Evaluation of different treatment processes with respect to mutagenic activity in drinking water

Treatment processes which are applied in The Netherlands during the preparation of drinking water have been evaluated with regard to introduction and removal of organic mutagens as well as halogenated organics. It appeared that the most efficient processes in reducing mutagenic activity were activated carbon filtration and artificial dune recharge. In general these processes were also the most efficient in removing halogenated organics. Using low doses of chlorine dioxide (< 1 mg C10₂/1) for safety disinfection of drinking water, no change or substantial less mutagenic activity than by chlorination (1 mg Cl/1) was found. This counts too for the formation of halogenated organics. Transport chlorination of stored river Meuse water was able to introduce or activate mutagenic nitro organics which have not been found previously. Ozone treatment under field conditions showed mostly a tendency to decrease the activity of organic mutagens. It was also shown that dependent on the water quality and treatment conditions a slight increase of mutagenic activity occurred, but this activity would be reduced by increasing the ozone dose. It seems possible to optimalize the ozone treatment conditions regarding the level of ozone dose and the contact time to avoid an increase of mutagenic activity. Futhermore it was shown that when a mutagenic raw water source was used a proper combination of treatment processes is able to produce drinking water in which no mutagenic activity could be detected under the test conditions. Finally it is stated that before far-reaching decissions with respect to use mutagenicity data for a selection of water sources or treatment processes will be made, more information on the relation mutagenic activity from drinking water and effects on human health should become available.     

Critical considerations on the significance of carcinogenic and mutagenic compounds in drinking water

Public and scientific concern has been expressed on the possible hazards of trace amounts of organic compounds with carcinogenic and mutagenic properties, identified in drinking water. For a number of these compounds, the carcinogenicity is well established according to IARC criteria, but the extremely low concentrations (< 1 μg/1) indicate a neglectable risk to humans. Some compounds, mainly volatile halogenated alkylated hydrocarbons, may be present at higher concentrations, but for these the weight of evidence for carcinogenicity often is very poor, being demonstrated in mouse liver only. The relevance of mouse liver tumours may be seriously questioned, especially after exposure to hepatotoxic doses and in the absence of sufficient evidence for genotoxicity. It is therefore not justified, to use a non-threshold approach in the toxicological evaluation of these compounds. More or less similar conclusions can be derived for the organic “mutagens” identified in water, that is either their concentration is extremely low or sufficient evidence for genotoxicity is lacking. It is concluded therefore, that, at the present time, drinking water in the Western world can be regarded in general as “chemically safe”.     

Characterization of natural organic matter in conventional water treatment processes for selection of treatment processes focused on DBPs control

Natural organic matter (NOM) from raw and process waters at a conventional water treatment plant was isolated into hydrophobic and hydrophilic fractions by physicochemical fractionation methods to investigate its characteristics. Formation potential of trihalomethanes (THMs) was highly influenced by the hydrophobic fraction, whereas haloacetic acids formation potential (HAAFP) depended more on the hydrophilic fraction. However the hydrophobic fraction was removed more than the hydrophilic fraction through conventional water treatment. Therefore residual hydrophilic NOM after conventional treatment needs to be removed to reduce HAAFP. Feasible additional processes are required to be evaluated by comparing preferential removal efficiency of hydrophilic NOM through pilot tests. The structural and chemical characteristics of hydrophobic NOM (i.e., humic substances (HS)) were further investigated to know how they are influenced by conventional treatment. The phenolic fraction in the hydrophobic NOM was mainly removed compared to the carboxylic fraction through water treatment, and a higher formation potential of THMs resulted from NOM with a higher phenolic content. The Fourier-transform infrared (FT-IR) and proton nuclear magnetic resonance ((1)H-NMR) employed for characterization of NOM through water treatment were insightful revealing that their results were quite close to each other. Decreases of ratio of UV absorbance at 253 and 203 nm, respectively (A(253)/A(203) ratio) and trihalomethane formation potential/dissolved organic carbon (THMFP/DOC) showed consistent trends; therefore, the A(253)/A(203) ratio may be a good indicator of tendency for the formation potential of disinfection by-products (DBPs).     

Biological processes and organic micropollutants in treatment processes

This paper characterizes the factors that control biodegradation of organic micropollutants in biologically active drinking water processes. Particularly important are the dominance of attached microorganisms, the aerobic potential, the low concentration of organic matter, the very low concentrations of specific micropollutants, and the presence of inorganic electron donors. Biodegradation of the specific compounds is feasible if sufficient microbial growth occurs through utilization of natural organic material and if the secondary-utilization kinetics of the micropollutants are sufficiently rapid.     

The influence of salting out on the sorption of neutral organic compounds in estuaries

The relative (unsaturated) solubility and sorption of 2,2′,5,5′-tetrachlorobiphenyl have been studied along an estuarine salinity gradient. The aqueous compound was salted out with increasing salinity and an aqueous salting constant of about 0.002 l g⁻¹ was derived. Sorption of the compound to estuarine particles increased with increasing salinity for a range of particle concentrations, but the magnitude of this effect (sorption salting constants of about 0.005–0.01 l g⁻¹) indicated that salting out of the aqueous phase was not solely responsible. It is suggested that the hydrophobicity of sediment organic matter is enhanced by its interaction with seawater ions through a reduction in the charge of the particle surface and, possibly, modification of the structure of the organic matter. Examination of literature data on the sorption of neutral organic compounds to estuarine sediment indicates a general increase in sorption with increasing salinity which can be empirically defined by a salting equation. Although charge reduction of estuarine particles is a general observation, it is not possible to establish the general significance of this effect (or any other form of salting out of sediment organic matter) on the sorption of organic compounds in estuaries because appropriate site- and compound-specific aqueous salting constants are unavailable.

Increased sorption at high salinities has obvious implications for the disposal and transport of organic chemicals in estuaries. However, the inverse dependency of sediment–water partitioning on particle concentration is likely to be of at least equal significance in macrotidal environments where sediment resuspension occurs. An empirical model, combining the effects of salinity and particle concentration, is proposed for deriving first-order estimates of the partitioning of neutral organic compounds in estuaries.     

Fractionation of mutagenic compounds formed during chlorination of humic water

Mutagenic compounds formed during chlorination of humic water were fractionated by reversed phase high performance liquid chromatography, size exclusion chromatography and thin layer chromatography, in sequence. Following each chromatographic separation the mutagenic compounds were found in one fraction predominantly. A remarkable purification of active compounds was achieved without serious losses of activity, thus enabling further purification and mass spectrometric studies of the main mutagens.     

The heterogenic photocatalysis in water treatment processes

The paper has considered the mechanism and main regularities of oxidizing destruction of organic compounds on semi-conductor photocatalysts (predominantly TiO₂). The paper discusses the impact of physicochemical factors (concentration and nature of a photocatalyst and a substrate, the pH and medium oxidation-reduction potential, oxidants, etc.) on the decomposition kinetics of pollutants. The paper has analyzed the methods of raising the efficiency of the destruction process by surface and volumetric modification of photocatalysts with noble and other metals, metal oxides, their immobilization on various carriers, etc. It has been shown that the development of highly efficient and low-power-capacity methods of water purification of toxic organic compounds based on heterogenic photocatalytic system in question with the use of oxidants (O₂, O₃, H₂O₂, etc.) is a promising area in the ecology of the hydrosphere.     

The influence of oxidation reduction potential and water treatment processes on quartz lamp sleeve fouling in ultraviolet disinfection reactors

Ultraviolet (UV) disinfection systems are incorporated into drinking water production facilities because of their broad-spectrum antimicrobial capabilities, and the minimal disinfection by-product formation that generally accompanies their use. Selection of an optimal location for a UV system within a drinking water treatment facility depends on many factors; a potentially important consideration is the effect of system location on operation and maintenance issues, including the potential for fouling of quartz surfaces. To examine the effect of system location on fouling, experiments were conducted at a groundwater treatment facility, wherein aeration, chlorination, and sand filtration were applied sequentially for treatment. In this facility, access to the water stream was available prior to and following each of the treatment steps. Therefore, it was possible to examine the effects of each of these unit operations on fouling dynamics within a UV system. Results indicated zero-order formation kinetics for the fouling reactions at all locations. Increases in oxidation reduction potential, caused by water treatment steps such as aeration and chlorination, increased the rate of sleeve fouling and the rate of irradiance loss within the reactor. Analysis of metals in the sleeve foulant showed that calcium and iron predominate, and relative comparisons of foulant composition to water chemistry highlighted a high affinity for incorporation into the foulant matrix for both iron and manganese, particularly after oxidizing treatment steps. Fouling behavior was observed to be in qualitative agreement with representations of the degree of saturation, relative to the metal:ligand combinations that are believed to comprise a large fraction of the foulants that accumulate on the surfaces of quartz jackets in UV systems used to treat water.     

水中铝盐对微生物活性影响的研究现状

探讨了研究水中铝的含量对水处理系统的影响及危害的意义,综合铝的累积、铝的毒性作用以及目前国内外关于水中铝盐对微生物活性影响的研究,旨在对铝毒危害在水处理过程中的效应引起重视,并对研究目标和内容做了一些建议.     

Seasonal fluctuations in the content of different forms of organic carbon and their changes in water treatment processes

We have assessed the content of different forms of organic carbon (total, bioaccessible, and assimilated) in the water of the Dnieper river in the area of the water intake of the Dnieper water station and in the water after all treatment stages used. The article has investigated seasonal changes in the content of different forms of organic carbon and the impact of water treatment on these indicators.     

The fate of xenobiotic organic compounds in wastewater treatment plants

The effective operation of wastewater treatment plants plays an important role in minimising the release of xenobiotic compounds into the aquatic environment. Considerable effort has been expended in developing models to quantify the overall removal and fate of these compounds in biological treatment plants. A synthesis and modification of these approaches has been made and a generalised fate model for organic compounds in an activated sludge plant is presented. The influence of the different removal mechanisms, such as sorption, volatilisation and advection for chemicals with different physico-chemical properties is investigated and the important role of biotransformation is discussed. The effect of some operating parameters has been found to have an important influence upon the concentration of xenobiotic released in the sludges and final effluent. This may have significance for a wide range of ecotoxic compounds and in particular the class of compounds increasingly recognised as having the potential to disrupt endocrine activity in some aquatic vertebrates.     

The effect of different drinking water treatment processes on the rate of chloroform formation in the reactions of natural organic matter with hypochlorite

This study is concerned with the changes in the rate of chloroform formation during the reactions of groundwater natural organic matter (NOM) and sodium hypochlorite caused by different drinking water treatments schemes: coagulation with FeCl₃, Al₂(SO₄)₃ and polyaluminum chloride (PACl), filtration of the raw water through granular activated carbon (GAC) and filtration through the columns filled with strong base macroporous ion-exchange resins (Purolite A501P and A500P) with and without pretreatment by coagulation process. It was found that the change of the concentration of chloroform, within 2 h and c(Cl₂)=100 mg l⁻¹, can be described by a kinetic equation of the form [CHCl₃]=a+bt^c. On the basis of this equation rates of the reaction were calculated. All processes applied decreased the rate of chloroform formation (process of coagulation moderately decreased the rate of reactions, while GAC adsorption caused dramatically drop of the rate). Also, it was found that the resins have had a higher affinity towards slow-reacting chloroform precursors.

The value of the chloroform formation potential was conventionally determined after a 7-day reaction at pH 7. In addition, the same parameter was estimated with a satisfactory deviation for raw water and for treated water on the basis of the kinetic constant (k) or by determining the chloroform concentration after 2 h (ChFP₂) under rigourous chlorination conditions at pH 8.4.     

The use of redox potential in water treatment processes

The use of redox potential as a control parameter of wastewater treatment processes for characterizing the natural water condition and estimating the antioxidant properties of drinking water has been investigated.     

The removal of manganese in water treatment clarification processes

The removal of dissolved manganese in water treatment floc blanket clarifiers has been studied. The removal mechanisms may be broadly classified as adsorption and oxidation. Specifically adsorbed manganese is oxidised at the iron(III) oxide surface when solution pH approaches 8.5. The extent to which these removal processes contribute to manganese removal at plant scale will depend on the retention time of both liquid and solid components of flow within the clarifier, as well as clarifier pH.     

Toxicity assessment of organic compounds in drinking water in the Netherlands

In a recent survey of organic compounds present in drinking water of twenty cities in The Netherlands, it was found that only a minor fraction (10%) of the total organic content could be identified. It appeared that drinking water prepared from polluted surface water contains more organic compounds with carcinogenic and mutagenic properties than water prepared from groundwater. The concentration of most of the organic constituents identified was generally below the microgram/litre level.It is not expected that circumstances will occur, that these compounds willbe present in quantities, which are acutely toxic for consumers. On the other hand it cannot be excluded that certain organic compounds, in particular carcinogens and mutagens, may cause chronic toxic effects as a result of life time consumption of such contaminated drinking water.Therefore an epidemiological study was started in The Netherlands in which cancer mortality was related to the raw water source used for drinking water and the level of organic constituents. Preliminary results of the epidemiological study are presented.Furthermore a limited survey was carried out whereby drinking water of six cities was investigated for the presence of organic genotoxic compounds. The results of this survey led to the decision to extend this investigation to 19 cities. Finally, preliminary results regarding the characterization of the organic genotoxic compounds, present in drinking water, will be discussed.     

Effects of organic solutes properties on the volatilization processes from water solutions

Effects of organic solutes properties, including Henry's law constant (H), molecular weight (M), molar volume at normal boiling point (Vb), and solubility (S), on the usefulness of rate estimation by reference to a reference substance (i.e., reference substance concept) and on the evaporation rate were investigated by measuring the volatilization rate constant of organic solutes under different environmental conditions, including mixing and surfactants. It was found that if benzene was used as a reference substance, the ratio of the solute rate to that of benzene (F) becomes insensitive to water mixing, whether the solute possessed high or low Henry's law constant. In the presence of surfactants, however, the F value changes sharply as the solute solubility decreases. For benzene, toluene, ethylbenzene, and xylenes (BTEX), the F values are essentially constant irrespective of the presence of other chemicals (including organic compounds, surfactants, and salinity) and of the variation in temperature. On the other hand, the volatilization rates are closely related to molecular weight (solubility) in the existence of mixing (surfactants). Three different approaches, i.e., mass-transport theory, modified Knudsen equation, and reaction rate concept, were used to evaluate the dependence of solute volatilization rates on solute properties. It was concluded that the interaction between solute properties and environmental parameters might play a key role in the volatilization process of organic solutes under different environmental conditions.     

Rate constants of reactions of ozone with organic and inorganic compounds in water—I: Non-dissociating organic compounds

Rate constants of reactions of ozone with non-ionized solutes, such as aliphatic alcohols, olefins, chlorosubstituted ethylenes, substituted benzenes and carbohydrates, have been determined from the absolute rates with which ozone reacts in the presence of various concentrations of these compounds in water. They have been tested by comparison with the relative rates by which pairs of these solutes are transformed by ozone. Different experimental methods have been developed to determine such rate constants in the range from 10^?2 to 10⁵ M^?1 s^?1. Interferences between the direct reactions of ozone and reactions due to its preliminary decomposition to secondary oxidants could be eliminated. The kinetics of all the reactions studied are first order with respect to ozone and solute concentration. The rate constants of many types of organic compounds in water are of the same order of magnitude as in organic solvents. Substituted benzenes, however, react in water about 100 times faster. They obey a linear free energy relationship with p = ?3.1 when based on δ_p⁺ values. Comparisons of rate constants with chemical structures of the reacting groups show that all reactions of ozone are highly selective and electrophilic. The kinetic data allow explanation of the chemical effects of ozone observed in water treatment practice.     

Adsorption of chlorinated organic compounds on activated carbon from water

The adsorption capacities and rates of seven principal chlorinated organic compounds for six commercial GACs were investigated. All the adsorption isotherms were expressed by the Freundlich equation, and the isotherms for the chloroethylenes such as trans - 1,2-dichloroethylene, trichloroethylene and tetrachloroethylene could be shown by the modified Freundlich equation Q′ = k′ (C/C_s)^l/n for each GAC. The magnitude of adsorption of the chlorinated organic compounds was in the order of: tetrachloroethylene > trichloroethylene > trans - 1,2-dichloroethylene > 1,1-dichloroethane > carbontetrachloride > 1.1,1-trichloroethane > chloroform. The value of k for a certain GAC could be predicted from the quantity of pores smaller than 2 nm in diameter. The adsorbed amounts were decreased by 10–20% when humic substances coexisted. The working periods of a fixed bed adsorber before regeneration were predicted by calculating breakthrough curves for various influent concentrations of trichloroethylene and tetrachloroethylene at the space velocities of 5 or 10 h⁻¹, and it was certified that the adsorption method by GAC was feasible for removing these compounds from water.     

Impact of recycling filter backwash water on organic removal in coagulation-sedimentation processes

The overall purpose of this research was to examine the impacts of filter backwash water (FBWW) and membrane backwash water (MBWW) recycles on water quality in coagulation-sedimentation processes. Specifically, the impact of recycling 5 or 10% by volume of FBWW and MBWW with surface water on the removal of natural organic matter (NOM) was evaluated at bench-scale using a standard jar-test apparatus and measurement of specific water quality parameters including total organic carbon (TOC), dissolved organic carbon (DOC), UV254, turbidity, total aluminum and zeta potential. The results of jar test conducted on a source water with a specific UV absorbance (SUVA) value within the range of 2-4 mg/L m showed a significantly higher removal of DOC from the raw water that was blended with 5 and 10% by volume of FBWW as compared to control trials where backwash water was not added. Increasing rates of MBWW that did not contain destabilized hydroxide precipitates did not significantly change DOC concentrations in the settled water samples as compared to the control trials. For source waters that are characterized as having low turbidity with medium SUVA values, these results could hold particular significance for plants that have reached treatment ceilings in terms of dissolved NOM removal using conventional coagulation designs.     

Aerosole complexes in water treatment processes

Defined are prospects of using ozone-hydroxyl aerosol blends for treating water by complex effects of electro-plasma charges and UV radiation of water volume under the layer of the air component given the pulse nature of regulating the electric field in the practice of conducting deactivation of impurities of the proposed unit. The use of the given technique of water treatment makes it possible to raise the efficiency of its purification of micromycetes and hardly oxidized organic and mineral pollutants without preliminary use of chemical reagents.