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Water TreatmentWater Treatment
CE 326 Principles of Environmental EngineeringCE 326 Principles of Environmental EngineeringDepartment of Civil, Construction and Environmental EngineeringDepartment of Civil, Construction and Environmental Engineering
I St t U i itI St t U i itIowa State UniversityIowa State UniversityMarch 2, 2009March 2, 2009
Tim Ellis, Ph.D., P.E.Tim Ellis, Ph.D., P.E.
Announcements Announcements
• Water Chemistry II Problem Set due todayy
• Schedule change: Wednesday, March 4lab will be part 1 of the water treatment lab will be part 1 of the water treatment plant design
• The Water Treatment Plant Field Trip has • The Water Treatment Plant Field Trip has been moved to Wednesday, March 11
Water Treatment Water Treatment
• Groundwater– hardness (aesthetic consideration)( )– disinfection (required by SDWA)
• Surface Water• Surface Water– turbidity and color removal
filtration (required by SDWA)– filtration (required by SDWA)– disinfection (required by SDWA)
CE 326 Principles of Environmental Engineering, Copyright © 2008 Tim Ellis, Iowa State University
Alkalinity in CoagulationAlkalinity in Coagulation
N d d t t li id f dNeeded to neutralize acid formed
Rapid MixRapid Mix
Rapid Mix Tank In line Blender Static MixerRapid Mix Tank In-line Blender Static Mixer
http://www.postmixing.com/mixing%20forum/Macro/Fluid%20Motion/process_intensifier/images/hga%20model.jpghttp://www.pumppackage.co.uk/images/KOFLO_Page%206/Kofloflowani.gif
Mixing CalculationsMixing Calculations
• Find P for a rapid mix basin where Q=0.05 m3/s; detention time= 60 s, Q / ; ,T=20°C, G=700 s-1;= 1.002 x 10-3 Pa·s
Mixing CalculationsMixing Calculations
h ld d f• How many hp would you need for a flocculation basin to provide a G=100 s-1
l f f d flGt value of 100,000 for a 10 mgd flow (1 mgd = 0.0438 m3/s);
3 h= 0.89 x 10-3Pa·s; 1 hp = 745.7 Watts
Groundwater Treatment PlantTreatment of Groundwater for Hardness Removal
AerationHard WaterCa+2 + Mg+2
to remove CO
RapidMix
SlowMix Recarbonation
addCO2
d Hadd D. O.
Bore Hole
to remove CO2and H 2S Fe2+ → Fe3+ Sedimentation
weir overflow rate: 268-322 m3/m. dsurface overflow rate:
to decrease pH
add lime (for CH)and soda ash (for NCH)raise pH to 10 11 5 Well
surface overflow rate:57-70 m3/m2 . d105-130 m3/m2 . d for upflow solids contact
raise pH to 10 - 11.5 to precip. hardness
to distri-b
Filtration Clear-well
bution
add Cl2 , polyphosphateG values for Rapid Mix: 700-1000 s-1
In-Line blender: 3000-5000 s-1
l f l lE.S. = 0.35 - 0.55 mmU C = 1 3 1 7 and F-Gto values for Flocculation
Type G(s-1) GtoSoftening (10%) 130-200 200,000-250,000Softening (39%) 150-300 390,000-400,000
U.C. = 1.3 - 1.7depth = 0.3 - 0.75loading rate = 120 - 240 m3/m2d
CE 326 Principles of Environmental Engineering, Copyright © 2008 Tim Ellis, Iowa State University
Surface Water Treatment PlantSurface Water Treatment for Turbidity and Color Removal
SedimentationIntake and P St ti
Bacteria, Color,Turbidity
RapidMix
SlowMix
Sedimentationweir overflow rate: surface O. R.: 143-179 m3/m. d light floc 20 - 40 m3/m2 . d179-268 m3/m. d heavy floc
Pump Station
G: 700-1000 s-1
t 30 60flocculationbasin
sedimentationbasin
Streamalum or iron salts for coagulation
add Cl2 or O3 for taste and odor
t: 30-60s basin basin
to distri-
and odor
Filtration Clear-well
bution
add Cl2 , polyphosphate,
G values for Rapid Mix: 700-1000 s-1In-Line blender: 3000-5000 s-1Gto values for Flocculation E.S. = 0.35 - 0.55 mm
U C = 1 3 1 7 and F-
lime for pHType G(s-1) GtoLow turbidity 20-70 60,000-200,000High turbidity 30-80 36,000-96,000
U.C. = 1.3 - 1.7depth = 0.3 - 0.75loading rate = 120 - 240 m3/m2d
CE 326 Principles of Environmental Engineering, Copyright © 2008 Tim Ellis, Iowa State University