DCW和最高MTG酶活的时间均较短;通过研究各种不同模型对细胞生长的影响得到最适合描述S.mobaraense生长与温度之间的关系方程为Schoolfield方程;通过对最大DCW和最大MTG酶活进行数学模拟,发现方程X(U)=-a     

氮源及其添加模式对钝齿棒杆菌JDN28-75合成L-精氨酸的影响

氮源是微生物过量合成L-精氨酸的重要营养因子之一,不同氮源对钝齿棒杆菌JDN28-75合成L-精氨酸的影响研究结果表明,硫酸铵为合适的氮源.不同初始硫酸铵浓度对JDN28-75产L-精氨酸的影响研究结果表明,氮源浓度过高或不足,都会使最终L-精氨酸产量有所降低.低浓度的硫酸铵虽然有利于菌体生长,但对L-精氨酸的合成明显不利,同时糖酸转化率也较低;而高浓度的硫酸铵尽管不利于细胞的生长且造成发酵结束时残糖含量过高,却有利于细胞合成L-精氨酸且实际耗糖的糖酸转化率维持在一个较高的水平.初始硫酸铵浓度为60 g/L时,对JDN28-75菌体的生长有明显的抑制作用,最终发酵液中剩余的硫酸铵也较多(大于30 g/L),但高浓度的硫酸铵是L-精氨酸合成所必需的.在上述研究结果的基础上,确定了初始硫酸铵浓度为20 g/L条件下的补氮策略,比较了4种不同的硫酸铵补加模式对产L-精氨酸的影响,结果表明,在总的硫酸铵浓度相同的情况下,采取分批、低浓度添加氮源的方式既可以有效解除发酵前期高浓度硫酸铵对菌体生长的抑制作用,又可以有效维持发酵中后期体系中菌体合成L-精氨酸所需的较高比例的氮源.最后,在5 L全自动发酵罐中采用20 g/L的初始硫酸铵浓度,连续流加25%的氨水来控制发酵体系pH及补加氮源,L-精氨酸的产量可以达到31.7 g/L,较对照组的产酸量(26.0 g/L)提高了21.9%.图4表2参11     

β-甘露聚糖酶基因在枯草芽孢杆菌中的克隆及表达

从Bacillus subtilis JNA 3-10中克隆出β-甘露聚糖酶基因成熟肽链编码序列manA1和含信号肽的β-甘露聚糖酶基因manA2,在B.subtilis 168中克隆表达,分别筛选获得高效分泌表达β-甘露聚糖酶的重组菌株BPM1001(pMA5-manA1/B.subtilis 168)和BPM1002(pMA5-manA2/B.subtilis 168),结果表明菌株BPM1002总酶活力是菌株BPM1001的9.65倍,是原始菌株的13.1倍.在基因manA2下游引入His序列克隆出β-甘露聚糖酶基因manA3,获得枯草芽孢杆菌168重组菌株BPM1003.采用Ni-NTA柱纯化重组菌株BPM1003分泌表达的β-甘露聚糖酶,并研究其酶学性质,该酶促反应的最适pH为6.5,最适温度为65℃,在37℃条件下保存一个月酶活力依然保留有77.8%.5 L发酵罐放大实验结果表明魔芋粉对于产β-甘露聚糖酶具有明显的诱导作用,酶活力最高可达2 748.82 U/mL.图9表3参19     

Comparison of the scope for growth with the growth performance of Ostrea edulis seed reared at different food concentrations in an open-flow system

Oyster (Ostrea edulis L.) seed was reared on five rations of Isochrysis galbana Parke: 10, 30, 100, 200 and 300 cells l^-1, in an open-flow system. Physiological parameters such as clearance, ingestion, absorption and respiration rates were measured, and the scope for growth (SFG) calculated from these parameters was compared with actual growth over 20 d. Actual growth was negligible at 10 cells l^-1 (daily maintenance ration=2.5% organic wt) and maximum (growth rate=13.64 d^-1) at 200 cells l^-1 (daily ration=43% organic wt), which also supported the maximum gross and net growth efficiencies (K ₁=50%, K ₂=85%). Ingestion rate was directly correlated to cell concentration up to maximum of 100 cells l^-1, but further increases failed to support higher ingestions. Absorption efficiency decreased with increasing algal concentration from 95% down to 60%. Due to the costs of growth, respiration rate significantly increased when food was added above maintenance levels; however, metabolic costs associated with feeding activity were undetectable. The scope for growth calculated from these physiological parameters agreed with the long-term growth performance, validating the physiological energetics method as a valuable tool for predicting long-term growth performance under constant environmental conditions.     

青霉素处理分离蓝藻细胞液泡

分别用 8 2 0 0u/mL ,15 30 0u/mL ,1880 0u/mL和 30 80 0u/mL的青霉素处理培养 4d的 4种蓝藻 :鱼腥藻sp .5 95 (Anabaenasp .5 95 )、念珠藻sp .96 (Nostocsp.96 )、织线藻 2 46 (Plectonemaboryanum 2 46 )和赖氏鞘丝藻〔LyngbyalargerheimiiMab (Gom)〕 ,处理时间为 2 4h ,各藻有不同程度的细胞破裂并且释放液泡 ,液泡释放率分别为 1.80 % ,2 .18% ,0 .48%和 0 .2 8% .图 4表 1参 16     

Extracellular amylase(s) production by fungi Botryodiplodia theobromae and Rhizopus oryzae grown on cassava starch residue

The fungi Botryodiplodia theobromae and Rhizopus oryzae produce extracellular amylase when grown on a liquid medium containing 2% (WN) soluble starch or cassava starch residue(CSR) (as starch equivalent), a waste generated after extraction of starch from cassava, as the sole carbon source. Using CSR as the sole carbon source, the highest amylase activity of 3.25 and 3.8 units (mg, glucose released x ml(-1) x h(-1)) were obtained in shake flask cultures during the late stationary phase of growth of B. theobromae and R. oryzae, respectively. These values were slightly lower than the values obtained using soluble starch as the carbon source. Maximum enzyme synthesis in CSR incorporated medium occurred at the growth temperature of 30 degrees C and pH 6.0. Presence of inorganic NH4+ salts like ammonium acetate and ammonium nitrate in culture medium yielded more amylase than the other nitrogen sources. Amylase(s) production in the controlled environment of a Table-Top glass Jar Fermenter (2-L capacity) was 4.8 and 5.1 units for B. theobromae and R. oryzae, respectively using CSR as the carbon substrate. It is concluded that CSR, a cheap agricultural waste obtained after starch extraction from cassava could replace soluble starch as carbon substrate for commercial production of fungal amylase(s).     

Measuring and decomposing changes in agricultural productivity, nitrogen use efficiency and cumulative exergy efficiency: Application to OECD agriculture

This paper uses an aggregate quantity space to decompose the temporal changes in nitrogen use efficiency and cumulative exergy use efficiency into changes of Moorsteen-Bjurek (MB) Total Factor Productivity (TFP) changes and changes in the aggregate nitrogen and cumulative exergy contents. Changes in productivity can be broken into technical change and changes in various efficiency measures such as technical efficiency, scale efficiency and residual mix efficiency. Changes in the aggregate nitrogen and cumulative exergy contents can be driven by changes in the quality of inputs and outputs and changes in the mixes of inputs and outputs. Also with cumulative exergy content analysis, changes in the efficiency in input production can increase or decrease the cumulative exergy transformity of agricultural production. The empirical study in 30 member countries of the Organisation for Economic Co-operation Development from 1990 to 2003 yielded some important findings. The production technology progressed but there were reductions in technical efficiency, scale efficiency and residual mix efficiency levels. This result suggests that the production frontier had shifted up but there existed lags in the responses of member countries to the technological change. Given TFP growth, improvements in nutrient use efficiency and cumulative exergy use efficiency were counteracted by reductions in the changes of the aggregate nitrogen contents ratio and aggregate cumulative exergy contents ratio. The empirical results also confirmed that different combinations of inputs and outputs as well as the quality of inputs and outputs could have more influence on the growth of nutrient and cumulative exergy use efficiency than factors that had driven productivity change.     

Autotrophic and bacterial production: Fractionation of plankton populations by differential filtration of samples from the English channel

The relationship between release of organic substances by phytoplankton and their utilization by heterotrophic bacteria has been measured by means of differential filtration in parallel Steemann Nielsen and Parsons and Strickland incubations. In Southampton Waters (UK), between March and September, the values for bacterial production measured in the above manner varied between 1 and 30%, the total primary production being taken as 100%. Even when low bacterial production occurs during the light period of incubation, a significant increase takes place during the following dark period. Thus, a close correlation between primary algal and the resultant bacterial production can be demonstrated. Quantitative data on bacterial production may be obtained from the conventional productivity experiments by simple double filtration.     

Clostridium papyrosolvens厌氧发酵产氢研究

采用分批培养研究了从高浓度厌氧产氢活性污泥中筛选的优势菌种Clostridium papyrosolvens的发酵产氢能力.结果表明:该菌有较强的高糖耐受性和耐酸性,当葡萄糖浓度为30 g/L、pH阶段性控制在4.5时,发酵44 h葡萄糖消耗率为83.7%,总产气量达到3 081.3 mL/L,最高产气率为187.5 mL L-1 h-1,氢气含量为67.5%,比产氢率达1.06 mol(H2)/mol(葡萄糖).研究中选用了廉价的发酵产氢培养基,以玉米浆为氮源,以还原铁粉作氧化还原电位控制剂,省去了牛肉膏、蛋白胨等昂贵氮源以及L-半胱氨酸、维生素、无机离子等高成本组分,显著降低了纯菌发酵的培养基成本,获得了较好的产氢效果.图5表2参23     

乙酰丙酸和前体物对Rhodobacter sphaeroides 5-氨基乙酰丙酸合成的影响

球形红细菌Rhodobacter sphaeroides光合成培养过程中(接种量2g/L),分别以不同方式加入不同浓度的乙酰丙酸(LA)、前体物(甘氨酸、琥珀酸),发现LA(30mmol/L)分3次加入,甘氨酸(60mmol/L)分2次加入,可使5-氨基乙酰丙酸合成酶(ALAS)的活性(149.1U/mg)提高,而其脱水酶(ALAD)活性(143.4U/mg)降低,使ALA产量提高到33.8mmol/L.图2参9