Advances in Water Treatment and Enviromental Management
Advances in Water Treatment and Enviromental Management
Advances in Water Treatment and Enviromental Management
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GREATER LYON EMERGENCY WATER INSTALLATIONS 59THE DECISION TO CONSTRUCT EMERGENCY WATER INSTALLATIONSFor this reason, <strong>in</strong> 1984 the Greater Lyons Council decided to set up emergency resources,which would make it possible to <strong>in</strong>terrupt pump<strong>in</strong>g operations <strong>in</strong> the catchment area dur<strong>in</strong>gthe passage downriver of the pollution slick. The capacity of the emergency water <strong>in</strong>stallations(150,000 cubic metres/day) was def<strong>in</strong>ed follow<strong>in</strong>g studies carried out on the risks of pollution<strong>and</strong> the correspond<strong>in</strong>g durations of <strong>in</strong>terruptions to water gather<strong>in</strong>g operations, it be<strong>in</strong>gunderstood, that low-priority water consumation (for the purposes of water<strong>in</strong>g, road wash<strong>in</strong>getc…) will be suspended dur<strong>in</strong>g the passage downriver of the pollution.Amongst the different solutions exam<strong>in</strong>ed, that <strong>in</strong>volv<strong>in</strong>g treatment of water from Lake Miribel-Jonage quickly emerged as the best choice, from both a technical <strong>and</strong> economic st<strong>and</strong>po<strong>in</strong>t.This lake, recently created, is a result of careffully-coord<strong>in</strong>ated extraction of alluvial depositsas part of a project for the development of a site for leisure activities. Located to the North-East of Lyons, it features a capacity of 7 000 000 cubic metres (which will eventually be<strong>in</strong>creased to 12 000 000 cubic metres) of water with highly satisfactory bacteriological <strong>and</strong>chemical characteristics.Given the geographical location of the lake, the logic beh<strong>in</strong>d the project is quite straightforward:Untreated water is drawn from the South-West side of the lake, <strong>and</strong> sent by a pump<strong>in</strong>gstationalong a pipe 1,10 metres <strong>in</strong> diameter to the treatment-plant, which is located <strong>in</strong>Rillieux, next to the Miribel canal. Treated water is returned to the catchment field pump<strong>in</strong>gnetwork, which means that the primary pump<strong>in</strong>g <strong>in</strong>stallations of the conurbation can beused.The development of this project was entrusted to the “Compagnie Générale des Eaux”, aspart of a concession agreement for construction <strong>and</strong> operation of the project.TREATMENT PROCESSThe treatment process is of course adapted to suit characteristics of lake water.The Rillieux plant is thus the first <strong>in</strong>stallation of its size to use the ozoflotation techniquedeveloped by OTV, which is particularly suited to elim<strong>in</strong>at<strong>in</strong>g algae <strong>and</strong> other suspendedparticles: although Lake Miribel does not for the time be<strong>in</strong>g give rise to any worries on thisaccount, algae development rema<strong>in</strong>s a constant threat to lake water.This process, which is carried out at the start of treatment operations, comes after flocculationwith ferric chloride followed by flash mix<strong>in</strong>g. The pr<strong>in</strong>ciple is as follows (see diagram below).<strong>Water</strong> overflow <strong>in</strong>to the ozonation compartment: porous plates diffus<strong>in</strong>g ozone are sweptalong by a stream of water, caus<strong>in</strong>g t<strong>in</strong>y bubbles to be created. This t<strong>in</strong>y bubbles are dragged<strong>in</strong>to the second compartment (flotation compartment), trapp<strong>in</strong>g a very hight proportion offloat<strong>in</strong>g particles <strong>and</strong> ensur<strong>in</strong>g optimum ozone transfer. The treated water exits from base ofthe flotation compartment <strong>and</strong> rejo<strong>in</strong>s the outlet channel.Periodic evacuation of impurities is carried out by rais<strong>in</strong>g the level of the water <strong>and</strong> us<strong>in</strong>g atransversal stream of water to sweep away the foam.The water is subsequently filtred by a battery of 9 tw<strong>in</strong>-layer “anthracites<strong>and</strong>” filters, afterwhich it undergoes a f<strong>in</strong>al ozonation process before enter<strong>in</strong>g the two 3 000 cubic metre tanksfor treated water. These tanks constitue the buffer storage of the <strong>in</strong>stallation <strong>and</strong> are used forbash wash<strong>in</strong>g the filters as well as for immediate start-up of the treatment plant.Sludge com<strong>in</strong>g from the ozoflotation process <strong>and</strong> from the filters is treated with the aid of arevolv<strong>in</strong>g blade thickener/clarifier followed by a belt-filter; this process makes it possible toreach a dry content value of over 25 %.One aspect related to the production of ozone is worthy of note: the ozone used here isproduced not from air but from pure oxygen, via a battery of two ozoniz<strong>in</strong>g devices.