影响生物脱氮除磷的因素

对生物脱氮除磷的基本原理作了简要分析，因其脱氮和除磷受多种因素影响，择其主要影响因素进行综述，以便为工程应用提供依据。     

好氧颗粒污泥实现同步硝化反硝化

采用人工配制的模拟生活污水，通过对运行条件的调控，在序批式反应器(SBR)中培养出了高活性的好氧颗粒污泥，颗粒污泥浓度达到4．55g/L以上，SVI值在32.5左右，反应器对于COD、NH3—N的去除率分别在83.6％—92.8％和82.3％—98.5％之间。实验结果表明：由于好氧颗粒污泥的存在，SBR反应器内发生了同步硝化反硝化(SND)反应，而不是通常所认为的顺序式硝化反硝化(SQND)反应。     

新型废水生物脱氮的微生物学研究进展

生物脱氮是含氮废水处理公认的最佳处理方式,随着对生物脱氮微生物学原理研究的不断深入,许多新的生物脱氮特殊菌株或菌群及微生物转化机制不断被发现.本文在传统生物脱氮过程机理上,结合最近国内外生物脱氮的新发现,就短程硝化反硝化、同时硝化反硝化、厌氧氨氧化的微生物学原理进行了阐述.图1表2参23     

三种载体上生物膜硝化作用动力学初步研究

通过测定水中COD、：NH4^ —N、NO2^-—N及NO3^-—N的浓度变化，研究了淹没式废水处理装置中沸石、活性炭和沙粒3种载体上硝化作用生物膜的动力学过程和反硝化作用。结果表明，3种载体上生物膜降解有机物(以COD表示)的过程可用一级动力学方程描述，反应速率常数分别为：沙粒0．0848h^-1、活性炭0．1187h^-1、沸石0．1334h^-1。3种载体上生物膜去除氨态氮的过程则可用零级动力学方程描述，反应速率常数分别为：沙粒-0．7743h^-1、活性炭-0．9886h^-1、沸石-1．0714h^-1．附着于沙上的生物膜去除亚硝酸盐氮的过程也可用零级动力学方程描述，反应速率常数为-0．6057h^-1，水中硝酸盐氮浓度较高时，载体沸石和活性炭上可能附着生长反硝化菌。图5表2参15。     

生物快滤池深度处理城市污水的性能及pH值变化规律

采用生物快滤池对城市污水厂二级出水进行深度处理的试验表明,生物快滤池对进水水质变化有很大的适应性,除卫生学指标外,其它指标出水绝大部分时间可满足生活杂用水水质标准(CJ25.1-89)中的洗车标准。随着进水水质的不同,生物快滤池中生化反应类型也随之变化,相应地滤池出水pH值也有不同的变化规律。可以通过生物快滤池进出水pH值的变化情况来判断滤池内生化反应类型和COD或氨氮指标的去除效果。     

双氰胺在四川3种主要土壤上的硝化抑制作用

采用室内培养试验方法,在不同浓度双氰胺(DCD)处理条件下,对四川3种主要土壤(紫色土、黄壤、灰潮土)的N2O释放量,NH4+-N及NO3--N含量动态变化进行了研究.结果表明,DCD对3种土壤N2O释放及土壤NO3--N含量有明显抑制作用,随DCD浓度增加,其抑制效果越显著.DCD同时能推迟NO3--N含量达到高峰,使土壤NH4+-N含量在较长时间保持相对较高水平,提高氮肥利用率,减少氮素流失.DCD在3种土壤上硝化抑制效果存在差异,表现为紫色土＞灰潮土＞黄壤.同时提出DCD在3种土壤上的适宜添加量,紫色土上为普通碳铵施入量的0.5%,黄壤和灰潮土上为0.3%.     

天津市东郊污水处理厂生物脱氮工艺设计

天津市东郊污水处理厂是新建投产的一座大型城市污水处理厂，其设计处理能力为４０００００ｍ￣３／ｄ。该厂引进了国外先进设备和技术，６００００ｍ￣３／ｄ污水采用前置缺氧脱氮的Ａ／Ｏ工艺进行了深化处理。本文全面论述了Ａ／Ｏ工艺曝气他的设计，并就设计参数取值、池型设计、进出水形式，回流方式和缺氧区与好氧区的容积比等进行了分析探讨。     

Mechanism studies on nitrogen removal when treating ammonium-rich leachate by sequencing batch biofilm reactor

The nitrogen removal mechanism was studied and analyzed when treating the ammonium-rich landfill leachate by a set of sequencing batch biofilm reactors (SBBRs), which was designed independently. At the liquid temperature of (32 ± 0.4)°C, and after a 58-days domestication period and a 33-days stabilization period, the efficiency of ammonium removal in the SBBR went up to 95%. Highly frequent intermittent aeration suppressed the activity of nitratebacteria, and also eliminated the influence on the activity of anaerobic ammonium oxidation (ANAMMOX) bacteria and nitritebacteria. This influence was caused by the accumulation of nitrous acid and the undulation of pH. During the aeration stage, the concentration of dissolved oxygen was controlled at 1.2–1.4 mg/L. The nitritebacteria became dominant and nitrite accumulated gradually. During the anoxic stage, along with the concentration debasement of the dissolved oxygen, ANAMMOX bacteria became dominant; then, the nitrite that was accumulated in the aeration stage was wiped off with ammonium simultaneously. Translated from Acta Scientiae Circumstantiae, 2006, 26(1): 55–60 [译自: 环境科学学报]     

Factors affecting simultaneous nitrification and denitrification in an SBBR treating domestic wastewater

An aerobic sequencing batch biofilm reactor (SBBR) packed with Bauer rings was used to treat real domestic wastewater for simultaneous nitrification and denitrification. The SBBR is advantageous for creating an anoxic condition, and the biofilm can absorb and store carbon for good nitrification and denitrification. An average concentration of oxygen ranging from 0.8 to 4.0 mg/L was proved very efficient for nitrification and denitrification. Volumetric loads of TN dropped dramatically and effluent TN concentration increased quickly when the concentration of average dissolved oxygen was more than 4.0 mg/L. The efficiency of simultaneous nitrification and denitrification (SND) increased with increasing thickness of the biofilm. The influent concentration hardly affected the TN removal efficiency, but the effluent TN increased with increasing influent concentration. It is suggested that a subsequence for denitrification be added or influent amount be decreased to meet effluent quality requirements. At optimum operating parameters, the TN removal efficiency of 74%–82% could be achieved. Translated from Acta Scientiae Circumstantiae, 2006, 26(5): 728–733 [译自: 环境科学学报]     

低碳氮比废水生物脱氮新技术

传统的除氨氮工艺需要消耗较多的氧气,且对于低碳氮(C/N)比的废水,需外加有机碳源才能进行反硝化。详细阐述了同步硝化反硝化、短程硝化反硝化、厌氧氨氧化和全程自养脱氮等生物脱氮新技术的特点,应用前景以及存在的问题。提出了今后的研究方向。