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SEDIMENTATION & SEDIMENTATION & SEDIMENTATION & SEDIMENTATION & FILTRATION FILTRATION FILTRATION FILTRATION CE326 Principles of Environmental Engineering CE326 Principles of Environmental Engineering Iowa State University Iowa State University Department of Civil, Construction, and Department of Civil, Construction, and Environmental Engineering Environmental Engineering Tim Ellis, Associate Professor Tim Ellis, Associate Professor March 6 2009 March 6 2009 March 6, 2009 March 6, 2009
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Page 1: SEDIMENTATION &SEDIMENTATION & FILTRATION

SEDIMENTATION &SEDIMENTATION &SEDIMENTATION & SEDIMENTATION & FILTRATIONFILTRATIONFILTRATIONFILTRATION

CE326 Principles of Environmental EngineeringCE326 Principles of Environmental EngineeringIowa State UniversityIowa State University

Department of Civil, Construction, and Department of Civil, Construction, and p , ,p , ,Environmental Engineering Environmental Engineering

Tim Ellis, Associate ProfessorTim Ellis, Associate ProfessorMarch 6 2009March 6 2009March 6, 2009March 6, 2009

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AnnouncementsAnnouncementsAnnouncementsAnnouncements

Jar test and Chlorination Lab due today byJar test and Chlorination Lab due today by Jar test and Chlorination Lab due today by Jar test and Chlorination Lab due today by 5 pm5 pm

Next week field trip to Ames Water PlantNext week field trip to Ames Water PlantNext week field trip to Ames Water PlantNext week field trip to Ames Water Plant 22ndnd exam tentatively scheduled for Friday, exam tentatively scheduled for Friday,

M h 27M h 27ththMarch 27March 27thth

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SEDIMENTATION ( cont’d)SEDIMENTATION ( cont’d)SEDIMENTATION ( cont d)SEDIMENTATION ( cont d)

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DefinitionsDefinitionsDefinitionsDefinitions

Filtration: A process for separating Filtration: A process for separating s_____________ and c ______________ impurities from water by passage through a p______ medium, usually a bed of s_____.

Most particles removed in filtration are much s_______ than the p____ s____ between the sand grains, and therefore, adequate particle d (coagulation) is extremelyd________________ (coagulation) is extremely important.

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Filtration SpectrumFiltration Spectrum

MICRON

IONSIONS MOLECULESMOLECULES MACRO MOLECULESMACRO MOLECULES MICRO PARTICLESMICRO PARTICLES MACRO PARTICLESMACRO PARTICLES

VISIBLE TO NAKED EYEVISIBLE TO NAKED EYEOPTICAL MICROSCOPEOPTICAL MICROSCOPESCANNING ELECTRON MICROSCOPESCANNING ELECTRON MICROSCOPE

Sugars

Molecularweight

Viruses

Angström

Algae and protozoans

Bacteria

ColloidsM t l i

Pesticides

Dissolved salts

Sugars Viruses

Sands

Humic acids

Metal ions

Reverse Osmosis Microfiltration

Ultrafiltration CONVENTIONAL FILTRATION

Note : 1 Angström = 10-10 meter = 10-4 micron

Nanofiltration

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PerformancePerformancePerformancePerformance

The influent The influent t__________ ranges from 1 - 10 NTUfrom 1 10 NTU (nephelometric turbidity units) with a typicalunits) with a typical value of 3 NTU. Effluent turbidity is aboutturbidity is about ______ NTU.

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MediaMediaMediaMedia

Medium SG d 2 65 sand 2.65

anthracite 1.45 - 1.73 garnet 3.6 - 4.2

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HistoryHistoryHistoryHistory

S s filters were introduced inlow and S s filters were introduced in 1804:

sand diameter 0 2 mm

low and

sand diameter 0.2 mm depth 1 m loading rate 3 - 8 m3/d·m2

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Slow Sand FiltersSlow Sand FiltersSlow Sand FiltersSlow Sand Filters S ___________________

- gelatinous matrix of bacteria- gelatinous matrix of bacteria, fungi, protozoa, rotifera and a range of aquatic insect larvae. g q

As a Schmutzdecke ages, more a____ tend to develop, and larger aquatic organisms may be present including some bryozoa,

il d lidsnails and annelid w______.

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http://water.shinshu-u.ac.jp/e_ssf/e_ssf_link/usa_story/12Someyafilteralgae.jpg

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R sand filters were introduced about 1890:

apid

effective size 0.35 - 0.55 mm uniformity coef 1 3 1 7 uniformity coef. 1.3 - 1.7 depth 0.3 - 0.75 m loading rate 120 - 240 m3/d·m2

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D m filters introduced about 1940:ual ediaD m filters introduced about 1940: Depth:

th it ( l) 0 45

ual edia

anthracite (coal) 0.45 m sand 0.3 m loading rate 300 m3/d·m2

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Pathogen Removal During Pathogen Removal During Fil iFil iFiltrationFiltration

poliovirus removal with filtration but poliovirus removal with filtration but without coagulation: 1-50%

poliovirus removal with filtration and with poliovirus removal with filtration and with coagulation: 90-99%C t idi t l ithCryptosporidium oocysts removal with filtration without coagulation: 90%

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OperationOperationOperation Operation FiltrationFiltration BackwashBackwashFiltrationFiltration BackwashBackwash

Backwash water out

Filter Media

Fluidized Filter Media

Backwash Water

Filtered WaterUnderdrain SupportUnderdrain Support

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Particle Removal MechanismsParticle Removal MechanismsParticle Removal MechanismsParticle Removal Mechanisms

GravityGravityGravityGravity InertialInertial

I t tiI t ti InterceptionInterceptionDiffusionDiffusion

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InertiaInertia

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Particle Removal MechanismsParticle Removal MechanismsParticle Removal MechanismsParticle Removal Mechanisms100

BrownianBrownianInterceptionGravityTotalC

*

10

mov

al a

s p

1

Parti

cle

rem

P

0.1 1 10 1000.1

Particle Diameter (m)

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Ideal Filter RunIdeal Filter RunIdeal Filter RunIdeal Filter RunFilter Ripening Period(T bidi 0 1 NTU i 15 i )

Terminal Head loss

(Turbidity < 0.1 NTU in 15 min)

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NonNon--AirAir--Scouring UnderdrainScouring Underdrain

26

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NonNon--AirAir--Scouring UnderdrainScouring UnderdrainNonNon AirAir Scouring UnderdrainScouring Underdrain

27

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NonNon--AirAir--Scouring UnderdrainScouring Underdrain

28

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WheelerWheelerWheeler Wheeler BlockBlock

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AirAir--Scouring UnderdrainScouring UnderdrainAirAir Scouring UnderdrainScouring Underdrain

30

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Leopold Type SLeopold Type S™™ Technology Technology UnderdrainUnderdrainUnderdrainUnderdrain

31

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AirAir--Scouring UnderdrainScouring Underdrain

32

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Bachwash EfficiencyBachwash EfficiencyBachwash EfficiencyBachwash Efficiency

• 5 nozzles/ft2 or 55 nozzles/m2 - acceptable • 24 nozzles/ft2 or 268 nozzles/m2 -good

33

• < 4 nozzles/ft2 or 40 nozzles/m2 – large dead zones

good

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Automatic Backwash FilterAutomatic Backwash Filter

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Automatic Backwash FilterAutomatic Backwash Filter

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first elevated steel first elevated steel water tank west of the water tank west of the Mississippi RiverMississippi RiverMississippi RiverMississippi River

erected in 1897 under erected in 1897 under the supervision and the supervision and ppdesign of Anson design of Anson MarstonMarston

constructed due to aconstructed due to a constructed due to a constructed due to a severe water shortage severe water shortage in 1895 that required in 1895 that required cancellation of classescancellation of classescancellation of classescancellation of classes

tank holds 162,000 US tank holds 162,000 US gallonsgallons

1978, the water tower 1978, the water tower was disconnected was disconnected when the universitywhen the universitywhen the university when the university switched to municipal switched to municipal waterwater

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Water Towers, 1951-1970, Water District No. 54Located on the north side of the Des Moines Field House, ,near the current skateboard park

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Stanton, IowaHollywood screen and TV personality Stanton, Iowa- 96 feet tall.- holds 2,400,000 cups of coffee (150,000 gals.)

l t d i ti f

Hollywood screen and TV personality Virginia Christine, "Mrs. Olson" of coffee commercial fame, was one of Stanton's famous daughters. At the time of our centennial in 1970, Virginia came home to be our parade marshal. During the

- completed in time for Homecoming 2000.

p gcelebration she served coffee to the public. Stanton's water tower was converted to a giant Swedish coffeepot the following year.

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Adair, IowaHelm, CaliforniaAtlanta, Illinois

Markle, Indiana Ironwood, Michigan

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