Effect of Cycloheximide on Development of Mitochondria in Germinating Pea Cotyledons

Polyethylene glycol (PEG) mediated transfection of Lactobacillus casei ATCC 27092 protoplasts by phage PL-1 DNA was done. The protoplasts were obtained by treatment with purified PL-1 phage N-acetylmuramidase in the presence of citrate. Optimum conditions for transfection were 50% PEG 4,000, 15 µg protamine sulfate/ml, 0.15 m sucrose, and 10 m m MgSO₄ in MR medium (pH 6.0). The extent of transfection was proportional to the amounts of DNA added, and the greatest efficiency of transfection after a 10-min incubation was about 3.3 × 10⁵ PFU/µg DNA. The eclipse period of growth of progeny phages in the transfectants was 3 hr and the average burst size was 200.     

Continuous rhamnolipid production using denitrifying Pseudomonas aeruginosa cells in hollow‐fiber bioreactor

Rhamnolipids are high‐value effective biosurfactants produced by Pseudomonas aeruginosa. Large‐scale production of rhamnolipids is still challenging especially under free‐cell aerobic conditions in which the highly foaming nature of the culture broth reduces the productivity of the process. Immobilized systems relying on oxygen as electron acceptor have been previously investigated but oxygen transfer limitation presents difficulties for continuous rhamnolipid production. A coupled system using immobilized cells and nitrate instead of oxygen as electron acceptor taking advantage of the ability of P. aeruginosa to perform nitrate respiration was evaluated. This denitrification‐based immobilized approach based on a hollow‐fiber setup eliminated the transfer limitation problems and was found suitable for continuous rhamnolipid production in a period longer than 1,500 h. It completely eliminated the foaming difficulties related to aerobic systems with a comparable specific productivity of 0.017 g/(g dry cells)‐h and allowed easy recovery of rhamnolipids from the cell‐free medium. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29: 346–351, 2013     

Post-treatment of fish canning effluents by sequential nitrification and autotrophic denitrification processes

In this research study a nitrifying/autotrophic denitrifying system was used for the post-treatment of an effluent coming from an anaerobic digester treating the wastewater produced in a fish canning industry. The nitrifying reactor achieved 100% of ammonia oxidation into nitrate. The effluent from this unit was fed to the autotrophic denitrifying reactor which treated a maximum sulphide loading rate (SLR) of 200 mg S^2?/L d with removal percentages of 100% and 30% for sulphide and nitrate, respectively. The low nitrate removal efficiency is attributed to sulphide limitations.The operational costs of this system were estimated as 0.92 €/kg N_removed, lower than those for conventional nitrification/denitrification processes. For nitrogen removal the SHARON/anammox processes is the cheapest option. However the combination of nitrification and autotrophic denitrification (using elemental sulphur) processes would present a better operational stability compared to the SHARON/anammox system.     

海洋最小含氧带氮流失过程与机制

对全球大洋氮循环的研究发现,大洋输入和输出的氮存在严重的不平衡,所固定的氮中有相当一部分被还原为N₂或N₂O从大洋中流失,而海洋最小含氧带(OMZ)被认为是发生氮流失的最主要区域,通过反硝化作用和厌氧氨氧化作用,固定氮在OMZ海区内损失量可达40～450 Tg·a^-1.对不同海区OMZ内固定氮损失的两种主要作用总结发现,异养反硝化作用在热带太平洋东部、阿拉伯海的OMZ内以及海洋沉积物内占有显著优势,在智利、秘鲁沿岸海域及阿拉伯海域也已发现自养反硝化作用的存在;而在黑海、非洲西南部的本格拉上升流、智利北部沿岸等地,厌氧氨氧化作用强烈,且其在陆架区的作用强度和面积要大于大洋区.OMZ氮的流失除受氮流失过程自身影响外,固氮作用、硝化作用、硝酸盐异化还原作用等都可能对OMZ海区内氮收支不平衡造成影响.其中固氮作用的影响最不能忽视,其在全球OMZ内固定的氮的总量可达15～40 Tg·a^-1,是对OMZ氮流失量的重要补充.区分反硝化作用和厌氧氨氧化作用对OMZ氮流失的相对贡献,明确氮流失的另一产物N₂O的形成机制和定量评估方法是当前OMZ氮流失研究中存在的最主要问题.本文针对存在问题提出了相应的研究设想,以期为海洋最小含氧带的研究提供参考.     

Microbial Community Analysis and Effects of Fe(II)/Mn(II) Ratio on Denitrification in the Mixotrophic Biological Reactor

In this study, the denitrification performance of the mixotrophic biological reactor was investigated under varying Fe(II)/Mn(II) molar ratio conditions. Results indicate that the optimal nitrate removal ratio occurred at an Fe(II)/Mn(II) molar ratio of 9:1, pH of 7, with an HRT of 10?h. When the reactor was performing under optimal conditions, the nitrate removal reached 100.00% at a rate of 0.116?mmol·L^?1·h^?1. The proportion of oxidized Fe(II) and Mn(II) reached 99.29% and 21.88%, respectively. High-throughput sequencing results show that Pseudomonas was the dominant species in the mixotrophic biological reactor. Furthermore, the relative abundance of Pseudomonas and denitrification performance was significantly influenced by variation in the Fe(II)/Mn(II) molar ratio.     

Treatment of Biogas Produced in Anaerobic Reactors for Domestic Wastewater: Odor Control and Energy/Resource Recovery

Anaerobic municipal wastewater treatment in developing countries has important potential applications considering their huge lack of sanitation infrastructure and their advantageous climatic conditions. At present, among the obstacles that this technology encounters, odor control and biogas utilization or disposal should be properly addressed. In fact, in most of small and medium size anaerobic municipal treatment plants, biogas is just vented, transferring pollution from water to the atmosphere, contributing to the greenhouse gas inventory. Anaerobic municipal sewage treatment should not be considered as an energy producer, unless a significant wastewater flow is treated. In these cases, more than half of the methane produced is dissolved and lost in the effluent so yield values will be between 0.08 and 0.18 N m³ CH₄/kg COD removed. Diverse technologies for odor control and biogas cleaning are currently available. High pollutant concentrations may be treated with physical-chemical methods, while biological processes are used mainly for odor control to prevent negative impacts on the treatment facilities or nearby areas. In general terms, biogas treatment is accomplished by physico-chemical methods, scrubbing being extensively used for H₂S and CO₂ removal. However, dilution (venting) has been an extensive disposal method in some small- and medium-size anaerobic plants treating municipal wastewaters. Simple technologies, such as biofilters, should be developed in order to avoid this practice, matching with the simplicity of anaerobic wastewater treatment processes. In any case, design and specification of biogas handling system should consider safety standards. Resource recovery can be added to anaerobic sewage treatment if methane is used as electron donor for denitrification and nitrogen control purposes. This would result in a reduction of operational cost and in an additional advantage for the application of anaerobic sewage treatment. In developing countries, biogas conversion to energy may apply for the clean development mechanism (CDM) of the Kyoto Protocol. This would increase the economic feasibility of the project through the marketing of certified emission reductions (CERs).     

Zn(II)对好氧反硝化菌Acinetobacter sp. JR-142的代谢活性影响

【目的】研究不同Zn(Ⅱ)浓度对好氧反硝化菌Acinetobacter sp.JR-142生理活性,尤其是反硝化代谢特性的影响。【方法】筛选一株好氧反硝化菌,优化了最佳活性条件;分析了不同Zn(Ⅱ)浓度对生长曲线和反硝化效率的影响以及对细胞形态的影响;明晰了不同Zn(Ⅱ)浓度条件下,细胞特征活性酶-硝酸盐还原酶和亚硝酸盐还原酶的活性变化情况,分析了不同活性同关键酶的编码基因napA和nirS的相对表达量之间的规律。【结果】获得一株具有好氧反硝化功能的菌株,命名为JR-142,经鉴定为不动杆菌Acinetobacter sp.。在以琥珀酸钠为碳源,C/N为6,pH为7.0,温度30℃,转速为180 r/min的条件下,好氧反硝化活性最高。结果表明当Zn(Ⅱ)浓度为3.25 mg/L时,对菌株的生长及好氧反硝化速率有促进作用;当Zn(Ⅱ)浓度为52 mg/L以上浓度时,菌株的生长及反硝化速率均受到抑制。酶活及关键基因napA、nirS的定量分析结果显示,对照组及JR+0.05处理组的硝酸盐还原酶NR、亚硝酸盐还原酶NiR活性均高于JR+0.8处理组,在24 h时,JR+0.05 Zn(Ⅱ)处理组中,细胞的关键好氧反硝化基因napA及nirS的相对表达量显著高于对照组,这进一步说明3.25 mg/L Zn(Ⅱ)可以促进好氧反硝化过程,而在24 h及32 h时对照组及JR+0.05处理组的基因相对表达量远高于JR+0.8处理组,也说明52 mg/L Zn(Ⅱ)则会对反应产生抑制。【结论】探究并系统分析了不同Zn(Ⅱ)浓度对不动杆菌Acinetobacter sp.JR-142生长繁殖以及和在重金属锌离子存在的情况下影响好氧反硝化生理活性的影响,为后续硝酸盐-重金属复合污染废水的生物处理技术提供了数据指导。     

耐高浓度氨氮的异养硝化好氧反硝化菌株U1的鉴定及其脱氮特性

【背景】城市垃圾渗滤液是一种成分复杂的有机废水,含氮量高,如果未经处理直接排放到环境中会造成严重的环境污染。【目的】筛选可以耐受垃圾渗滤液中高浓度氨氮并高效去除污水中氮素的异养硝化好氧反硝化菌株,为解决垃圾渗滤液的氮素污染提供功能菌株。【方法】从垃圾渗滤液中筛选分离能耐受高氨氮浓度的菌株,通过测定各菌株的脱氮能力,筛选到一株脱氮能力最强的菌株,命名为U1,通过测定16S rRNA基因序列和生理生化特性确定该菌株为铜绿假单胞菌。进一步研究了菌株U1在不同初始氨氮浓度、碳源、转速、初始pH、碳氮比等单因素变量下的脱氮能力,并结合L₉（3⁴）正交试验研究了菌株U1的最佳脱氮条件。【结果】分离出一株铜绿假单胞菌并命名为U1。该菌株的最优脱氮条件为:初始氨氮浓度为1 000 mg/L,红糖和柠檬酸三钠的混合碳源,pH 6.0,C/N为10,转速为130 r/min,菌株U1的最大总氮去除率为64.37%,最大氨氮去除率为76.73%。对于总氮和氨氮含量分别是2 345 mg/L和1 473.8 mg/L的垃圾渗滤液,菌株U1最大总氮去除率为27.86%...     

羟胺氧化还原酶在生物脱氮中的研究进展

羟胺氧化还原酶(hydroxylamine oxidoreductase,HAO)属于多血红素蛋白酶家族,每个单体由7个电子转移血红素和1个催化血红素组成。HAO既可分别催化羟胺和肼的氧化反应,也可催化羟胺、一氧化氮及亚硝酸盐的还原反应。不同硝化细菌中,HAO的最适温度、p H、底物、产物特异性及酶抑制剂等存在差异。作为生物硝化过程的关键酶,HAO在提升生物脱氮速率及清除硝化中间产物(羟胺)对生物的毒害方面发挥重要作用。本文系统综述了HAO在脱氮微生物中的分布、蛋白结构、表达调控及其活性等,总结其在不同硝化细菌中的生物化学特性,最后对HAO进一步的研究方向进行展望,有助于深入理解生物脱氮过程和微生物体内羟胺代谢的机理,为优化废水处理工艺提供新的指导。     

Role of heterotrophic nitrifiers and aerobic denitrifiers in simultaneous nitrification and denitrification process: a nonconventional nitrogen removal pathway in wastewater treatment

Bacterial species capable of performing both nitrification and denitrification in a single vessel under similar conditions have gained significance in the wastewater treatment scenario considering their unique character of performing the above reactions under heterotrophic and aerobic conditions respectively. Such a novel strategy often referred to as simultaneous nitrification and denitrification (SND) has a tremendous potential in dealing with various wastewaters having low C : N content, considering that the process needs very little or no external carbon source and oxygen supply thus adding to its cost-effective and environmentally friendly nature. Though like other micro-organisms, heterotrophic nitrifiers and aerobic denitrifiers convert inorganic or organic nitrogen-containing substances into harmless dinitrogen gas in the wastewater, their ecophysiological role in the global nitrogen cycle is still not fully understood. Attempts to highlight the role played by the heterotrophic nitrifiers and aerobic denitrifiers in dealing with nitrogen pollution under various environmental operating conditions will help in developing a mechanistic understanding of the SND process to address the issues faced by the traditional methods of aerobic autotrophic nitrification–anaerobic heterotrophic denitrification.