Some properties of a sequencing batch reactor for treatment of wastewater containing thiocyanate compounds

Thiocyanate (SCN) compounds in photo-processing wastewater (PPWW) could be treated by an SBR system without any release of thiocyanate to the atmosphere during the aeration step. An SCN loading greater than 84 g m(-3)d(-1) showed negative effects on the growth of bio-sludge and removal efficiencies of the system. The acclimatization period of the system was increased with an increase in SCN concentration or loading. The COD, BOD(5), TKN, and SCN removal efficiencies were 96.0 +/- 1.6%, 72 +/- 2%, 49 +/- 5%, and 82 +/- 3%, respectively, under an SCN loading of up to 84 g m(-3)d(-1). The removal efficiency of the system was repressed by SCN due to the repressed growth rate of nitrification bacteria. However, the removal efficiency could be increased with an increase in HRT or a decrease in SCN loading. Also, increases in HRT or decreases in SCN loading led to increased sludge age or solid retention time (SRT) and decreased the sludge volume index (SVI) value. The SRT and SVI of the system with synthetic wastewater containing 840 mg l(-1) SCN under an HRT of 3 days (SCN loading of 280 g m(-3)d(-1)) were 3.9 +/- 0.7 days and 65 +/- 4 ml g(-1), respectively, while they were 11.2+/-0.8 days and 55 +/- 6 ml g(-1), respectively under an HRT of 10 days (SCN loading of 84 g m(-3)d(-1)).     

A/O-MBBR工艺处理生活污水性能及菌群结构

采用设计规模为100m³/d的一体化缺/好氧-移动床生物膜反应器(A/O-MBBR)处理实际生活污水,通过265d的中试研究考察了该工艺在多因素扰动下的除碳和脱氮性能,并对不同运行阶段微生物群落结构的动态变化进行了研究.结果表明,一体化A/O-MBBR系统具有良好的COD去除效果和脱氮性能.当好氧池溶解氧(DO)浓度和进水碳氮比(COD/N)分别为2.5~3.5mg/L和(7.9±2.0)时,COD、NH₄⁺-N和TN去除率分别达到(93.3±5.4)%、(99.1±0.6)%和(67.9±10.5)%.Proteobacteria、Bacteroidetes和Chloroflexi在不同运行时期均有较高的相对丰度,保证了有机物的高效去除.A/O-MBBR系统脱氮功能菌在运行初期主要分布于活性污泥中,且相对丰度较低.长期运行后,生物膜与活性污泥中均同时检出大量硝化菌和反硝化菌.其中,相对丰度最高的硝化菌为Nitrospira,主要分布于生物膜上(19.48%~28.05%).反硝化菌则以Thauera、Terrimonas和Dokdonella等为主.     

小冲杆试验测定重离子辐照A508-3钢的硬化和脆化

目的采用小冲杆测试方法测量高能重离子辐照反应堆压力容器A508-3钢的辐照硬化和脆化特性,为工况条件下反应堆压力容器寿命预测提供实验依据。方法采用兰州重离子加速器提供的高能C^(6+)离子通过减能装置在290℃条件下开展A508-3钢辐照实验,并在样品表面形成一定厚度、准均匀分布的离位损伤层。通过开展不同辐照剂量辐照样品的小冲杆测试,得到不同辐照剂量A508-3钢的小冲杆载荷-位移曲线。通过对小冲杆测试得到的载荷-位移曲线的分析,测定不同辐照剂量样品的辐照硬化和脆化特性。结果压力容器A508-3钢辐照样品的硬化和脆化随着辐照剂量的增加逐渐增强,0.15 dpa以前呈线性增长,而后缓慢增大,约0.2 dpa时达到饱和趋势。结论通过小冲杆测试可以得到离子辐照样品的硬化和脆化行为,A508-3钢辐照硬化和脆化行为具有一致的变化趋势。     

基于平面压入技术研究焊接接头单轴应力-应变关系

目的 获取异种金属焊接接头母材和热影响区局部拉伸应力-应变关系。方法 对压水堆机组蒸汽发生器接管安全端异种金属焊接接头(20MND 5-INCONEL 52-Z2 CND 18.12控氮)进行研究,通过金相检验和显微硬度测试,研究DMWJ母材、热影响区、焊缝熔合线位置的金相组织和维氏硬度分布。采用等直圆棒拉伸试验获得DMWJ低合金钢(20MND 5)母材的应力-应变关系,采用基于能量等效理论的平面压入技术获得DMWJ低合金钢母材、热影响区和焊缝局部材料应力-应变关系。结果 DMWJ材料组织、力学性能不均匀,等直圆棒拉伸试验得到的低合金钢母材拉伸应力-应变关系与平面压入技术测得结果较为吻合。结论 基于能量等效理论的平面压入技术可精确测得DMWJ低合金钢母材、热影响区和焊缝局部材料应力-应变关系,对压水堆核电站DMWJ在役检测及结构完整性评价具有重要意义。     

多种复合材料固定化反应器的对比研究

选用活性炭、海砺壳2种材料作为固定化载体,对改良型UASB系统去除COD的性能进行研究,结果表明选择既高柱又循环且增加载体填充体积的系统,可有效去除高浓度有机废水的COD,但当填充载体过高时,循环系统难以实现,并存在憋气的可能。     

“混凝沉淀+纳米零价铁”处理印刷电路板生产废水中试研究

提出一种新纳米零价铁反应器(Nanoscale Zero-Valent Iron Reactor,简称NIR)及"混凝沉淀+纳米零价铁"处理工艺,通过实际生产废水进行中试,考察和研究该工艺和NIR技术处理江苏省某市印刷电路板(Printed Circuit Board,简称PCB)工业园区废水的效果。结果表明,此工艺对PCB生产废水中Cu、TP及COD Cr去除率分别可达到97.3%、73.7%、26%,其中Cu处理效果最佳;XRD结果表明,纳米零价铁(Nanoscale Zero-Valent Iron,nZVI)与PCB生产废水反应后含有γ-Fe2O3、Fe3O4、γ-FeOOH、CuO、Cu2O、Cu0等产物。"混凝沉淀+纳米零价铁"工艺处理废水时具有处理效果好、工艺耐冲击性能好、产泥量小、不易造成二次污染等优点。     

Steady performance of a zero valent iron packed anaerobic reactor for azo dye wastewater treatment under variable influent quality

Zero valent iron (ZVI) is expected to help create an enhanced anaerobic environment that might improve the performance of anaerobic treatment. Based on this idea, a novel ZVI packed upflow anaerobic sludge blanket (ZVI-UASB) reactor was developed to treat azo dye wastewater with variable influent quality. The results showed that the reactor was less influenced by increases of Reactive Brilliant Red X-3B concentration from 50 to 1000 mg/L and chemical oxygen demand (COD) from 1000 to 7000 mg/L in the feed than a reference UASB reactor without the ZVI. The ZVI decreased oxidation-reduction potential in the reactor by about 80 mV. Iron ion dissolution from the ZVI could buffer acidity in the reactor, the amount of which was related to the COD concentration. Fluorescence in situ hybridization test showed the abundance of methanogens in the sludge of the ZVI-UASB reactor was significantly greater than that of the reference one. Denaturing gradient gel electrophoresis showed that the ZVI increased the diversity of microbial strains responsible for high efficiency.     

运用三维荧光光谱解析高温厌氧产氢反应过程对温度变化的响应

为建立反应器运行状态的荧光光谱快速监测方法,应用三维荧光光谱表征了高温厌氧反应器的出水,采用平行因子分析方法分析后得到3种荧光组分——蛋白质、辅酶NADH和核黄素,并获得它们的激发发射光谱图及相对浓度.结果表明,当温度从50 ℃上升到60 ℃的过程中,3种荧光物质的相对浓度均呈现相应的变化,它们与反应器的运行参数呈现明显相关性.进一步研究表明,核黄素是高温厌氧产氢反应中的特有荧光物质,采用标准加入法和二阶校正方法可以测定其实际浓度,出水中核黄素浓度变化范围为0.04~0.13 mg·L^-1.该研究为厌氧产氢反应器的运行监控提供了理论基础.     

厌氧序批式反应器预处理垃圾渗滤液的碳平衡研究

为初步了解垃圾渗滤液中有机物降解过程的物质和能量转化,对渗滤液实际处理工程提供借鉴,在最优工艺参数条件下,分别用处于中温(35±1)℃和常温状态的厌氧序批式反应器(ASBR)对垃圾渗滤液进行预处理。通过对反应器内的液相、气相和固相碳素进行全面的分析测定,结果表明:中温(常温)条件下,整个反应周期内约有86.4%(77.6%)的碳进入气相,约有1.7%(1.4%)的碳进入固相,其余约11.7%(22.3%)的碳仍存于液相中;其中,进入气相部分的碳有77.6%(71.3%)以甲烷形式存在,8.8%(4.7%)以二氧化碳形式存在,这说明ASBR预处理垃圾渗滤液过程中产生的甲烷资源化利用潜力较大。另外,反应器在中温状态下较常温状态处理效果更佳。     

Biological sulfate removal from acrylic fiber manufacturing wastewater using a two-stage UASB reactor

A two-stage UASB reactor was employed to remove sulfate from acrylic fiber manufacturing wastewater. Mesophilic operation (35±0.5℃) was performed with hydraulic retention time (HRT) varied between 28 and 40 hr. Mixed liquor suspended solids (MLSS) in the reactor was maintained about 8000 mg/L. The results indicated that sulfate removal was enhanced with increasing the ratio of COD/SO₄^2-. At low COD/SO₄^2-, the growth of the sulfate-reducing bacteria (SRB) was carbon-limited. The optimal sulfate removal efficiencies were 75% when the HRT was no less than 38 hr. Sulfidogenesis mainly happened in the sulfate-reducing stage, while methanogenesis in the methane-producing stage. Microbes in sulfate-reducing stage performed granulation better than that in methane-producing stage. Higher extracellular polymeric substances (EPS) content in sulfate-reducing stage helped to adhere and connect the flocculent sludge particles together. SRB accounted for about 31% both in sulfate-reducing stage and methane-producing stage at COD/SO₄^2- ratio of 0.5, while it dropped dramatically from 34% in sulfate-reducing stage to 10% in methane-producing stage corresponding to the COD/SO₄^2- ratio of 4.7. SRB and MPA were predominant in sulfate-reducing stage and methane-producing stage respectively.