search results

215 results found for:

Photo 28. - Barranca Berreja plant (Colombia) for Ecopetrol. Output: 72,000 m3· d–1. Oily water flotation. Four 15 m Ø Sediflotazur

Table 6. - NARA heat balance per kg · h–1 of water evaporated (based on a 20 % dry solids content sludge, 90 % dry)

Photo 4. - Algiers pumping station (New Orleans – USA): four 5.5 m wide and 6.1 m water depth climbing screens

Photo 11. - The Chattanooga plant (Tenessee) which treats the effluents of 1 600 000 PE, and includes 2 thermophilic digesters which feed 4 mesophilic digesters.

Photo 2. - SI Lesaffre yeast works (flour mill – starch works) (Marquette-lez-Lille, France) – Output: 4,100 m3· d–1

Polychémie - Horizontal degasifying heater

Photo 5. - Polychémie Bedrijf Beek (Netherlands) plant for pour DSM (Dutch Staat Smijnen). Output: 255 m3· h–1. Horizontal degasifying heater

Photo 19. - Gravity biological iron removal – Lomé DWTP (Togo). Capacity: 52,800 m3 · j–1 – four 24.5 m2 filters

Process water production treatment influents Pemex refinery

Photo 9. - Process water production and treatment of influents at the Pemex refinery (Salina Cruz – Mexico) – Flow: 6,000 m3.d-1

Photo 24. - Kernilis DWTP (Finistère, France). Capacity: 500 m3· h–1. Two of the three 2.5 m diameter Azurion exchangers

Solubility of CO2 and O2 in water - atmospheric pressure and pure gas atmosphere

Figure 32. - Solubility of CO2 and O2 in water in mg · L–1 of gas per litre of water at atmospheric pressure and in a pure gas atmosphere

Figure 24. - Crissey DWTP (Saône et Loire, France) for the Nord de Chalon Water Board. Installation diagram – Capacity: 7,200 m3 · j–1

town covering impermeabilisation combined separate systems

Table 32. - Theoretical case of a 10,000 inhabitant town covering a 170 hectare, 30 % impermeabilisation, site: mass discharged in t · year–1 by the plant and by the combined or separate systems

Photo 2. - Cebron-Puy Terrier plant (Deux-Sèvres). Output: 36 000 m3·d–1 – View of the water intake when the reservoir is drained out

Photo 21. - Simultaneous iron and manganese removal followed by activated carbon. Poncey gravity flow DWTP (Dijon, France) – Capacity: 72,000 m3 · j –1

Bleaching - production COD - chlorine derivatives

Table 55. - Bleaching: production of COD and chlorine derivatives (measured as AOX.t–1 ADt pulp) [European Commission, 2015, BREF "Pulp & Paper"]

Photo 23. - Nitrazur N –53 m2 filter in operation. Louveciennes plant (Yvelines). Output: 120 000 m3 · j–1

Figure 10. - Schematic diagram of the Mont Valérien (Hauts-de-Seine, France) DWTP – Capacity: 53,000 53 000 m3 · j–1

ozone solubility pure water - saturation concentration water temperature- ozone concentration gas pressure

Figure 36. - Ozone solubility in pure water or saturation concentration according to water temperature and ozone concentration in the gas under a 101.3 kPa (1 atm) pressure

Textile factory Association Haute Vallée de la Touyre

Photo 38. - Textile factory of the Association de la Haute Vallée de la Touyre – Lavelanet (Ariège, France) – Output: 15,000 m3· d–1

Alberta electricity station - condensate demineralisation unit skid-mixed beds

Photo 3. - Alberta electricity generating station (Canada). Output: 2 × 540 m3· h–1. Condensate demineralisation unit using skid-mounted mixed beds

181 - 200 of 215 result(s)