GL-CL-03 – New Wastewater Treatment Plant in Lieşti. New Wastewater Treatment Plant in Pechea
The technological objects of the two plants are similar (but different sized, depending on influent flow rates), the difference being the necessity to build an effluent pumping station in Lieşti, because of the long distance (1.8 km) to emissary - Siret River.
Connection value: 27,005 p.e.
Type of the sewage system: mixed
Type of admission: Pressure pipe
Average daily flow: 5,025 m3/day
Maximum daily flow: 6,722 m3/day
Max. flow dry weather: 375 m3/h
Max. flow rainy weather: 502 m3/h
Connection value: 15,615 p.e.
Type of the sewage system: mixed
Type of admission: Pressure pipe
Average daily flow: 2,759 m3/day
Maximum daily flow: 3,518 m3/day
Max. flow dry weather: 191 m3/h
Max. flow rainy weather: 248 m3/h
Maximum values for effluent:
BOD5 Concentration: 20.0 mg/l
COD Concentration: 100.0 mg/l
Nitrogen (N) Concentration: 10.0 mg/l
Phosphorus (P) Concentration: 1.0 mg/l
Suspended solids: 35.0 mg/l
Aerial view of WWTP Pechea, Romania (15,615 p.e.)
Wastewater is transported through the inlet pipeline of the sewer system or, if using cesspool emptiers, through a septic sludge receiving station to the inlet pipe fitted with a flow meter. Thanks to the advanced technological design, the treatment plant can work effectively even in case of large variations of the influent flow.
Retention of solids from the wastewater is done using a compact system consisting of two technological lines, each containing 1 coarse screen and 1 fine screen. Particles less than 2 mm and floating matters are separated and removed by grit and grease separator. A sand classifier takes the retained particles which are then washed, compacted and stored in a container.
For phosphorus removal and industrial water coagulation (reduction of organic substances - COD, suspended solids - SS, ammonium - NH4+, etc.) a solution of ferric chloride - FeCl3 is used. For this purpose, a FeCl3 dosing station is provided. The solution is introduced through a pipe system into the distribution chamber to the anaerobic tanks, being mixed with the wastewater.
The biological treatment starts after introducing the wastewater into the distribution chamber to the anaerobic tanks and mixing it with the recycled activated sludge, then the mixture of wastewater and activated sludge is passed to one of the two adjacent tanks, thus the process of the anaerobic treatment starts.
The technological design provides an innovative construction for the biological treatment: the "combi-pool", consisting of a set of concentric tanks: an outer annular aeration tank and a circular clarifier, centrally located. Each of the two technological lines include/s such a system, being able to operate independently.
The aeration system provides three high-efficiency blowers, one for each of the technological lines, the third being the reserve. The aeration equipment, located at the base of the aeration tanks (ring shaped), contains a fine-bubble aeration system with membrane diffusers. Due to the oxygen sensors from inside the aeration tanks, the assembly provides the amount of oxygen required for the biological treatment, fulfilling the condition of reducing energy consumption.
Following the steps of the biological treatment, in the final clarifier (the central circular tank) the activated sludge settles and then is transported to the distribution chamber to the anaerobic tanks, for ensuring a new cycle of treatment. Treated wastewater is discharged through a circular pipe, located at the top of the tank and subsequently discharged to the emissary.
Excess sludge and the floating sludge collected at the surface of the final clarifier are transported and stored in a circular tank - thickener tank for activated sludge in excess. When the sludge concentration from inside this tank reaches a threshold value, the sludge is transported to the dewatering station. Using a polymer solution, automatically dosed by a special equipment, the sludge is dewatered using 2 belt filter presses and then stored on drying platforms.
Pechea: Coarse screens
Pechea: Grit and grease separator
Lieşti: Screens building, Grit and grease separator
Lieşti: "combi-pool", Sludge Thickener
Lieşti: Polymer dosing station for sludge dewatering
Pechea: Control panel for the biological stage (MCC2)
Pechea: Laboratory of the treatment plant
Lieşti: Belt filter press - start-up
Pechea: SCADA terminal for monitoring and control
When designing, for both stations the redundancy principle was considered: for each stage were designed two identical independent technological lines, in order to ensure the plant operation even in case of fault or maintenance works on some equipment.
Technological project ensures reduction in consumption of electricity, mainly by using the gravitational flow of the wastewater throughout the treatment process. This ensures by the contract the guarantee for maximum annual operating costs of the station (costs arising from the consumption of electricity, concentrated polymer, ferric chloride).
Reliability, low power consumption and a lifetime of over 50 years are guaranteed by the fact that the delivered equipments have components from leading companies in this field: Siemens, Xylem, Aerzen, Invent, Getriebebau NORD, Helios, OCM, Watergates, Friulana, Grundfos, Netzsch etc.
Wastewater
Average daily flow (26 months): 1,155 m3
Maximum daily flow (13.10.2016): 7,381 m3
Energy consumption for technological equipment
Average daily power consumption (26 months): 696.3 kWh/day
Average annually power consumption (26 months): 254,135.6 kWh/year
Average annually power consumption per p.e.: 9.41 kWh/year * p.e.
CCO-Cr (max. 100 ml/l)
Average daily value influent (26 months): 78.2 ml/l
Average daily value effluent (26 months): 30.5 ml/l
Suspended Solids (max. 35 ml/l)
Average daily value influent (26 months): 95.1 ml/l
Average daily value effluent (26 months): 22.7 ml/l
Total Nitrogen (max. 10 ml/l)
Average daily value influent (26 months): 17.2 ml/l
Average daily value effluent (26 months): 4.4 ml/l
Ammonium (max. 3 ml/l)
Average daily value influent (26 months): 42.8 ml/l
Average daily value effluent (26 months): 0.9 ml/l
Aerial view of WWTP Liești, Romania