Itaconic acid production from xylose in repeated-batch and continuous bioreactors

Summary Itaconic acid production from xylose by immobilized Aspergillus terreus TKK 200-5-2 mycelia was optimized both in repeated shake-flask fermentations and in continuous column bioreactors using statistical experimental design and empirical modelling. Using continuous 9-1 scale air-lift bioreactors, a pH of 2.5, aeration rate of 0.6 v/v per minute and residence time of 160 h gave the highest itaconic acid concentration. In air-lift bioreactors a cubic carrier size of 0.5 cm gave a 3.3-fold higher product concentration than 1-cm cubes. Packed-bed column reactors had a higher production rate than air-lift reactors. Offprint requests to: H. Kautola     

Evaluation of culture medium for nisin production in a repeated-batch biofilm reactor

In this study, a biofilm reactor with plastic composite support (PCS), made by high-temperature extrusion of agricultural products and polypropylene, was evaluated for nisin production using L. lactis strain NIZO 22186. The high-biomass density of the biofilm reactor was found to contribute to a significantly shorter lag time of nisin production relative to a suspended-cell reactor. In comparison to glucose (579 IU/mL), sucrose significantly increased the nisin production rate by 1.4-fold (1100 IU/mL). However, results revealed that high levels of sucrose (8% w/v) had a suppressing effect on nisin production and a stimulating effect on lactic acid production. A high concentration of MgSO4.7H2O at 0.04% (w/v) was found to reduce the nisin production, while concentrations of KH2PO4 of up to 3% (w/v) did not have any significant effect on growth or nisin production. The best of the tested complex media for nisin production using the PCS biofilm reactor consisted of 4% (w/v) sucrose, 0.02% (w/v) MgSO4.7H2O, and 0.1% (w/v) KH2PO4. Nisin production rate in the biofilm reactor was significantly increased by 3.8-fold (2208 IU/mL) when using the best complex medium tested.     

Enhanced anthocyanin production by repeated-batch culture of strawberry cells with medium shift

Repeated-batch cultures of strawberry cells (Fragaria ananassa cv. Shikinari) subjected to four medium-shift procedures (constant LS medium, constant B5 medium, alternation between LS and B5 starting from LS and alternation between LS and B5 starting from B5) were investigated for the enhanced anthocyanin productivity. To determine the optimum period for repeated batch cultures, two medium-shift periods of 9 and 14 days were studied, which represent the end of the exponential growth phase and the stationary phase. By comparison with the corresponding batch cultures, higher anthocyanin productivity was achieved for all the repeated-batch cultures at a 9-day medium-shift period. The average anthocyanin productivity was enhanced 1.7- and 1.76-fold by repeated-batch cultures in constant LS and constant B5 medium at a 9-day shift period for 45 days, respectively. No further improvement was observed when the medium was alternated between LS (the growth medium) and B5 (the production medium). Anthocyanin production was unstable at a 14-day shift period regardless of the medium-shift procedures. The results show that it is feasible to improve anthocyanin production by a repeated-batch culture of strawberry cells.     

Optimization of L-(+)-lactic acid production by ring and disc plastic composite supports through repeated-batch biofilm fermentation.

Four customized bioreactors, three with plastic composite supports (PCS) and one with suspended cells (control), were operated as repeated-batch fermentors for 66 days at pH 5 and 37 degrees C. The working volume of each customized reactor was 600 ml, and each reactor's medium was changed every 2 to 5 days for 17 batches. The performance of PCS bioreactors in long-term biofilm repeated-batch fermentation was compared with that of suspended-cell bioreactors in this research. PCS could stimulate biofilm formation, supply nutrients to attached and free suspended cells, and reduce medium channelling for lactic acid production. Compared with conventional repeated-batch fermentation, PCS bioreactors shortened the lag time by threefold (control, 11 h; PCS, 3.5 h) and sixfold (control, 9 h; PCS, 1.5 h) at yeast extract concentrations of 0.4 and 0.8% (wt/vol), respectively. They also increased the lactic acid productivity of Lactobacillus casei subsp. rhamnosus (ATCC 11443) by 40 to 70% and shortened the total fermentation time by 28 to 61% at all yeast extract concentrations. The fastest productivity of the PCS bioreactors (4.26 g/liter/h) was at a starting glucose concentration of 10% (wt/vol), whereas that of the control (2.78 g/liter/h) was at 8% (wt/vol). PCS biofilm lactic acid fermentation can drastically improve the fermentation rate with reduced complex-nutrient addition.     

基于细菌体系生产双链RNA的条件优化

化学杀虫剂是农业害虫防治的主要手段,然而农业害虫已对化学杀虫剂产生了抗药性。RNA农药的应用将是减少使用化学杀虫剂的一种途径。RNA农药具有专一、高效、易降解和对环境友好等优点而受到了关注,但在靶标分子、靶标分子的双链RNA（dsRNA）生产工艺和应用制剂等方面仍需进一步研究。本研究以褐飞虱Nilaparvata lugens蛋白激酶B基因的dsRNA（dsNlAKT）为例,对利用细菌体系生产dsRNA的方法进行了探究。将NlAKT构建进L4440载体后,将其转化到缺乏核酸酶（RNase Ⅲ）的大肠杆菌Escherichia coli HT115（DE3）中,进行了dsRNA生产条件的测试。结果表明：（1）当异丙基-β-D-硫代半乳糖苷（IPTG）工作浓度为0.1 mM或0.5 mM时dsRNA的产量没有明显变化,而当其工作浓度增加至1 mM时dsRNA产量明显减少;（2）在IPTG诱导时间为2~8 h范围内,添加IPTG后诱导6 h获得的dsRNA产量最多;（3）在实验室常规提取RNA方法中,增加低剂量溶菌酶预处理这一步骤可增加提取产物中dsRNA的含量。试验结果证明了采用工作浓度为0.1 mM的IPTG诱导6 h的生产条件,并在提取过程中增加溶菌酶的预处理步骤有助于获得较高的dsRNA含量。研究结果为RNA农药的生产条件提供了实验依据。     

High-yield production of citric acid by Yarrowia lipolytica on glycerol in repeated-batch bioreactors

An acetate negative mutant of Yarrowia lipolytica Wratislavia AWG7 was found to be suitable for the production of high amounts of citric acid in long-term repeated-batch cultures. When 40% of fresh replaced medium was fed, this strain produced 154 g l⁻¹, on average, which corresponded to a 0.78 g g⁻¹ yield and a productivity of 1.05 g l⁻¹ h⁻¹. The activity of the culture remained stable for more than 1,650 h, i.e., 16 cycles of the repeated-batch bioreactors.     

Porous alumina beads for immobilization of lactic acid bacteria and its application for repeated-batch fermentation in soy sauce production

Porous alumina beads with controlled pores were prepared for the immobilization of lactic acid bacteria to improve soy sauce productivity, and the alumina support with the highest lactic acid productivity was used for repeated-batch fermentation. Immobilized lactic acid bacteria could be used 5 times in repeated-batch fermentation, where higher productivities were obtained than that in conventional fermentation. The lactic acid fermentation process was mathematically modeled from the material balance and the rate equation. The simulated results agreed with the experimental ones.     

Batch culture and repeated-batch culture of Cunninghamella bainieri 2A1 for lipid production as a comparative study

This research was performed based on a comparative study on fungal lipid production by a locally isolated strain Cunninghamella bainieri 2A1 in batch culture and repeated-batch culture using a nitrogen-limited medium. Lipid production in the batch culture was conducted to study the effect of different agitation rates on the simultaneous consumption of ammonium tartrate and glucose sources. Lipid production in the repeated-batch culture was studied by considering the effect of harvesting time and harvesting volume of the culture broth on the lipid accumulation. The batch cultivation was carried out in a 500 ml Erlenmeyer flask containing 200 ml of the fresh nitrogen-limited medium. Microbial culture was incubated at 30 °C under different agitation rates of 120, 180 and 250 rpm for 120 h. The repeated-batch culture was performed at three harvesting times of 12, 24 and 48 h using four harvesting cultures of 60%, 70%, 80% and 90%. Experimental results revealed that nitrogen source (ammonium tartrate) was fully utilized by C. bainieri 2A1 within 24 h in all agitation rates tested. It was also observed that a high amount of glucose in culture medium was consumed by C. bainieri 2A1 at 250 rpm agitation speed during the batch fermentation. Similar results showed that the highest lipid concentration of 2.96 g/L was obtained at an agitation rate of 250 rpm at 120 h cultivation time with the maximum lipid productivity of 7.0 × 10⁻² mg/ml/h. On the other hand, experimental results showed that the highest lipid concentration produced in the repeated-batch culture was 3.30 g/L at the first cycle of 48 h harvesting time using 70% harvesting volume, while 0.23 g/L gamma-linolenic acid (GLA) was produced at the last cycle of 48 h harvesting time using 80% harvesting volume.     

Retamycin production by immobilized cells of Streptomyces olindensis ICB20 in repeated-batch cultures

Repeated-batch cultures of Ca-alginate immobilized cells of Streptomyces olindensis ICB20 for retamycin production were carried out in two different bioreactors: a basket-type stirred tank reactor (BSTR) and a bubble column reactor (BCR). Higher average values of retamycin content (R) and productivity (P_R) were achieved in the BSTR cultures (about 1.7 AU and 0.031 AU h⁻¹, respectively) compared to those obtained in the BCR cultures (about 0.6 AU and 0.012 AU h⁻¹, respectively). The BCR, on the other hand, presented significantly better operation stability than the BSTR, which makes the former much more promising regarding future industrial applications.     

RNA病毒基因组和转录复制多样性的分子基础

自然界中RNA病毒的种类和数量比DNA病毒多得多,根据基因组类型,RNA病毒可分为多种类型,许多研究者认为,存在于古细菌Myxobacteria中,仅仅有一个逆转录酶基因的反转子（Retron)可能是所有病毒的祖先,进化的模式如下,反转子→反座子→反转录转座子→反转录病毒→副反转录病毒→DNA病毒,RNA病毒转录。／复制在很多特征上与DNA病毒迥然不同,依赖于RNA的RNA聚合酶是RNA病转录／复制的主要催化剂,RNA病毒基因组转录和复制都从3'端poly(A)或类tRNA结构或其他结构起始,内部终止是转录,通读到5'末端终止是复制,RNA病毒的模板有正链病毒（RNA模板,负链病毒RNA模板和全长正负链反基因组RNA模板,RNA模板的选择调控机制非常复杂,目前知之甚少,选择模板,RNA聚合酶与转录因子结合形成复制体是两种主要的调控方法,另外,5'UTR和3'UTR也可以调控RNA病毒的转录。