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[Production of mutagenic compounds during the water purification treatment of surface water].

In the last years many studies have reported the presence of mutagenic/carcinogenic compounds in treated waters. These substances can be present in raw water, but are also produced during drinking water purification. Mutagens are formed as by-products of chemical reactions between oxidants/disinfectants used in treatments and organic load of the raw water (humic and fulvic acids). The aim of this study was to evaluate the production of mutagenic substances during the main phases of the Po river water treatment ("PO3" plant) in Turin. Water samples (50 litres), collected from February 1989 to August 1990, were concentrated with XAD-2/XAD-8 resins mixture. Extracts were tested for mutagenicity at different doses (1, 2.5, 5 and 10 litres) by Ames Salmonella assay, using TA 100 and TA 98 strains, without microsome fraction (S9). Raw water was rarely mutagenic while, in particular at the highest doses (5 and 10 litres), sometimes showed toxic effect. After ozonation treatment only few samples were mutagenic with TA 100 strain, while 43% of the samples were mutagenic with TA 98. The following treatment of clariflocculation and chlorination with NaClO produced mutagens in 95% of the samples assayed with TA 100 and in 85% of the samples assayed with TA 98. The next GAC/sand filtration step seems to reduce the mutagenic load produced in the previous phases. Finally, drinking water after chlorination with ClO2 showed weak mutagenicity at 1 litre dose (26% and 21% of positive samples with TA 100 and TA 98 respectively) and this effect increased at the higher dosages.(ABSTRACT TRUNCATED AT 250 WORDS)

Carcinogenicity Tests

A water purification system for laboratory use.

A water purification system is described, capable of producing Type I water upon demand at multiple locations up to 700 feet, from the purifying equipment. Tap water is initially treated employing reverse osmosis, followed by treatment with activated charcoal and mixed anion/cation exchange resins. The resultant Type I quality water is maintained by means of a recycling loop until removal upon demand. The current cost of producing water of this quality is $0.03 per liter, exclusive of capital and installation costs.

Dialysis

[Water purification from ethylene glycol by catalytic oxidation using hydrogen peroxide].

In order to select the method of water regeneration from air moisture condensate in a manned enclosed environment, the procedure of water decontamination from ethylene glycol was investigated. The process developed at t 20-22 degrees C and the following concentrations of C2H6O2 = 0.0125-0.5 mole/l, H2O2 = 1-5 mole/l, and catalyst = 1.7-50% wt. In the presence of 6.67 g/l of homogeneous catalyst FeSO4.7H2O, destructive oxidation of ethylene glycol to yield CO2 in the system 0.1 M C2H6O2 + 1M H2O2 proceeded effectively. However, the iron concentration in the decontaminated water exceeded significantly the maximally allowable concentration of iron in potable water as well as in industrial and non-industrial sewage. Heterogeneous MnO- and PbO-based catalysts provided no more than 20% ethylene glycol oxidation. Siderite, a natural mineral containing 33% wt. Fe2+, proved a more effective catalyst of ethylene glycol oxidation. When ethylene glycol and hydrogen peroxide were used at ratios of 1:30 and 1:80 with 5% wt. siderite, the degree of C2H6O2 to CO2 conversion was 99.2% and 99.8, respectively.

Aerospace Medicine

[Method of purification of water by means of ion-exchange cellulose fibers].

A new method of and an arrangement for continuous ion-exchange purification of water from admixtures contained therein in the form of dissolved electrolyte ions have been devised. As a basic working element for this purpose serves anion-exchange tape made of anion-exchange cellulose fibre (ICF) that enables a continuous purification of water from impurities contained therein the be effected as needed.

Cellulose