电絮凝处理脱硫废水中重金属及动力学模型

采用电絮凝法处理脱硫废水中重金属离子,研究去除过程的影响因素及动力学模型,并对电絮凝产物进行分析。考察电絮凝时间、电流密度、废水pH值、曝气量对电絮凝法处理重金属离子效果的影响。结果表明,电絮凝时间40min,电流密度4mA/cm2,废水pH=7,曝气量0.4m3/h时,四种金属去除率达90%。电絮凝产物为铁的多核羟基络合物,且去除过程具有一级动力学反应特征。     

絮凝-漂白粉催化氧化处理印染废水

采用絮凝-漂白粉催化氧化法,筛选出硫酸镁催化剂,提高难生化处理的印染废水对色度、COD的去除效果。实验结果表明,对COD_(Cr) 592 mg/L、色度625倍、pH 9.82、SS 150 mg/L的某印染废水,当废水p H为6时,投加Al_2(SO_4)_3·18H_2O 400 mg/L、聚丙烯酰胺(PAM)2 mg/L,催化剂硫酸镁80 mg/L,有效氯30%的漂白粉1.0 g/L,CODCr最终去除率达到88.2%,色度去除率98.4%,浊度去除率86.6%,出水pH为6,达到国家二级排放标准。催化氧化的脱色速率提高近一倍,结果对印染废水的处理研究和实际应用具有一定价值。     

PFSS絮凝-膜分离法处理炼油废水

采用PFSS絮凝-膜分离法处理炼油废水.通过对PAC、PFS和PFSS的除油、CODcr、SS性能比较,确定了PFSS为较好的絮凝剂,探讨了絮凝剂用量、絮凝时间对絮凝效果的影响.通过对膜材料的分析,确定了聚氯乙烯-聚丙烯腈膜对炼油废水有较好的处理效果,探讨了进料流量、操作压力、温度对膜通量的影响.结果表明:当PFSS用量为50-70mg/L、反应时间为8min、进料流量为60L·h-1、操作压力为1.6Mpa、温度为40℃时,通过絮凝沉降、膜分离处理过程,炼油废水中的油、CODcr、SS的去除率分别达到98%、95%、93%以上.出水水质达到国家一级排放标准.     

电絮凝-O3联合工艺处理页岩气压裂采出水

通过研究比较不同处理工艺对页岩气压裂采出水的效果,设计出电絮凝-O_3联合处理采出水的工艺。以化学需氧量(COD)、总悬浮物(TSS)为指标,讨论电絮凝-O_3联合工艺处理页岩气压裂采出水过程中pH、电流密度、电极间距、电解时间以及O_3通气量的影响。结果表明,当pH=8. 0、电流密度为1250A/m~2、极板间距为2cm、电解时间6min、O_3通气量为40L/h时,COD去除率为98. 3%,TSS的去除率为95. 9%,经过电絮凝-O_3联合处理后的采出水的色度、浊度、oil及NH_4-N等污染指标都达到了国家排放标准。     

丙烯酸基水凝胶处理重金属废水的研究进展

重金属废水因其对环境污染严重、危害人类健康而越来越引起人们的重视。丙烯酸基高分子水凝胶由于含有多种功能基团和大量的活性吸附位点,在重金属吸附方面发挥了重要作用。本文主要综述了丙烯酸基高分子水凝胶在重金属废水处理方面的研究进展,总结和归纳了其制备方法和分类等,分析了聚丙烯酸基高分子水凝胶作为吸附剂在重金属废水处理方面存在的问题,并对其后续应用和研究进行了展望。     

“氧化·脱色·絮凝”协同法处理含吡啶酮废水

根据染料中间体吡啶-2-酮生产废水的特点,提出了利用“氧化、脱色和絮凝”三位一体的物化方法处理这种废水;探究了搅拌速度、絮凝反应时间、pH值、药剂用量、废水浓度和温度对COD去除率和脱色率的影响,得出了最佳工艺条件.研究结果表明,在常温下,两性聚丙烯酰胺NDPAM用量35 mg/L,氧化交联剂PDO用量0.55 mL/L,pH=5.7,搅拌速度80 r/m in,絮凝时间为15 m in和静止时间为30 m in的条件下,COD的去除率和脱色率均达到98%,处理后的废水达到了可生化的指标范围.并对处理成本和絮凝动力学机理进行了探讨.     

壳聚糖对印染废水的絮凝作用和脱色效果

壳聚糖可作为阳离子型和阴离子型絮凝剂 ,对无机化合物、极性有机化合物、蛋白质等产生絮凝作用[1] .壳聚糖无毒 ,对动、植物无害 ,用其作为絮凝剂的污泥可作肥料 .在环境保护方面具有广阔的应用前景 .本文报道直接用壳聚糖对印染厂废水处理的絮凝和脱色效果研究 .壳聚糖自制 ,广东省佛山市上朗针织漂染厂印染废水 ,上海分析仪器厂 72 2光栅分光光度计 ,可调多联搅拌器 .结果与讨论絮凝效果的测定参照美国材料与试验协会 ( ASTM)有关标准[2 ,3 ] .取印染废液 1 0 0 0 m L,快速搅拌约 1 min,降低转速至约 2 0～ 60 r/min进行慢速搅拌 ,记录…     

辐射诱导合成水凝胶及其处理重金属废水的研究进展*

水凝胶是一种经适度交联而具有三维网络结构的新型功能高分子材料。制备水凝胶因操作简单、无须添加交联剂和引发剂等优点而受到关注。传统的处理重金属废水的方法或成本较高,或效率低,利用水凝胶处理重金属废水成为一种新的颇具潜力的方法。本文综述了辐射法制备水凝胶及其在重金属吸附去除方面的研究进展包括材料的制备、改性、去除重金属性能等方面的研究进展,并指出了水凝胶去除重金属的发展前景和今后的研究方向。     

New trends in removing heavy metals from industrial wastewater

Innovative processes for treating industrial wastewater containing heavy metals often involve technologies for reduction of toxicity in order to meet technology-based treatment standards. This article reviews the recent developments and technical applicability of various treatments for the removal of heavy metals from industrial wastewater. A particular focus is given to innovative physico-chemical removal processes such as; adsorption on new adsorbents, membrane filtration, electrodialysis, and photocatalysis. Their advantages and limitations in application are evaluated. The main operating conditions such as pH and treatment performance are presented. Published studies of 94 cited references (1999–2008) are reviewed.It is evident from survey that new adsorbents and membrane filtration are the most frequently studied and widely applied for the treatment of metal-contaminated wastewater. However, in the near future, the most promising methods to treat such complex systems will be the photocatalytic ones which consume cheap photons from the UV-near visible region. They induce both degradation of organic pollutants and recovery of metals in one-pot systems. On the other hand, from the conventional processes, lime precipitation has been found as one of the most effective means to treat inorganic effluent with a metal concentration of >1000 mg/L. It is important to note that the overall treatment cost of metal-contaminated water varies, depending on the process employed and the local conditions. In general, the technical applicability, plant simplicity and cost-effectiveness are the key factors in selecting the most suitable treatment for inorganic effluent     

Use of a glass residue in the removal of heavy metals from wastewater

The extraction of silica from powdered glass cullet with an aqueous solution of sodium hydroxide has been proposed as an alternative to glass recycling aimed to the low temperature production of sodium silicates. The unextracted residue obtained after a counter current two-step extractive process at approximately 100 degrees C and room pressure is mainly made of calcium and sodium silicate and shows high porosity and a large surface area. We thought that it could be active as an agent for the removal of heavy metals from wastewater. In this paper the capacity of the unextracted residue of removing six metal ions (i.e., Cu2+, Ni2+, Zn2+, Cd2+, Pb2+ e Cr3+) was studied in a stirred batch reactor. The data obtained demonstrate that the removal of metal ions from wastewater is achieved with high capacity in a short time and their concentration is lowered under the legal limits without any appreciable influence from changes of physical and chemical conditions. Sodium and calcium ions take the place of heavy metals in water while pH keeps almost neutral. The exchange mechanism was identified.     

Encapsulated zerovalent iron/nickel-fly ash zeolite foam for treating industrial wastewater contaminated by heavy metals

Pollution due to heavy metal discharge into water systems is a global issue that has attracted growing attention in recent years. Thus, we had synthesized encapsulated zerovalent iron/nickel-fly ash zeolite foam (SA-ZFN foam) by freeze-drying method for the simultaneous removal of various heavy metals from industrial wastewater. The resulting SA-ZFN foam’s structural characterization was performed using advanced instrumental techniques. In addition, factors influencing heavy metal removal were discussed including the pH, reaction time, temperature, initial metal concentration, and their competition with each other; and the adsorption mechanism was investigated. The Langmuir maximum capacity of as-prepared foam was 75.76, 49.78, 44.89, and 7.31 mg/g for Cu(II), As(V), Hg(II), and Cr(VI), respectively. Furthermore, isotherms and kinetic data revealed that the rate-limiting step is monolayer adsorption on a homogeneous surface.Furthermore, thermodynamic studies indicated that ΔG° decreases as temperature rises, i.e. the adsorption process becomes more favorable at higher temperatures. The results suggest the no significant decrease of adsorption capacity on each cycle was observed by re-sustaining over three times in the first two cycles. When applied to real industrial wastewater, the SA-ZFN foam reduced the residual heavy metals to acceptable levels. Continuous column experiment also suggested that the SA-ZFN foam could simultaneously remove the heavy metals from aqueous solutions. From these results, it is demonstrated that the SA-ZFN foam is a promising, efficient, and economical material for wastewater treatment.     

Thermodynamic parameters for adsorption equilibrium of heavy metals and dyes from wastewater with low-cost adsorbents

This note revisits the literature evaluating the thermodynamic parameters of adsorption equilibrium uptakes of heavy metals and dyes from water and wastewater streams using low-cost adsorbents derived from agricultural waste, industrial wastes, inorganic particulates, or some natural products. We highlighted the possible flaws in some adsorption studies when their thermodynamic parameters were assessed, since compensation effects during enthalpy and entropy evaluation were possibly overlooked.     

贵阳污灌区菜地土壤团聚体中有机碳和重金属的含量特征及相关性分析

以贵阳某污灌区菜地土壤为研究对象,分别采用微波消解-电感耦合等离子体质谱(ICP-MS)法和水合热重铬酸钾氧化分光光度法分析不同粒径土壤团聚体中重金属和有机碳的含量特征,并对有机碳和重金属的相关性进行分析。结果表明,以2mm粒径团聚体的含量为最高,约占75%。Cu、Zn、Cd和Pb在0.25～0.5mm粒径团聚体中含量最高,Cr在5～8mm粒径团聚体中含量最高,As在不同粒径团聚体中的含量变化不大,重金属含量随土层深度增大而减小。土壤重金属富集因子表现为CuPbCdZnCrAs,Cu、Zn、Cd和Pb在0.25～0.5mm粒径团聚体中分布因子最高,而在5～8mm粒径团聚体中重金属的质量负载因子最大。土壤有机碳含量随团聚体粒径的增大表现为先增大后减小,不同粒径团聚体中Cu、Cd、Pb和As含量与有机碳含量均呈显著正相关(p0.05)。污灌区菜地土壤Cr、As在5～8mm粒径团聚体中富集现象显著,Cu、Zn、Cd、Pb在0.25～0.5mm粒径团聚体中均表现出显著的富集特征。6种重金属在5～8mm粒径团聚体中的质量负载因子均为最高,表明6种重金属在5～8mm粒径团聚体中的贡献最大。     

聚硅硫酸铁絮凝剂去除市政污水磷的研究

将自制复合絮凝剂聚硅硫酸铁(PFSS i)用于市政污水除磷,考察了影响PFSS i除磷效果的一些因素,确定了PFSS i复合絮凝剂除磷的优化配比和用量。在优化条件下,对模拟污水中磷的去除率为96.7%,浊度去除率为92%;对实际污水中磷的去除率为82.3%,浊度去除率为96.5%。结果表明该复合絮凝剂有良好的除磷、除浊性能。     

Determination of heavy metals in industrial wastes by SXRF method

Samples of the raw input material and industrial wastes collected at different processing stages of lead smelting units have been analyzed using the synchrotron induced X-ray fluorescence method to detect and estimate the presence of heavy metals. Heavy metals such as Sb, Cd, Sn, Pb are found to be present in significant amounts.     

Analysis of heavy metals in atmospheric particulate by ion chromatography

Cu, Ni, Zn, Co, Fe+2, Mn, Cd, Fe+3 and Pb are easily separated and detected in isocratic mode by ion chromatography with post-column derivatization using a bifunctional ion-exchange column and an eluent formed by oxalic acid (28 mM) and sodium nitrate (250 mM). The separation is optimised by using a suggested sample solution containing a given concentration of chloride. Detection limits were 10-15 ppb for all the metals except for cadmium and lead, for which detection limits of 30 and 60 ppb were found, respectively. The method was tested on an atmospheric particulate certified sample. The measured values were in good agreement with certified values. Real samples of atmospheric particulate from industrial and urban sites were analysed and the results are discussed.     

Treatment of sugar processing industry wastewater using copper electrode by electrocoagulation: Performance and economic study

This paper demonstrates the use of copper electrode for the treatment of sugar processing industry wastewater (SPIW) in terms of chemical oxygen demand (COD) by applying electrocoagulation (EC) method. EC process was carried out in batch mode with electrode effective area of 0.0112 m², supplied current intensity (CI) of 44.64 A/m² - 223.21 A/m², electrode gap (EG) of 0.5–2.5 cm, electrolyte (NaCl) dose (ED) of 0.5–2.5 g/L to treat SPIW with initial chemical oxygen demand (COD) of 6000 mg/L. The maximum COD removal 73% of SPIW is achieved at optimized condition of SPIW pH: 7, CI: 89.28 A/m², EG: 1.5 cm & ED: 1.5 g/L. Sludge and scum generated during EC process were characterized by FTIR, TGA/DTA/DTG, proximate & ultimate analysis to find its applicability and their disposal. Additionally, economic study of EC treatment process at optimum condition suggest treatment cost was 11.2 US$/m³ and it indicate economic results as comparison to other available treatment processes.     

Sorption and preconcentration of some heavy metals by 2-mercaptobenzothiazole-clay

2-Mercaptobenzothiazole loaded on previously treated clay was prepared, characterized and used for sorption and preconcentration of Hg(II), Pb(II), Zn(II), Cd(II), Cu(II) and Mn(II) from an aqueous solution. The support used was a natural clay previously treated with sulphuric acid solution. Adsorption isotherms of metal ions from aqueous solutions as function of pH were studied at 298 K. Conditions for quantitative retention and elution were established for each metal by batch and column methods. The chemically treated clay was very selective to Hg(II) in solution in which Zn(II), Cd(II), Pb(II), Cu(II) and Mn(II) were also present.