Selective removal of arsenate from drinking water using a polymeric ligand exchanger

The new maximum contaminant level (MCL) of 10 μg/L for arsenic in the US drinking water will take effect on January 22, 2006. The compliance cost is estimated to be $ 600 million per year using current treatment technologies. This research aims to develop an innovative ion exchange process that may help water utilities comply with the new MCL in a more cost-effective manner. A polymeric ligand exchanger (PLE) was prepared by loading Cu²⁺ to a commercially available chelating ion exchange resin. Results from batch and column experiments indicated that the PLE offered unusually high selectivity for arsenate over other ubiquitous anions such as sulfate, bicarbonate and chloride. The average binary arsenate/sulfate separation factor for the PLE was determined to be 12, which were over two orders of magnitude greater than that (0.1–0.2) for commercial strong-base anion (SBA) exchangers. Because of the enhanced arsenate selectivity, the PLE was able to treat 10 times more bed volumes (BVs) of water than commonly used SBA resins. The PLE can operate optimally in the neutral pH range (6.0–8.0). The exhausted PLE can be regenerated highly efficiently. More than 95% arsenate capacity can be recovered using 22 BVs of 4% (w/w) NaCl at pH 9.1, and the regenerated PLE can be reused without any capacity drop. Upon treatment using FeCl₃, the spent brine was recovered and reused for regeneration, which may cut down the regenerant need and reduces the volume of process waste residuals. The PLE can be used as a highly selective and reusable sorbent for removal of arsenate from drinking water.     

Magnetic zeolites: a new adsorbent for removal of metallic contaminants from water

In this work the adsorption features of Na Y zeolite with the magnetic properties of iron oxides have been combined in a composite to produce a magnetic adsorbent. These magnetic composites can be used as an adsorbent for metallic contaminants in water and subsequently removed from the medium by a simple magnetic process. The zeolites:iron oxide magnetic composites, were prepared by using Na Y with weight ratio of 3:1 and were characterized by powder X-ray diffraction (XRD), magnetization measurements, chemical analyses, N(2) adsorption isotherms and M?ssbauer spectroscopy. Nitrogen adsorption isotherms showed that the surface area decreased from 505 m(2)g(-1) for the pure Na Y to 353 m(2)g(-1) for the Na Y:Fe oxide 3:1 composite. The adsorption isotherms of metal ions Cr(3+), Cu(2+) and Zn(2+) from aqueous solution onto the composites also showed that the presence of iron oxide does not affect the adsorption capacity.     

Rapid column-mode removal of arsenate from water by crosslinked poly(allylamine) resin

Performances of crosslinked poly(allylamine) resin (PAA) as arsenate (As(V)) adsorbent were studied using a column packed with PAA in hydrochloride form. PAA has a high amino group content of 14.6 mmol/g in free amine form and a high chloride content of 10.2 mmol/g in hydrochloride form. Its wet volumes in water were 4.5 and 3.1 mL/g in hydrochloride and free amine forms, respectively, indicating its high hydrophilicity. Breakthrough capacities for As(V) were evaluated changing conditions of adsorption operations: pH of feeds from 2.2 to 7.0, concentration of As(V) in feeds from 0.020 to 2.0 mM, and feed flow rate from 250 to 4000 h⁻¹ in space velocity. Breakthrough capacities increased from 2.6 to 3.4 mmol/g with a decrease in pH from 7.0 and 2.2, and also from 0.81 to 2.8 mmol/g with an increase in As(V) concentration from 0.020 to 2.0 mM. When feed flow rate increased from 250 to 4000 h⁻¹, breakthrough capacities changed form 3.5 to 0.81 mmol/g. Because of non-Hofmeister anion selectivity behavior of PAA, the interference of chloride and nitrate was minor. Although PAA slightly preferred As(V) to sulfate, the latter more markedly interfered with uptake of As(V) than chloride and nitrate. Competitive uptake of As(V) and phosphate revealed that PAA slightly preferred phosphate to As(V). The adsorbed As(V) was quantitatively eluted with 2 M HCl and PAA was simultaneously regenerated into hydrochloride form. All results were obtained using the same column without change of the packed PAA and any deterioration in column performances for 4 months.     

Re-use of water treatment works sludge to enhance particulate pollutant removal from sewage

This paper attempted to study the feasibility of reusing water treatment works sludge ("alum sludge") to improve particulate pollutant removal from sewage. The main issues focused upon were: (1) the appropriate dosage of the alum sludge, (2) the appropriate operating conditions, and (3) the possible mechanisms for enhancement by adding alum sludge. Actual alum sludge and sewage were applied to a series of jar tests conducted under various conditions. It has been found that both the SS and COD removal efficiencies could be improved by the addition of the alum sludge, which was mainly attributed to the removal of relatively fine particles with a size of 48-200 microm. The appropriate dosage of the alum sludge was determined to be 18-20 mg of Al/L. Increasing the mixing speed or reducing the floc size of the alum sludge enhanced the SS and COD removal and the dispersed alum sludge could remove particulate contaminants with smaller size than the raw sewage. ToF-SIMS evidence revealed that the aluminum species at the surface of the alum sludge were effectively utilized for improving the SS and COD removal. It was postulated that the sweep flocculation and/or the physical adsorption might play key roles in the enhancement of particulate pollutant removal from sewage.     

Hydrological controls of pollutant removal from highway surfaces

Sediment and metal loadings to roadside gully-pots (weight/area of catchment/runoff depth) are calculated for two defined sites within a highway catchment and compared with data from other urban studies. The higher metal loadings associated with the more active site are particularly noticeable for Cu but at both sites the relative sizes of the metal loadings reflect the expected metal availabilities.The measured total surface runoff volumes represent between 34 and 83% of the total incoming rainfall volume for the catchment. The possible reasons for these water losses are assessed in terms of surface characteristics, seasonal variations and instrument limitations.Stepwise linear regression analysis of pollutant loadings against five selected hydrological parameters indicates that total runoff volume and storm duration together explain over 90% of the observed variance in Pb, Cd, Mn and sediment loadings. The results demonstrate the lack of importance of antecedent dry period and rainfall intensity in controlling the removal of particulate associated pollutants from this catchment. The derived model is used to predict temporal pollutant removal rates and these are shown to be consistent with those reported in other urban catchment studies.     

Hybrid reactor for priority pollutant nitrobenzene removal

The performance of a hybrid reactor, comprising of trickling filter and activated sludge process, in treating nitrobenzene wastewater was investigated. Acetate induced cells of mixed consortia was acclimatized with gradual increase of nitrobenzene concentration up to 90 mg/l in 100 days using sodium acetate as co-substrate and considering COD and nitrobenzene concentration as paramount parameters for assessing the growth of biofilm and acclimation. A removal of 60-95.80% COD and 80-90.23% nitrobenzene was observed during acclimation. During hydraulic retention time (HRT) studies, the optimum HRT was found to be 29.55 h at which a maximum of 95.83% COD and 97.93% nitrobenzene removal was observed. Other studies included optimization of C:N ratio, substrate:co-substrate ratio, effect of shock loading and estimation of volatilization losses. The optimum C:N ratio was found to be 100:20 at which maximum 97.93% removal of nitrobenzene was observed. At optimum HRT (29.55 h) and optimum C:N ratio (100:20) optimum substrate:co-substrate ratio was found to be 1:33. From the shock load studies it can be concluded that the system can withstand shock load up to two times of usual nitrobenzene concentration. A loss of 9.44% nitrobenzene was observed due to volatilization and mass balance gave an efficiency of 87.49% biological removal of nitrobenzene.     

An evaluation of pretreated natural zeolites for ammonium removal

Clinoptilolite has been widely studied for ammonium removal in the past 2 yr. However, many investigators have reported variations in the measured capacities of samples of clinoptilolite. These studies and the factors believed to influence measured zeolite capacity are reviewed. In addition no studies to evaluate other natural zeolites for ammonium removal have been reported.In this study samples of clinoptilolite, erionite, mordenite and phillipsite provided by the Anaconda Company were evaluated for ammonium removal from wastewaters. In addition, samples of clinoptilolite were pretreated in various ways to determine whether an improvement in ammonium removal performance could be realized. Total exchange capacities, capacities for ammonium removal from a synthetic waste, packed bed densities and crushing strengths were measured.Phillipsite was found to have almost twice the weight capacity for ammonium removal from synthetic waste compared to that of clinoptilolite. The volumetric capacity was 26% better than that of clinoptilolite. However, the phillipsite sample was extremely friable and it could not be used for water treatment unless it was strengthened with a binder.Pretreatment of clinoptilolite with NaOH, HNO₃ and steam did little to improve the zeolite's performance. However, heat pretreatment (600°C for 1 h) improved the zeolite's selectivity for ammonium significantly. Ammonium removal capacities were increased by approximately 17% for heat treated zeolite samples although the total exchange capacity of the zeolite was reduced somewhat.     

Uranium removal from contaminated groundwater by synthetic resins

Synthetic resins are shown to be effective in removing uranium from contaminated groundwater. Batch and field column tests showed that strong-base anion-exchange resins were more effective in removing uranium from both near-neutral-pH (6.5)- and high-pH (8)-low-nitrate-containing groundwaters, than metal-chelating resins, which removed more uranium from acidic-pH (5)-high-nitrate-containing groundwater from the Oak Ridge Reservation (ORR) Y-12 S-3 Ponds area in Tennessee, USA. Dowex 1-X8 and Purolite A-520E anion-exchange resins removed more uranium from high-pH (8)-low-nitrate-containing synthetic groundwater in batch tests than metal-chelating resins. The Dowex 21K anion-exchange resin achieved a cumulative loading capacity of 49.8 mg g(-1) before breakthrough in a field column test using near-neutral-pH (6.5)-low-nitrate-containing groundwater. However, in an acidic-pH (5)-high-nitrate-containing groundwater, metal-chelating resins Diphonix and Chelex-100 removed more uranium than anion-exchange resins. In 15 m L of acidic-pH (5)-high-nitrate-containing groundwater spiked with 20 mg L(-1) uranium, the uranium concentrations ranged from 0.95 mg L(-1) at 1-h equilibrium to 0.08 mg L(-1) at 24-h equilibrium for Diphonix and 0.17 mg L(-1) at 1-h equilibrium to 0.03 mg L(-1) at 24-h equilibrium for Chelex-100. Chelex-100 removed more uranium in the first 10 min in the 100mL of acidic-(pH 5)-high-nitrate-containing groundwater ( approximately 5 mg L(-1) uranium); however, after 10 min, Diphonix equaled or out-performed Chelex-100. This study presents an improved understanding of the selectivity and sorption kenetics of a range of ion-exchange resins that remove uranium from both low- and high-nitrate-containing groundwaters with varying pHs.     

Nitrate removal from ground water

A new technique is described for nitrate removal from ground water. This technique is a combination of ion exchange and biological denitrification. Nitrate is removed by ion exchange. Regeneration of the resin in a closed circuit is achieved with a denitrification reactor. In contrast with traditional denitrification procedures there is no direct contact between ground water and denitrifying bacteria. Also brine production and regeneration salt requirements are minimal as compared with conventional regeneration of ion exchange resins. The basic design criteria and the first pilot plant results are presented. The pilot plant results show that the process is very attractive when compared with ion exchange and biological denitrification as separate techniques. Ground water with a relatively high sulfate concentration can be treated when a nitrate selective resin is used.     

Effects of water chemistry and flow rate on arsenate removal by adsorption to an iron oxide-based sorbent

Arsenate removal from water using an iron oxide-based sorbent was investigated to determine the optimal operating conditions and the influence of water composition on treatment efficiency. The novel sorbent with a high surface area was studied in flow-through column experiments conducted at different flow rates to quantify the effect of empty bed contact time (EBCT) on treatment performance. Arsenic removal efficiency declined with decreasing EBCT. Arsenic breakthrough curves at different EBCT values were successfully simulated with a pore and surface diffusion model (PSDM). Surface diffusion was the dominant intraparticle mass transfer process. The effect of water composition on arsenic removal efficiency was evaluated by conducting experiments with ultrapure water, ultrapure water with either phosphate or silica, and a synthetic groundwater that contained both phosphate and silica. Silica was more inhibitory than phosphate, and the silica in synthetic groundwater controlled the arsenic removal efficiency.     

Investigation of phosphorus removal from water

The removal of different phosphate compounds from water and waste water by precipitant was investigated. Calcium hydroxide precipitated orthophosphate with greater efficiency than aluminium sulphate, while aluminium sulphate gave better efficiency in the removal of polyphosphates. Calcium hydroxide was not able to precipitate the phosphate in glucose phosphate—and aluminium sulphate effects only a slight precipitation. Bentonite and polyelectrolyte (partly anionic type), in conjunction with aluminium sulphate, gave an increased phosphate reduction, settling velocity, a decreased turbidity of the liquid and a decreased sludge volume.

In the case of waste water, considerably better results were achieved due to the high content of suspended matter, which helped to bind the phosphate compounds into flocs. The use of bentonite and polyelectrolyte in treating waste water gave better results and better results were also obtained when calcium hydroxide was used alone for precipitation.     

Variation among plant species in pollutant removal from stormwater in biofiltration systems

Biofiltration systems use vegetation to improve efficiency of pollutant removal from stormwater, but little is known of how plants vary in their capacity to improve biofilter effectiveness. We used a pot trial of 20 Australian species to investigate how species vary in the removal of pollutants from semisynthetic storm water passing through a soil filter medium. Effluent levels of total suspended solids (TSS), Al, Cr, Cu, Pb and Zn were similarly low for vegetated and non-vegetated soils, with reduction to <1-12% of levels in the stormwater input. N and P effluent concentrations were generally lower from vegetated than non-vegetated soils, but total N increased on average in effluent of both vegetated and non-vegetated soils relative to stormwater input. Effluent concentrations varied 2-4-fold among species for TSS, total N and P, total dissolved N (TDN), organic nitrogen and Cu, to more than 20-fold for NOx, NH4+, Mn, Pb and Fe. Species also varied markedly in pollutant removal per root mass (a means of standardising for plant size), with 18-50-fold variation among species in effluent concentrations of total P and N, TDN and organic N, to >150-fold variation in NOx and NH4+. Hence, choice of plant species may have marked effects on biofilter effectiveness.     

Organic arsenic removal from drinking water

Arsenic occurs in both inorganic and organic forms in water. Although various methods have been adopted to remove inorganic species of arsenic from drinking water, not much emphasis has been given to the removal of organic species of arsenic. In the present study column studies were conducted using manganese greensand (MGS), iron oxide-coated sand (IOCS-1 and IOCS-2) and ion exchange resin in Fe³⁺ form, to examine the removal of organic arsenic (dimethylarsinate) spiked to required concentrations in tap water. Batch studies were conducted with IOCS-2, and the results showed that the organic arsenic adsorption capacity was 8 μg/g IOCS-2. Higher bed volumes (585 BV) and high arsenic removal capacity (5.7 μg/cm³) were achieved by the ion exchange resin among all the media studied. Poor performance was observed with MGS and IOCS-1.     

Probabilistic modeling of detention basins for highway stormwater runoff pollutant removal efficiency

The effects of various design configurations and the operation of detention basins for pollutant removal efficiency is evaluated using a Monte-Carlo simulation approach. A physically based numerical model representing the build-up and wash-off of pollutants from the highway surface has been used to predict storm events pollutographs for dissolved Cu and Zn. The probability of discharging dissolved Cu and Zn from detention basins were assessed using randomly-generated rainfall-runoff events and build-up pollutant concentrations. The simulations were performed by comparing the results of a one-compartment detention basin with a two-compartment design. The simulation results revealed that dividing the detention basin into two compartments and using the first compartment for first flush treatment can substantially reduce the frequency of discharging toxic metals such as Cu and Zn into the receiving waters. With the first flush treatment method, the size of the detention basin can be reduced to half of the conventional design.     

Aminopolycarboxylic acid functionalized adsorbents for heavy metals removal from water

Due to the excellent chelating properties of aminopolycarboxylic acid (APCAs), they can be used for the removal of metals from contaminated waters. This paper reviews the research results obtained for both commercial and self-prepared adsorbents functionalized with four most common APCAs: iminodiacetic acid (IDA), nitrilotriacetic acid (NTA), ethylenediaminetetraacetic acid (EDTA), and diethylenetriaminepentaacetic acid (DTPA). The structural characteristics and unique metal binding properties of these chelating adsorbents are presented. The theory of the adsorption phenomena is discussed based on the kinetics of adsorption, equilibrium adsorption isotherm models, and thermodynamic models. The most important applications of APCA-functionalized adsorbents are also described. APCA-functionalized adsorbents are found to be highly promising materials for metal removal from contaminated waters.     

水源水中乐果污染物应急处理工艺的试验研究

以乐果为目标化合物,探讨了活性炭吸附、活性炭吸附-混凝沉淀工艺以及石灰碱解-活性炭吸附-混凝沉淀三种工艺对乐果的去除效果.结果表明,乐果的去除效果随着活性炭投加量与吸附时间的增加而增加,采用活性炭吸附-常规混凝沉淀工艺对乐果的去除效果要略好于单独采用活性炭吸附,但这两种工艺都不能有效去除水中的乐果.采用石灰碱解-活性炭吸附-混凝沉淀工艺时,乐果的去除率随着石灰碱解的pH值升高而增加.当原水乐果含量为0.182 mg/L,用石灰调节原水pH值为9,投加30 mg/L活性炭吸附20 min后,去除率达89.9%,沉淀出水乐果浓度为0.018 4 mg/L,满足标准要求.     

Low-level mercury removal from groundwater using a synthetic chelating ligand

Mercury is present in many industrial processes at low concentrations and is a cause for concern due to the propensity for mercury to bioaccumulate. As a cumulative toxin, introduction of mercury into the environment at any level has the potential to adversely affect ecologic systems. To date, no commercial precipitants are available that can irreversibly and permanently bind mercury. In the current work, selected commercial reagents were compared alongside the dianionic ligand 1,3-benzenediamidoethanethiolate (BDET(2-)) to test the feasibility of low-level (parts-per-billion, ppb) mercury treatment for groundwater near a chloralkali plant. Of all the reagents examined, only K(2)BDET was capable of reducing mercury concentrations to below instrumental detection limits of 0.05 ppb with the added benefit of producing a stable precipitate.     

Phosphorus removal from water by means of electrolysis

P removal from water by electrolysis was examined by an experimental laboratory system. Two types of electrodes, Al and Fe, were investigated with respect to the relationship between P removal and energy consumption. The Al electrodes were most efficient in this respect. Alternating current gave the best “self-cleansing” of the electrodes, but the period should exceed 2–3 min to give maximum P-removal efficiency.     

A review of technologies for the removal of sulfate from drinking water

Because of the current water crisis worldwide, it is of great importance to find alternative sources of drinking water, such as sulfur water. This review analyses laboratory, pilot and industrial-scale technologies available for sulfate removal from water produced for human consumption, from naturally occurring sulfur water and that resulting from human activities. Most of them exceed 90% removal efficiencies. However, the concentrations treated in each study were different; some technologies evaluate concentrations below recommended limits (250 mg L⁻¹), while others evaluate much higher concentrations but require previous treatments. The technologies with higher energy requirements such as reverse osmosis and ion exchange have better removal efficiencies but require larger initial investments and have higher operational costs. Biological treatments, on the other hand, with lower energy and material requirements, are less expensive but require long retention times and depend on the season of the year and/or environmental conditions. Lastly, adsorption removal technologies fall in the middle, especially for energy requirements and operational costs and retention times. This review shows that although there are a variety of sulfate removal technologies suitable for use, there is still room for a novel methodology that removes sulfates from a wider range of concentrations more economically, more effectively and in less time than what is currently available.     

Sorption materials for arsenic removal from water: a comparative study

Five different sorption materials were tested in parallel for the removal of arsenic from water: activated carbon (AC), zirconium-loaded activated carbon (Zr-AC), a sorption medium with the trade name 'Absorptionsmittel 3' (AM3), zero-valent iron (Fe(0)), and iron hydroxide granulates (GIH). Batch and column tests were carried out and the behavior of the two inorganic species (arsenite and arsenate) was investigated separately. The sorption kinetics of arsenate onto the materials followed the sequence Zr-AC > GIH = AM3 > Fe(0) > AC. A different sequence was obtained for arsenite (AC > Zr-AC = AM3 = GIH = Fe(0)). AC was found to enhance the oxidation reaction of arsenite in anaerobic batch experiments. The linear constants of the sorption isotherms were determined to be 377, 89 and 87 for Zr-AC, AM3 and GIH, respectively. The uptake capacities yielded from the batch experiment were about 7gl(-1) for Zr-Ac and 5gl(-1) for AM3. Column tests indicated that arsenite was completely removed. The best results were obtained with GIH, with the arsenate not eluting before 13100 pore volumes (inflow concentration 1 mg l(-1) As) which corresponds to a uptake capacity of 2.3 mg g(-1) or 3.7 g l(-1).