FILTRATION CE326 Principles of Environmental Engineering

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Presentation transcript:

FILTRATION CE326 Principles of Environmental Engineering Iowa State University Department of Civil, Construction, and Environmental Engineering Tim Ellis, Associate Professor March 7, 2008

Definitions Filtration: A process for separating s_____________ and c ______________ impurities from water by passage through a porous medium, usually a bed of sand. Most particles removed in filtration are much smaller than the pore size between the sand grains, and therefore, adequate particle d______________ (coagulation) is extremely important.

Filtration Spectrum Microfiltration Ultrafiltration IONS MOLECULES SCANNING ELECTRON MICROSCOPE OPTICAL MICROSCOPE VISIBLE TO NAKED EYE IONS MOLECULES MACRO MOLECULES MICRO PARTICLES MACRO PARTICLES MICRON Angström Molecular weight Sugars Viruses Algae and protozoans Dissolved salts Bacteria Pesticides Colloids Metal ions Sands Humic acids Reverse Osmosis Microfiltration Nanofiltration Ultrafiltration CONVENTIONAL FILTRATION Note : 1 Angström = 10-10 meter = 10-4 micron

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

Media Medium SG sand 2.65 anthracite 1.45 - 1.73 garnet 3.6 - 4.2

History S s filters were introduced in 1804: sand diameter 0.2 mm depth 1 m loading rate 3 - 8 m3/d·m2 low and

Slow Sand Filters S ___________________ - gelatinous matrix of bacteria, fungi, protozoa, rotifera and a range of aquatic insect larvae. As a Schmutzdecke ages, more algae tend to develop, and larger aquatic organisms may be present including some bryozoa, snails and annelid worms.

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

R sand filters were introduced about 1890: effective size 0.35 - 0.55 mm uniformity coef. 1.3 - 1.7 depth 0.3 - 0.75 m loading rate 120 - 240 m3/d·m2 apid

D m filters introduced about 1940: Depth: anthracite (coal) 0.45 m sand 0.3 m loading rate 300 m3/d·m2 ual edia

Fluidized Filter Media Operation Filtration Backwash Backwash water out Fluidized Filter Media Backwash Water Filter Media Filtered Water Underdrain Support

Particle Removal Mechanisms Gravity Inertial Interception Diffusion

Inertia

Particle Removal Mechanisms

Ideal Filter Run Filter Ripening Period (Turbidity < 0.1 NTU in 15 min) Terminal Head loss

Non-Air-Scouring Underdrain 20

Non-Air-Scouring Underdrain 21

Non-Air-Scouring Underdrain 22

Wheeler Block

Air-Scouring Underdrain 24

Leopold Type S™ Technology Underdrain 25

Air-Scouring Underdrain 26

Bachwash Efficiency 5 nozzles/ft2 or 55 nozzles/m2 - acceptable < 4 nozzles/ft2 or 40 nozzles/m2 – large dead zones 24 nozzles/ft2 or 268 nozzles/m2 - good 27

Automatic Backwash Filter

Automatic Backwash Filter

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

- holds 2,400,000 cups of coffee (150,000 gals.) Stanton, Iowa - 96 feet tall. - holds 2,400,000 cups of coffee (150,000 gals.)  - completed in time for Homecoming 2000.  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 celebration she served coffee to the public. Stanton's water tower was converted to a giant Swedish coffeepot the following year.

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