Systems Analysis of Zaragoza Urban Water - SWITCH - Managing ...

Systems Analysis of Zaragoza Urban Water - SWITCH - Managing ... Systems Analysis of Zaragoza Urban Water - SWITCH - Managing ...

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Systems Analysis of Zaragoza UWS Guillermo Penagos Table 4. Zaragoza public WWTPs WWTP Cartuja Almozara Parameter Sewage Origin Industrial and domestic Industrial and domestic Average flow at design 3.00 0.40 (m 3 s -1 ) Average actual flow in 1.72 0.37 2006 (m 3 s -1 ) Water treatment Primary sedimentation, Biological Primary decantation, Biological treatment by activated sludge and treatment by activated sludge and secondary decantation secondary decantation, Phosphorus removal with Iron Chloride Sludge treatment Primary and secondary digestion plus dehydration by filter press Centrifuge dehydration flowed by incineration As it can be seen in table 4 “Almozara” is working near its actual capacity whereas “Cartuja” seems to be over dimensioned and is working at half of its actual capacity. 4.3 Environmental performance of Zaragoza UWS 4.3.1 Use of chemical products Figure 7 shows the annual consumption of chemical products by Zaragoza UWS from 2000 for DWT and from 2001 for WWT. There is a steady trend over these years, but Chlorine and Allum shows a clear reduction for 2005 and 2006, from around 3000 to 2500 ton and from 8000 to 6000 ton respectively. PAC use for DWT started in 2003 and it has not been steady since then. 32

Systems Analysis of Zaragoza UWS Guillermo Penagos Chlorine consumption Alum consumption 4,000 12,000 Chloride (tons) 3,500 3,000 2,500 2,000 1,500 1,000 500 Alum (tons) 10,000 8,000 6,000 4,000 2,000 0 2000 2001 2002 2003 2004 2005 2006 Year 0 2000 2001 2002 2003 2004 2005 2006 Year Powdered Activated Carbon consumption Iron Chloride consumption 400 12,000 350 300 10,000 PAC (tons) 250 200 150 100 FeCl 3 (ton) 8,000 6,000 4,000 50 0 2000 2001 2002 2003 2004 2005 2006 Year 2,000 0 2001 2002 2003 2004 2005 2006 year Figure 7. Chemical products consumption by Zaragoza UWS. Chlorine, Allum and PAC are used for DWT whereas Iron Chloride is used for WWT in “Carjuja”plant 33

<strong>Systems</strong> <strong>Analysis</strong> <strong>of</strong> <strong>Zaragoza</strong> UWS<br />

Guillermo Penagos<br />

Table 4. <strong>Zaragoza</strong> public WWTPs<br />

WWTP Cartuja<br />

Almozara<br />

Parameter<br />

Sewage Origin Industrial and domestic Industrial and domestic<br />

Average flow at design<br />

3.00 0.40<br />

(m 3 s -1 )<br />

Average actual flow in<br />

1.72 0.37<br />

2006 (m 3 s -1 )<br />

<strong>Water</strong> treatment<br />

Primary sedimentation, Biological Primary decantation, Biological<br />

treatment by activated sludge and treatment by activated sludge and<br />

secondary decantation<br />

secondary<br />

decantation,<br />

Phosphorus removal with Iron<br />

Chloride<br />

Sludge treatment Primary and secondary digestion<br />

plus dehydration by filter press<br />

Centrifuge dehydration flowed by<br />

incineration<br />

As it can be seen in table 4 “Almozara” is working near its actual capacity whereas<br />

“Cartuja” seems to be over dimensioned and is working at half <strong>of</strong> its actual capacity.<br />

4.3 Environmental performance <strong>of</strong> <strong>Zaragoza</strong> UWS<br />

4.3.1 Use <strong>of</strong> chemical products<br />

Figure 7 shows the annual consumption <strong>of</strong> chemical products by <strong>Zaragoza</strong> UWS<br />

from 2000 for DWT and from 2001 for WWT. There is a steady trend over these<br />

years, but Chlorine and Allum shows a clear reduction for 2005 and 2006, from<br />

around 3000 to 2500 ton and from 8000 to 6000 ton respectively. PAC use for DWT<br />

started in 2003 and it has not been steady since then.<br />

32

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