Transcript Lecture 6

Philadelphia University
Faculty of Engineering
Department of Civil Engineering
First Semester, 2013/2014
ENVIRONMENTAL
ENGINEERING
441
Lecture 5:
Water Treatment (3)
Sedimentation & filtration
RAPID MIXING - FLOCCULATION
The process whereby the chemicals are quickly &
uniformly dispensed in the water
 During coagulation and softening, the chemical
reaction that take place in rapid mixing for
precipitation – in less 10-13 second
 For flocculation, enough mixing to bring the flocs
from settling in the basin. To much will shear the
flocs particles so that the flocs is small & finely
dispersed.

SEDIMENTATION -OVERVIEW
Process of heavier solid particles in suspension,
settle to the body of the tank by gravity
 Designed to remove settled water from the basin
without carrying away any of the floc particles.
 Sedimentary Basin/ clarifier are divided into
four zones: Inlet, settling, outlet and sludge
storage

SEDIMENTATION -OVERVIEW
SEDIMENTATION-CONCEPT

Velocity of flowing water (Over flow
rate/surface loading rate( is
proportional to the flow rate divided
by the surface area
o
c
Where,
Vo = water velocity (m/s)
Q = water flow (m3/s)
Ac= cross surface area (m2)
SEDIMENTATION-CONCEPT
Particle removal is dependent on the overflow rate
and independent of the depth of sedimentary tank
 If the particle to be removed from the bottom of the
clarifier and not go out in the settled water, then the
particle settling velocity must be greater than the
over flow rate (Vs>Vo);
Surface Area=A


If (Vs>Vo); 100% removal of particle
If (Vo>Vs); Zero% removal of particle
 Often Vo is set as 50 to 70%


Vo
Vs
For designing a sedimentary tank, first we have to
determine the Vs before set the over flow rate Vo . Vs
is dependent on the type of particles
FILTRATION
Filtration is a process for separating suspended or
colloidal impurities from water by passing
through a porous medium, usually a bed of sand
or other medium.
Settled water (Sedimentation effluent) turbidity
range 1-10 TU – due to residue of flocs particles.
So turbidity need to be reduce to less than 0.3
Common materials for granular bed filters:
Sand (slow, rapid or high)
 Anthracite coal
 Dual media (Coal plus sand)
 Mixed media (coal, sand & garnet)

FILTRATION- FILTER MEDIA

Loading rate
Where,
Vo = water velocity (m/s)
Q = water flow (m3/s)
Ac= cross surface area (m2)
FILTRATION
Slow sand filters
 Low filtration rate with the use of smaller sand
 Filter sand is less uniform
 Particles are removed on the surface of the filter
(forming a mat of materials , called schmultzdecke)
 Schmultzdecke forms a complex of biological
community that degrade some organic compounds.
 Pretreatment is not important
 Require large are of land and are operator intensive
Rapid sand filters ( most common)
 Graded (layered) within the bed to optimize the
passage of water while minimizing the passage of
particulate mater
 Cleaned in place by backwashing process
 Pretreatment to destabilize particles is essential
Dual-media Filters
• Constructed of silica sand and anthracite coal.
• Depth of sand is about 0.3m and coal 0.45 m. Size and
uniformity is selected to produce a distinct separation
after backwashing
• Disadvantage is that filtered materials are held loosely
in the anthracite layer and can dislodge with sudden
changes in hydraulic loading. The material can then
bind to the sand layer
Mixed Media Filters
• The perfect filter is composed of a grading of large
media at the top to small at the base. This is best
achieved by the use of 3 or more media with ranging
size, density and uniformity coefficient
• Typical installation – Overall bed depth 0.75m; 60%
anthracite; 30% silica sand; 10% garnet sand
• Size range from 1.0mm anthracite to 0.15 garnet sand
• Filtration rates range from 10 to 20m/hr