Electrochemical disinfection using the gas di usion electrode system

A study on the electrochemical disinfection with H2O2 generated at the gas diffusion electrode(GDE) from active carbon/polytetrafluoroethylene was performed in a non-membrane cell.The effects of Pt load and the pore-forming agent content in GDE,and operating conditions were investigated.The experimental results showed that nearly all bacterial cultures inoculated in the secondary effluent from wastewater treatment plant could be inactivated within 30 min at a current density of 10 mA/cm 2 .The disinfection ...     

双铝电极电絮凝处理高含氟地下水的影响因素及动力学分析

为探求电絮凝处理高含氟地下水工艺技术参数及其除氟动力学,采用双铝电极电絮凝装置处理人工模拟高含氟地下水,研究了双铝电絮凝除氟过程及其除氟动力学模型,分别考察了电流密度、pH、极板间距及初始氟浓度对电絮凝除氟过程影响。结果表明,电絮凝除氟过程符合一级反应动力学模型,理论所需除氟时间取决于初始氟浓度和除氟动力学常数,而除氟动力学常数受电流密度、极板间距和初始氟浓度影响;当电流密度为300 A·m~(-3),pH为6.0～7.0,极间距为10 mm时,双铝电絮凝除氟能效最高,氟离子去除率为89.56%,能耗为0.157 8 kWh·g~(-1);但较高的初始氟浓度容易使铝氟比下降,导致除氟效果下降,不利于除氟过程。以上结果可为电絮凝处理高含氟地下水工程化应用和除氟反应器开发提供参考。     

电除尘器电源交流分量对PM_（2.5）等细微颗粒物除尘效率的影响

除尘器对颗粒物的除尘效率与颗粒物的荷电量密切相关,PM2.5等细小颗粒物由于其荷电量不足而导致其吸收效率较低,对环境造成危害。为了增加粒子的荷电量,以粒子荷电原理为理论依据,从离子电流密度和通过电凝并扩大尘粒中位径2个方面研究了电除尘电源中交流电压分量对PM2.5等细小颗粒物荷电特性的影响,得出了电除尘器电源中交流电压分量可从以上2个方面提高装置对PM2.5等微小颗粒物的荷电量,且频率越高,幅值越大,荷电效果越好,从而可以提高装置对细小颗粒物的除尘效率。     

电化学氧化法去除超高盐榨菜废水中的氨氮

采用电化学氧化法去除超高盐榨菜废水中的氨氮,阳极为Ti/RuO2-TiO2-IrO2-SnO2网状电极,阴极为网状钛电极,考察了电流密度、电解时间、极板间距、初始pH以及极水比对氨氮去除率的影响,并分析了电流密度对氨氮能耗和阳极效率的影响。结果表明,在初始氨氮浓度为472.73 mg/L,电流密度为156 mA/cm2,极板间距为1.5 cm,极水比为0.8dm2/L,原水pH为4.3～5.0时,电解30 min和60 min时氨氮的去除率分别为89.75%和99.94%,电解30 min时,氨氮能耗最低为96 kWh/kg,阳极效率最高为8.47 g/(h.m2.A)。     

Oxidation behavior of ammonium in a 3-dimensional biofilm-electrode reactor

Excess nitrogenous compounds are detrimental to natural water systems and to human health. To completely realize autohy- drogenotrophic nitrogen removal, a novel 3-dimensional biofilm-electrode reactor was designed. Titanium was electroplated with ruthenium and used as the anode. Activated carbon fiber felt was used as the cathode. The reactor was separated into two chambers by a permeable membrane. The cathode chamber was filled with granular graphite and glass beads. The cathode and cathode chamber were inhabited with domesticated biofilm. In the absence of organic substances, a nitrogen removal efficiency of up to 91% was achieved at DO levels of 3.42 ± 0.37 mg/L when the applied current density was only 0.02 mA/cm^2. The oxidation of ammonium in biofilmelectrode reactors was also investigated. It was found that ammonium could be oxidized not only on the anode but also on particle electrodes in the cathode chamber of the biofilm-electrode reactor. Oxidation rates of ammonium and nitrogen removal efficiency were found to be affected by the electric current loading on the biofilm-electrode reactor. The kinetic model of ammonium at different electric currents was analyzed by a first-order reaction kinetics equation. The regression analysis implied that when the current density was less than 0.02 mA/cm^2, ammonium removal was positively correlated to the current density. However, when the current density was more than 0.02 mA/cm^2, the electric current became a limiting factor for the oxidation rate of ammonium and nitrogen removal efficiency.     

脉冲电流对电化学除氯的影响

目的 探究不同电流密度下,直流和脉冲2种电流模式对钢筋混凝土电化学除氯的影响,降低钢筋渗氢量,减小通电后阴极产生的氢气使钢筋发生氢脆的风险,提高除氯效率,改善电化学除氯效率的均匀性。方法 通过在电流密度为2、3、4 A/m²的条件下,对混凝土进行直流和脉冲电流电化学修复,测定处理后的钢筋的释氢电流,计算释氢总电量,来表示钢筋渗氢量,对比处理后强电流区和弱电流区混凝土的氯离子含量,分析2种方式除氯效率的均匀性,同时用扫描电子显微镜观察电化学除氯前后混凝土的微观结构。结果 计算得到不同通电电流密度下钢筋的释氢总电量和除氯效率,脉冲电流的释氢总电量比直流电流低约20%,而除氯效率提高了约10%。结论 增加电流密度可以提高除氯效率,但是会增加钢筋发生氢脆的风险。相较于直流电流,脉冲电流电化学修复可以降低钢筋渗氢量,显著提高弱电流区的除氯效率,从而改善除氯效率的均匀性。     

芒刺-板式电除尘器收尘极板电流密度分布规律研究

在芒刺-板式电除尘器中,板电流密度分布越均匀,越有利于除尘效率提高.因此,知道收尘极板电流密度分布对电除尘器的电极结构设计是重要的.然而,由于处于芒刺正下方的峰值电流不易确定,导致现有的电流密度分布式很难用于实际工程计算.另外,这些计算式不满足高斯通量定理.要使芒刺-板式电除尘器收尘极板电流密度分布满足高斯电通量定理,电流密度分布规律应服从某种特定的分布函数.通过对Warburg单根芒刺-板式电极极板电流密度分布模型的变量分析,发现芒刺-板式电除尘器收尘极板电流密度分布恰是自由度n=4的t分布.根据电流密度的分布特征,建立了由总电流确定极板电流密度的理论计算式.由于总电流很容易通过实测得到,因此,所建立的极板电流密度t分布模型更具实用性.比较研究表明,该理论式与其他研究者的实验结果有很好的一致性.     

纳米SiO2改性聚偏氟乙烯离子交换膜对单组分电解质溶液的脱盐性能研究

对纳米SiO2改性聚偏氟乙烯(SiO2/PVDF)离子交换膜电渗析处理单组分电解质溶液进行了试验研究。结果表明,在不同操作条件下,SiO2/PVDF离子交换膜的极限电流密度和脱盐率均大于未改性聚偏氟乙烯(PVDF)离子交换膜。SiO2/PVDF离子交换膜的极限电流密度随着淡水流量和电解质浓度的增加而增加;随着电流强度的增加,SiO2/PVDF离子交换膜的脱盐率也相应增加;随着淡水流量增加,脱盐率会逐渐降低。为使SiO2/PVDF离子交换膜用于电渗析过程获得良好的脱盐效果和节约能量,NaCl质量浓度为500mg/L时电流密度应控制在1.17mA/cm2。     

库尔勒碱性土壤环境中交流干扰对X100管线钢阴保电位的影响

管道作为运输能源的重要工具,其安全问题一直是人们重点关注的对象,随着X100管线在石油天然气运输中的应用越来越多,交流干扰一直被认为是危害埋地钢质管道安全的重要隐患。本文采用电化学测试技术和浸泡试验研究了在碱性土壤溶液中被不同阴保电位(-0.75 V、-0.95 V、-1.1 V、-1.2 V)保护的X100管线钢电位受交流干扰电流密度(0～500A/m²)的影响。结果表明在碱性的库尔勒土壤模拟液中,给体系施加交流干扰后,X100管线钢平均阴保电位均会发生正向偏移,瞬时电位变化与干扰电流一致,呈现周期性震荡,说明交流干扰会减弱阴保系统的保护能力,但偏移量与阴保电位数值无明显的相关性。     

掺硼金刚石膜电极处理医院废水的研究

通过研究自制电解槽,利用掺硼金刚石膜电极(BDD)对医疗废水进行消毒实验研究.实验研究了电流密度、消毒时间及Cl-浓度对消毒效果的影响.实验结果表明:电流密度越大,消毒效果越好;消毒接触时间越长,消毒效果越好;Cl-浓度对消毒效果影响显著,医疗废水C1-质量浓度达到200 mg/L以上,消毒接触时间≥9s,出水即可满足GB 18466-2005《医疗机构水污染物排放标准》粪大肠茵群数均不得超过500 MPN/L.