5-酮基-D-葡萄糖酸发酵生产的工艺条件优化

葡萄糖酸氧化杆菌可将葡萄糖转化为5-酮基-D-葡萄糖酸(5-KGA),而5-KGA是重要食品添加剂L(+)-酒石酸的合成前体。为提高5-KGA产量及其对葡萄糖的转化率,对5-KGA发酵生产的工艺条件进行优化。在摇瓶水平最适的培养基和培养条件下,5-KGA最高产量为19.7 g/L,较优化前提高43.8%。在5 L发酵罐上控制恒定pH值5.5、溶氧浓度15%条件下,5-KGA产量达到46.0 g/L,较摇瓶最高产量提高1.3倍,应用葡萄糖流加工艺,5-KGA最高产量达到75.5 g/L,转化率超过70%,与已见报道的最高水平相比提高了32.0%,为实现微生物发酵生产5-KGA、进而合成L(+)-酒石酸的工业化提供了切实有效的途径。     

Microbial production of 2,3-butanediol from Jerusalem artichoke tubers by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

2,3-Butanediol is one of the promising bulk chemicals with wide applications. Its fermentative production has attracted great interest due to the high end concentration. However, large-scale production of 2,3-butanediol requires low-cost substrate and efficient fermentation process. In the present study, 2,3-butanediol production by Klebsiella pneumoniae from Jerusalem artichoke tubers was successfully performed, and various technologies, including separate hydrolysis and fermentation (SHF) and simultaneous saccharification and fermentation (SSF), were investigated. The concentration of target products reached 81.59 and 91.63 g/l, respectively after 40 h in batch and fed-batch SSF processes. Comparing with fed-batch SHF, the fed-batch SSF provided 30.3% higher concentration and 83.2% higher productivity of target products. The results showed that Jerusalem artichoke tuber is a favorable substrate for 2,3-butanediol production, and the application of fed-batch SSF for its conversion can result in a more cost-effective process.     

玉米雄穗性状遗传结构与形成分子机制*

玉米为雌雄同株异花植物,其雄穗着生于植株顶部,雌穗腋生。雄穗一方面需产生足量花粉以保证雌穗授粉结实,另一方面由于对下部叶片的遮蔽作用和自身营养需求,其生长发育会同时影响叶片光合作用效率和能量分配,因此优化雄穗结构是提高玉米产量的重要措施之一。玉米雄穗性状包括雄穗分枝数、雄穗分枝长度、雄穗主轴长度、雄穗分枝总长度、雄穗分枝角度等,均为多基因控制的数量性状。自20世纪90年代,研究者开始利用数量性状位点(quantitative trait locus,QTL)定位方法解析玉米雄穗性状遗传结构;随着玉米自交系B73等参考基因组释放,以及DNA微阵列、基因组重测序等高通量基因分型技术的日益成熟,全基因组关联分析(genome-wide association study, GWAS)成为数量性状遗传研究的主流方法,目前已鉴定出大量玉米雄穗性状遗传位点。通过总结雄穗性状遗传定位研究结果,构建一致性图谱并挖掘定位热点区间,有助于进一步了解雄穗性状遗传结构特征及指导雄穗性状候选基因克隆。此外,通过对调控雄穗发育的已知基因进行功能分类,可为解析玉米雄穗发育的遗传网络和调控通路提供理论支撑。     

Effects of lanthanum on rumen fermentation, urinary excretion of purine derivatives and digestibility in steers

The objective of this study was to evaluate the effects of LaCl₃ supplementation on rumen fermentation, urinary excretion of purine derivatives and feed digestibility in the total tract of steers. Eight ruminally cannulated Simmental steers (420 ± 20 kg) were used in a replicated 4 × 4 Latin square experiment. The treatments were control (without LaCl₃); La-low; La-medium and La-high with 450, 900 and 1800 mg LaCl₃ per steer per day, respectively. Diet consisted of 600 g/kg corn stover and 400 g/kg concentrate (dry matter [DM] basis). Dry matter intake (averaged 9 kg/day) was restricted to a maximum of 90% of ad libitum intake. Ruminal pH (range of 6.59–6.42) was quadratically (P<0.04) changed, whereas total volatile fatty acids (VFA) concentration (range of 74.16–88.61 mM) was linearly (P<0.01) and quadratically (P<0.01) increased with increasing La supplementation. Ratio of acetate to propionate decreased linearly (P<0.01) from 3.28 to 1.79 as La supplementation increased due to the increased in propionate production. In situ ruminal neutral detergent fibre (aNDF) degradation of corn stover was improved but the crude protein (CP) degradability of soybean meal was decreased with increasing La supplementation. Urinary excretion of purine derivatives was quadratically (P<0.01) changed with altering La supplementation (75.5, 81.0, 82.4 and 70.6 mmol/day for control, low-, medium- and high-LaCl₃ supplementation, respectively). Similarly, digestibilities of organic matter, aNDF and CP in the total tract were also linearly and quadratically increased with increasing La supplementation. The present results indicate that supplementation of diet with LaCl₃ improved rumen fermentation and feed digestion in beef cattle. It was suggested that the La stimulated the digestive microorganisms or enzymes in a dose-dependent manner. In the experimental conditions of this trial, the optimum La dose was about 900 mg LaCl₃ per steer per day.     

塔拉单宁水解酶产生条件的研究

微生物通过发酵产酶可以将植物单宁降解成小分子酚类化合物或其衍生物,但培养条件对其产酶影响很大。论文采用固态培养法,对黑曲霉产生塔拉单宁水解酶的条件进行了研究。结果表明,当培养液中塔拉单宁浓度为75 g/L、葡萄糖浓度为3 g/L、(NH4)2SO4浓度为0.2 g/L2、50 mL锥形瓶装液量为25 mL、惰性载体用量为5.6%(w/v)、起始pH为5.5、接种量为12%(v/v)、30℃培养72 h时,该黑曲霉产生的塔拉单宁水解酶活力可达到44.29 U/mL,是其自然条件下酶活力(24.09 U/mL)的1.84倍;没食子酸产率达到79.3%。研究结果对于揭示塔拉单宁生物降解的机理具有一定的参考价值。     

海洋真菌Xylaria sp.(No.2508)生产xyloketal B的发酵优化

对海洋真菌Xylariasp．（No．2508）生产xyloketa]B的摇瓶发酵过程进行了初步优化。结果表明,Xylariasp．（No．2508）在培养120h时xyloketalB产量最高,当培养168h后菌体进入衰亡期且xyloketalB迅速降解,因此Xylariasp．（No．2508）生产xyloketalB的最适发酵周期为120h;Xylariasp．（No．2508）合成xyloketalB的过程及用乙酸乙酯萃取xyloketalB的过程对pH非常敏感,其中最适xyloketalB生产的发酵液初始pH为5．7,利用乙酸乙酯萃取xyloketalB时的发酵液最适pH为3。0;最适接种量为10％（v／v）;接种前发酵液中加入10g／L的大孔树脂XAD-16可以降低某些代谢产物对xyloketalB合成的抑制作用,从而使产量提高2倍左右,而菌体进入稳定期以后加入大孔树脂XAD-16对产物产量没有影响。     

川西北泡沙参种群根系生长动态及其与环境因素关系研究

对川西北地区泡沙参种群根系生物量累积和形态发育过程及其与环境因素的关系进行了研究.结果表明,泡沙参种群根系生物量累积一般规律符合Logistic增长过程.较高的泡沙参根系生物量累积和形态发育时期可以持续到15～17年生以后,根系采收直径应在1.7cm以上.动物啃食、人为采挖、土壤、气候等环境条件与不同海拔各种群的根系生物量累积等有着密切联系,中海拔地区(2800～3300m)人为干扰少,土壤和水热条件适宜,根系生物量和形态发育达到较高水平,适合高产栽培.而低海拔和高海拔地区的不利环境条件限制了泡沙参根系生长.在进行野生资源保护利用以及人工栽培泡沙参时应充分考虑环境因素,努力减少放牧、采挖等人为破坏,有条件的地区应实行分区禁牧、禁采挖,为泡沙参种群恢复和药材品质提高创造条件.     

Changes of Saccharomyces cerevisiae cell membrane components and promotion to ethanol tolerance during the bioethanol fermentation

During bioethanol fermentation process, Saccharomyces cerevisiae cell membrane might provide main protection to tolerate accumulated ethanol, and S. cerevisiae cells might also remodel their membrane compositions or structure to try to adapt to or tolerate the ethanol stress. However, the exact changes and roles of S. cerevisiae cell membrane components during bioethanol fermentation still remains poorly understood. This study was performed to clarify changes and roles of S. cerevisiae cell membrane components during bioethanol fermentation. Both cell diameter and membrane integrity decreased as fermentation time lasting. Moreover, compared with cells at lag phase, cells at exponential and stationary phases had higher contents of ergosterol and oleic acid (C_18:1) but lower levels of hexadecanoic (C_16:0) and palmitelaidic (C_16:1) acids. Contents of most detected phospholipids presented an increase tendency during fermentation process. Increased contents of oleic acid and phospholipids containing unsaturated fatty acids might indicate enhanced cell membrane fluidity. Compared with cells at lag phase, cells at exponential and stationary phases had higher expressions of ACC1 and HFA1. However, OLE1 expression underwent an evident increase at exponential phase but a decrease at following stationary phase. These results indicated that during bioethanol fermentation process, yeast cells remodeled membrane and more changeable cell membrane contributed to acquiring higher ethanol tolerance of S. cerevisiae cells. These results highlighted our knowledge about relationship between the variation of cell membrane structure and compositions and ethanol tolerance, and would contribute to a better understanding of bioethanol fermentation process and construction of industrial ethanologenic strains with higher ethanol tolerance.     

Process of simultaneous hydrogen sulfide removal from biogas and nitrogen removal from swine wastewater

The feasibility of a new flowchart describing simultaneous hydrogen sulfide removal from biogas and nitrogen removal from wastewater was investigated. It took 30 days for the reactor inoculated with aerobic sludge to attain a removal rate of 60% for H₂S and NO_x–N simultaneously. It took 34 and 48 days to attain the same removal rate for the reactor without inoculated sludge and the reactor inoculated with anaerobic sludge respectively. The reactor without inoculated sludge still operated successfully, despite requiring a slightly longer startup time. The packing material was capable of enhancing the removal efficiency of reactors. Based on the concentration of NO_x–N and H₂S in the effluent, the loading rate and the ability of the system to resist shock loading, the performance of the reactor filled with hollow plastic balls was greater than that of the reactor filled with elastic packing and the reactor filled with Pall rings.