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Biofiltration
Any type of
filter with attached biomass on the filter-media can
be defined as a
Biofilter.
The filtration process in which the pollutants are
removed due to
Biological degradation rather than physical straining
as is the case in
normal filter,
is called Biofiltration.
3.Decay and detachment of microorganisms
2. Growth of microorganism
1. Attachment of microorganism
Organisms attached to medium and grow into dense films of
viscous, jellylike nature.
Mechanisms by which microorganisms can attach and
colonize on the surface of the filter media of a biofilter are:
(i) Transportation,((a) diffusion (Brownian motion), (b)
convection,(c) sedimentation due to gravity, and (d) active
mobility of the microorganisms)
(ii) Initial adhesion, (depending upon the total interaction
energy)
(iii) Firm attachment (depend on influent characteristics
(such as organic type and concentration) and surface
properties of the filter media)
(iv) Colonization (depend on influent characteristics (such as
organic type and concentration) and surface properties of the
filter media)
*Dissolved organics passes into biofilm due to
concentration gradients within film.
*Suspended particles and colloids retain on sticky
surface and decomposed into soluble products.
*Oxygen for aerobic reactions , provided by dissolved
oxygen in WW and from void spaces of medium.
*Waste products diffuse outwards and carried away by
water currents.
*The factors that influence the rate of substrate
utilization within a biofilm are
(i) substrate mass transport to the biofilm,
(ii) diffusion of the substrate into the biofilm, and
(iii) utilization kinetics within the biofilm.
*As the film grows thicker, both anaerobic and
endogenous mechanisms occur at biofilm-medium
surface interface.
*Attachment mechanism weakened.
*Shearing action of WW washes it away. This Process is
called “sloughing”.
*Sloughing is function of hydraulic and organic loading
rate.
*Limiting factor is oxygen diffusivity. Aerobic zones are
limited to 0.1-0.2 mm thickness.
Biofiltration Process
WW flow Rate
Organic loading rate
Rate of diffusivity of substrate
Rate of diffusivity into oxygen
Temperature
Biofilters used in Waste
Water Treatment
Contact Beds
Intermittent
Sand Filters
Trickling
Filters
1.Works in
cycles(alternate
contact of sewage and
air).
2.One cycle lengh=8-12
hrs
3. 80% SS and 60-75%
BOD removal.
4.Rate of loading should
not exceed 110 litres
per day per sqm.
5. Have become almost
obsolete these days.Source: Environmental engineering, S.K.
1.Sewage is applied for
24hrs on one bed then
to another bed.
2.D10 =0.2-0.5 mm &
Cu= 2to5 .
3.Excellent
performance effluent
SS<10ppm,BOD<5ppm.
4.Large area
requirement.
5. Not used these days.
Source: Environmental engineering, S.K.
Garg
A TF consists of a permeable media made of a bed
of rock, slag, or more recently, plastic over which
wastewater is distributed and trickles through.
Single Stage TF
• Carbon oxidation & nitrification take
place in a single TF unit
Two- stage TF
• The first-stage filter and intermediate
clarifier reduce carbonaceous BOD, and
nitrification takes place in the second stage
Biofiltration
Biofiltration
Source: Water Environment Federation (1996),
Biofiltration
Source: Environmental engineering, Metcalf & Eddy
Dosing characteristics of the
distribution system
Choosing the right packing / media
Configuration of the underdrain system
Provision for adequate ventilation
Consists of distributor arms mounted on a pivot
in the center,
These are hollow through which water is
discharged over the filter bed
For uniform distribution the flowrate per unit of
length should be proportional to the radius from
the center
Head loss is in the range of (0.6 –1.5 m)
Dosing tanks must ensure that minimum flow is
sufficient to rotate the distributor & discharge
all wates from nozzles
 A material having high surface area per
unit volume , does not clog easily
Media can be rock , plastic , pvc etc.
Stones less than 25mm not be used as they
do not provide sufficient pore space
Source: Environmental engineering, Metcalf & Eddy
These are waste water collection systems that collects the
filtered waste water & solids discharged from the filter
packing
They ventilate the filter by providing air for the micro-
organisms by being open at least to a circumferential
channel
Should be designed such that forced air vibrations can be
added later
Air flow:
Natural draft
Forced air ventilator
Source: Environmental engineering, S.K. Garg
Because of their large air-water interface can
remove CO2,H2S, N2 & other gases
A portion of liquid in underdrain system is
recycled:
It improves the treatment efficiency
To dilute strength of incoming wastewater
To maintain enough wetting of slime layer
Prevents ponding in filter
Suitable for shock loads
Low running cost
Additional treatment may be needed to meet
more stringent discharge standards
Generates sludge that must be treated and
disposed of
Regular operator attention needed
 Relatively high incidence of clogging
 Relatively low loadings required depending on
the media
Limited flexibility and control in comparison with
activated sludge processes
Potential for vector and odour problems
Trickling filters running at low organic loading
are found to have nitrification(Stequist et al. 1974;
Parker and Richards, 1986)
Heterotrophic bacteria have high yield coefficient
and high growth rate are competitive than
nitrifying bacteria
Significant nitrification occurs when BOD is
appreciably reduced. BOD had to be less than 30
mg/L to initiate nitrification and less than 15 mg/L
for complete nitrification(Bruce et al., 1975)
Fly nuisance
Odor nuisance
Ponding trouble
Icing
Biofiltration

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Biofiltration

  • 2. Any type of filter with attached biomass on the filter-media can be defined as a Biofilter. The filtration process in which the pollutants are removed due to Biological degradation rather than physical straining as is the case in normal filter, is called Biofiltration.
  • 3. 3.Decay and detachment of microorganisms 2. Growth of microorganism 1. Attachment of microorganism
  • 4. Organisms attached to medium and grow into dense films of viscous, jellylike nature. Mechanisms by which microorganisms can attach and colonize on the surface of the filter media of a biofilter are: (i) Transportation,((a) diffusion (Brownian motion), (b) convection,(c) sedimentation due to gravity, and (d) active mobility of the microorganisms) (ii) Initial adhesion, (depending upon the total interaction energy) (iii) Firm attachment (depend on influent characteristics (such as organic type and concentration) and surface properties of the filter media) (iv) Colonization (depend on influent characteristics (such as organic type and concentration) and surface properties of the filter media)
  • 5. *Dissolved organics passes into biofilm due to concentration gradients within film. *Suspended particles and colloids retain on sticky surface and decomposed into soluble products. *Oxygen for aerobic reactions , provided by dissolved oxygen in WW and from void spaces of medium. *Waste products diffuse outwards and carried away by water currents. *The factors that influence the rate of substrate utilization within a biofilm are (i) substrate mass transport to the biofilm, (ii) diffusion of the substrate into the biofilm, and (iii) utilization kinetics within the biofilm.
  • 6. *As the film grows thicker, both anaerobic and endogenous mechanisms occur at biofilm-medium surface interface. *Attachment mechanism weakened. *Shearing action of WW washes it away. This Process is called “sloughing”. *Sloughing is function of hydraulic and organic loading rate. *Limiting factor is oxygen diffusivity. Aerobic zones are limited to 0.1-0.2 mm thickness.
  • 8. WW flow Rate Organic loading rate Rate of diffusivity of substrate Rate of diffusivity into oxygen Temperature
  • 9. Biofilters used in Waste Water Treatment Contact Beds Intermittent Sand Filters Trickling Filters
  • 10. 1.Works in cycles(alternate contact of sewage and air). 2.One cycle lengh=8-12 hrs 3. 80% SS and 60-75% BOD removal. 4.Rate of loading should not exceed 110 litres per day per sqm. 5. Have become almost obsolete these days.Source: Environmental engineering, S.K.
  • 11. 1.Sewage is applied for 24hrs on one bed then to another bed. 2.D10 =0.2-0.5 mm & Cu= 2to5 . 3.Excellent performance effluent SS<10ppm,BOD<5ppm. 4.Large area requirement. 5. Not used these days. Source: Environmental engineering, S.K. Garg
  • 12. A TF consists of a permeable media made of a bed of rock, slag, or more recently, plastic over which wastewater is distributed and trickles through. Single Stage TF • Carbon oxidation & nitrification take place in a single TF unit Two- stage TF • The first-stage filter and intermediate clarifier reduce carbonaceous BOD, and nitrification takes place in the second stage
  • 15. Source: Water Environment Federation (1996),
  • 18. Dosing characteristics of the distribution system Choosing the right packing / media Configuration of the underdrain system Provision for adequate ventilation
  • 19. Consists of distributor arms mounted on a pivot in the center, These are hollow through which water is discharged over the filter bed For uniform distribution the flowrate per unit of length should be proportional to the radius from the center Head loss is in the range of (0.6 –1.5 m) Dosing tanks must ensure that minimum flow is sufficient to rotate the distributor & discharge all wates from nozzles
  • 20.  A material having high surface area per unit volume , does not clog easily Media can be rock , plastic , pvc etc. Stones less than 25mm not be used as they do not provide sufficient pore space
  • 22. These are waste water collection systems that collects the filtered waste water & solids discharged from the filter packing They ventilate the filter by providing air for the micro- organisms by being open at least to a circumferential channel Should be designed such that forced air vibrations can be added later Air flow: Natural draft Forced air ventilator
  • 24. Because of their large air-water interface can remove CO2,H2S, N2 & other gases A portion of liquid in underdrain system is recycled: It improves the treatment efficiency To dilute strength of incoming wastewater To maintain enough wetting of slime layer Prevents ponding in filter Suitable for shock loads Low running cost
  • 25. Additional treatment may be needed to meet more stringent discharge standards Generates sludge that must be treated and disposed of Regular operator attention needed  Relatively high incidence of clogging  Relatively low loadings required depending on the media Limited flexibility and control in comparison with activated sludge processes Potential for vector and odour problems
  • 26. Trickling filters running at low organic loading are found to have nitrification(Stequist et al. 1974; Parker and Richards, 1986) Heterotrophic bacteria have high yield coefficient and high growth rate are competitive than nitrifying bacteria Significant nitrification occurs when BOD is appreciably reduced. BOD had to be less than 30 mg/L to initiate nitrification and less than 15 mg/L for complete nitrification(Bruce et al., 1975)

Editor's Notes

  • #5: The mechanisms by which microorganisms can attach and colonize on the surface of the filter media of a biofilter are (i) transportation, (ii) initial adhesion, (iii) firm attachment, and (iv) colonization [Van Loosdrecht et al., 1990]. The transportation of microorganisms to the surface of the filter media is further controlled by four main processes, (a) diffusion (Brownian motion), (b) convection, (c) sedimentation due to gravity, and (d) active mobility of the microorganisms. As soon as the microorganisms reach the surface, initial adhesion occurs which can be reversible or irreversible depending upon the total interaction energy, which is the sum of Van der waals force and electrostatic force. The DLVO (Derjaguin-Landau-Verwey- Overbeek) theory is often used to describe the adhesion of the microorganisms on the surface of the filter media. The processes of firm attachment and colonization of microorganisms depend on influent characteristics (such as organic type and concentration) and surface properties of the filter media. The steric effects, hydrophobicity of the microorganisms, contact angle, and electrophoretic mobility values are taken into consideration to estimate the attachment of microorganisms on the surface of filter media.
  • #6: A biofilm is an accumulation of microorganism onto a surface. Since the microorganisms are attached to the surface, the supply of organics or substrate (food) to the microorganisms in a biofilm is mainly controlled by the bulk and surface transport phenomena. The substrate must be transported from the bulk liquid to the biofilms outer surface where it has to diffuse into the biofilm for its metabolism. The factors that influence the rate of substrate utilization within a biofilm are (i) substrate mass transport to the biofilm, (ii) diffusion of the substrate into the biofilm, and (iii) utilization kinetics within the biofilm.
  • #11: 20-40mm particle size 1 to 1.
  • #12: May be used for smaller quantity of sewer and hospital waste.