中试厌氧氨氧化反应器的运行性能及其过程动力学特性

研究了上流式中试厌氧氨氧化(anaerobic ammonium oxidation,ANAMMOX)反应器在环境温度下的运行性能及其过程动力学特性.基质浓度试验表明,中试厌氧氨氧化反应器可在进水亚硝酸盐浓度为(380.4±18.3)mg.L-1稳定运行,继续提升至(480.5±21.9)mg.L-1时,反应器性能恶化.在水力停留时间(hydraulic retention time,HRT)试验中,HRT可缩短至3.43 h,反应器容积基质氮去除速率可达3.45 kg.(m3.d)-1.长期运行中,温度对中试厌氧氨氧化反应器的性能影响较大.采用改进型的Stover-Kincannon模型可较好地模拟非抑制状态下中试厌氧氨氧化反应器在不同温度范围下的行为.获得的Stover-Kincannon模型动力学参数及其出水总基质浓度预测公式和总基质去除率预测公式,可用于指导中试厌氧氨氧化反应器的实际操作.     

黑藻吸附Cu2+机制研究

生物吸附法是一种经济有效的去除废水中有害重金属离子的方法.以黑藻(Hydrilla verticillata)干样为生物吸附材料,研究了黑藻对水体中Cu<'2+>等温吸附的基本特征,并通过测定吸附前后溶液离子浓度变化以及pH值、基团屏蔽对Cu<'2+>吸附的影响,结合红外光谱技术,从静电吸附作用、离子交换作用、基团作用...     

潮汐流人工湿地低温下 NH4+ -N去除模型的比较和优化

针对目前人工湿地在低温条件下脱氮效能降低的问题,本研究对每天3个运行周期的潮汐流人工湿地在低温条件下对NH4+ -N的处理效能进行研究,同时利用表观动力学模型、多元参数回归模型及Monod机制模型对NH4+-N的去除过程进行拟合.结果显示,在平均水温为9～13℃条件下,每天3个运行周期的潮汐流人工湿地对NH4+-N有良...     

连续流膜生物反应器中好氧颗粒污泥的形成及机制探讨

为了探讨好氧颗粒污泥在连续流膜生物反应器(MBR)中的形成过程和机制,采用连续流试验的方法,研究了好氧颗粒污泥形成过程中膜反应器内污染物的去除效果和好氧颗粒污泥特性的变化,并对连续流MBR中好氧颗粒污泥的形成机制进行了探讨.结果显示,连续流MBR中好氧颗粒污泥的形成增强了MBR的运行稳定性和抗冲击能力.废水中微生物抑制...     

基于格网的太湖生态环境质量空间评价

将GIS格网空间分析技术应用于太湖生态环境综合评价,实现了全湖范围内多因素的综合评价,揭示太湖生态环境状况的空间分布规律。首先将太湖分为800个格网单元,在2002~2003年实测样点的水体、底泥、水生生物特征数据基础上,通过空间插值获得全部单元模拟值,然后进行格网叠加计算,通过层次分析法得出各单元综合评价值,将太湖分为好、较好、中等、较差、差5个等级区,生成太湖生态环境空间综合评价图。结果显示,评价结果与太湖实际情况基本相符,太湖生态环境质量基本上由东南向西北逐渐降低,中等以下地区占全部湖区的一半以上,整体状况偏差。     

春季太湖光量子产额空间分布的特征分析

基于2009年4月28日、5月4日、5月5日及5月6日在太湖梅梁湾的栈桥头、直湖港的河口区、太湖中心及胥口湾中心测定的初级生产力及水下光场数据,计算了各测点的藻类光量子产额和P-I曲线,并分析了其空间差异的特征.太湖栈桥头的P-I曲线呈现出明显的光抑制现象;在胥口湾中心和直湖港河口,P-I曲线呈现出弱的光抑制现象;而在太湖中心区域,P-I曲线只达到了光饱和状态,并未出现光抑制现象.单位叶绿素a的最大光量子产额的大小顺序为太湖中心区域、梅梁湾的栈桥头、直湖港的河口区及胥口湾的湖心区.     

臭氧处理循环冷却水节能减排效益分析

文章基于臭氧(O3)处理法处理循环冷却水因可以同时达到阻垢脱垢、缓蚀、杀菌等多重功能,其在国外已得到广泛应用,同时国内也逐步普及应用的环境下,结合国内外长期的工程实践经验,从节水、节能、减排和公共卫生效益四个方面,详细分析了臭氧处理循环冷却水所带来的巨大经济效益、社会效益和环境效益。     

富营养化水体中黑水团的吸收及反射特性分析

对黑水团水体光学特性进行研究,是利用遥感技术监测和评估黑水团事件的前提.针对2015年7月在太湖发生的黑水团现象,采集了太湖黑水团区(区域一)、蓝藻水华区(区域二)、清水区(区域三)共36个水样,对这3个区域的水体遥感反射率以及吸收特性进行对比分析.结果表明:1区域一水体的总颗粒物、色素颗粒物和非色素颗粒物吸收系数比区域二、区域三高出1~2倍,在400~500 nm之间,区域一CDOM吸收系数相比另外两个区域的水体高出2倍左右.导致黑水团区域水体具有很低的遥感反射率,被人眼感知时呈现为黑色;2黑水团区域水体M值低于滇池、巢湖和太湖的M值变化范围,说明黑水团中CDOM的腐殖酸含量较高.此外,叶绿素a浓度与CDOM在350 nm处吸收系数之间具有很好的相关性,表明蓝藻的降解可能是黑水团中CDOM的一个主要来源;3在380 nm之后,黑水团区域的水体总吸收以色素颗粒物占主导,但在短波350~380 nm处,CDOM对总吸收的贡献率高于色素颗粒物和非色素颗粒物.     

Enhanced struvite recovery from wastewater using a novel cone-inserted fluidized bed reactor

The feasibility of struvite recovery at low （12.5 mg/L） and high （120 mg[L） phosphorus concentrations was studied by constructing a novel fluidized bed reactor with cones （FBRwc） and without cones （FBRwoc）. The crystallization process was continuously operated for 133 days under different hydraulic retention times （HRT = 1-10 hr）, pH （7.5-10）, and molar ratios of Mg/P （0.75-1.75）, N/P （1-10） and Ca/Mg （0-2）. The optimum operating conditions of HRT, pH, Mg/P and N/P molar ratios were found to be 2 hr, 9, 1.25, and 7.5, respectively. Under these optimum conditions, the phosphorus precipitation efficiencies of FBRwc were 93% for low and 98% for high phosphorus influent; however, the efficiencies were 78% and 81% for FBRwoc, respectively. Due to crystal losses at each junction （17%-31%）, the crystal recovery efficiency of FBRwoc was relatively low （47%-65%） for both influent concentrations. However, the losses were minimal in FBRwc, which showed 75% and 92% crystal recovery for low and high phosphorus concentrations, respectively. At low calcium concentration, crystal chemical analysis showed the product to be pure struvite （〉 99%）. The scanning electron microscope and X-ray diffraction results further confirmed that the crystal recovered from FBRwc contained pure struvite, which could be considered a high quality fertilizer. Except HRT, all parameters （pH, Mg/P, N/P and Ca/Mg） were found to be influencing factors for FBRwc performance. Overall, inserting cones in each part of the reactor played a significant role in enhancing struvite recovery from a wide range of phosphorus-containing wastewater.     

Arsenic removal from groundwater by acclimated sludge under autohydrogenotrophic conditions

Arsenic in the environment is attracting increasing attention due to its chronic health effects. Although arsenite(As(III)) is generally more mobile and more toxic than arsenate(As(V)), reducing As(V) to As(III) may still be a means for decontamination, because As(III) can be removed from solution by precipitation with sulfide or by adsorption or complexation with other metal sulfides. The performance of As(V) bio-reduction under autohydrogenotrophic conditions was investigated with batch experiments. The results showed that As(V) reduction was a biochemical process while both acclimated sludge and hydrogen were essential. Most of the reduced arsenic remained in a soluble form, although 20% was removed with no addition of sulfate, while 82% was removed when sulfate was reduced to sulfide. The results demonstrated that the reduced arsenic was re-sequestered in the precipitates, probably as arsenic sulfides. Kinetic analysis showed that pseudo first-order kinetics described the bio-reduction process better than pseudo second-order. In particular, the influences of pH and temperature on As(V) reduction by acclimated sludge under autohydrogenotrophic conditions and total soluble As removal were examined. The reduction process was highly sensitive to both pH and temperature, with the optimum ranges of pH 6.5–7.0 and 30–40°C respectively. Furthermore, Arrhenius modeling results for the temperature effect indicated that the As(V) reduction trend was systematic. Total soluble As removal was consistent with the trend of As(V) reduction.