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ROTATING
BIOLOGICAL
CONTACTORS
OVERVIEW
 Wastewater treatment processes in use
today may be broadly categorized as either
fixed film processes or suspended growth
processes.
 RBCs may be the best process choice for
some wastewater treatment plants because
of their proven simplicity, reliable
performance, and low energy usage
(particularly important when considering
LEED qualification).
Q1. HOW DOES THE
ROTATING BIOLOGICAL
CONTACTOR SYSTEM WORK?
Q2. WHY ARE FIXED FILM
SYSTEMS, SUCH AS RBCS,
BECOMING MORE POPULAR?
 Low Energy Usage
 Process Stability with Load Variations
 Low Solids Generation
 More Reliable Liquid/Solids Separation
 Easy to Operate
 No Sludge Return
 Less Land Required
Q3. CAN RBCS
PRODUCE HIGH QUALITY
EFFLUENT?
“Properly designed the RBC system can
achieve superior performance to suspended
growth biological treatment systems as well
as other fixed film systems due to lower
organic loading per mass of biological solids,
longer solids detention time, and better
control of short circuiting.” (emphasis added)
United States Environmental Protection
Agency (1992) Rotating Biological
Contactors, EPA/540/S-92/007, Washington.
Q4. CAN RBCS BE USED
FOR LARGER WASTEWATER
TREATMENT PLANTS?
Peoria, Illinois,
where eighty
four (84), 8
meter long, 3
meter diameter
RBCs are used
to remove
ammonia from
a design
average flow of
37 mgd
(140,000 cubic
meters per
day).
Q5. CAN THE ENERGY SAVINGS
OF RBCS BE QUANTIFIED?
RBC
 0.0023 lbs of BOD per square
foot of disc surface area.
 motors drawing 3 kW per
100,000 square feet of disc
surface area.
 will need approximately
26,700,000 square feet of
disc surface area.
 approximately 800 kW of
power
ASP
 1.2 pounds of oxygen per
pound of BOD removed.
 need to generate 75,000
pounds of oxygen per day.
 1 kWh of power is required to
provide approximately 2
pounds of oxygen.
 This will require 1,500 kW of
power.
 Process total over 1,650 kW
Designing a plant for 30 mgd, 250 mg/l of BOD (62,000 pounds per day)
Q6. HOW DO RBCS REDUCE THE
COST OF OTHER PLANT
PROCESSES?
By the nature of the excess biosolids
 ASP sludge finely divided nature and occasional problems with
filamentous bacteria.
 RBCs, on the other hand, generate larger, more rapidly settling
sludge particles.
 Secondary clarifiers for RBC plants approx. 20% smaller than for
activated sludge plants.
 Difference in solids separation also leads to reduced operator
attention.
 RBC sludge is more concentrated than waste activated sludge
and thickens better.
 Volume reduction of approx. 25%.
 reduces the size of sludge processing facilities, such as digesters
by a similar percentage and can also reduce operating costs.
Q7. HOW MUCH LESS LAND
IS USED BY THE RBC PROCESS
THAN THE ACTIVATED SLUDGE
PROCESS?
RBC
 26,700,000 square feet of
RBC media are required.
 A 10 foot by 25 foot tank
will contain 100,000
square feet of media.
 Therefore, 270 RBCs are
needed, occupying a
surface area of
approximately 98,000
square feet, including
three feet on all sides of
the tank.
ASP
 An aeration basin with
about 8 hours of detention
time is needed.
 For 15 feet deep basin,
the area required is
90,000 square feet.
 The blower and control
building will typically
occupy approximately
10,000 square feet.
Q8. CAN RBCS PROVIDE
NUTRIENT REMOVAL SIMILAR TO
THAT PROVIDED BY ACTIVATED
SLUDGE SYSTEMS?
 For ammonia conversion to nitrates (nitrification),
more surface area must be provided, just as more
microorganisms (higher sludge age) are required
for activated sludge to nitrify. For nitrogen
removal, submerged RBCs are used following
nitrification.
 With regard to phosphorus removal, conventional
biological processes remove phosphorus with
excess cell mass. If further phosphorus removal
is required, the addition of iron or aluminum salts
to RBCs is the way in which phosphorus levels
can be reduced to less than 1 mg/l.
Q9. WHY ARE FIXED FILM
SYSTEMS MORE RESISTANT TO
PROCESS UPSETS THAN ACTIVATED
SLUDGE?
RBCs are more resistant to process upsets for
two reasons:
1. The microorganisms are attached to the media
and are not washed out of the system by high
flows. Also, since the microorganisms are
attached to the media, recovery from toxic
discharge upsets is much more rapid.
2. Second, there are more kilograms of
microorganisms in an RBC plant than an
activated sludge plant. The more microorganisms
in a system the better able it is to withstand
increased organic loads and toxic discharges.
Q10. WHY HAS THE
WASTEWATER INDUSTRY PRIMARILY
USED ACTIVATED SLUDGE
TREATMENT?
 Fixed film processes, mainly rock trickling filters,
predominated formerly. Drawbacks:
 Plugging
 Odors
 Seasonally poor performance
Relatively tall, plastic media trickling filter facilities.
Rotating biological contactors, which were
developed as an even more energy efficient
fixed film process than synthetic media trickling
filters, were developed in the late 1960s and
began to be commercialized in the mid-1970s.
Q11. HOW MUCH LESS
OPERATION AND MAINTENANCE
ATTENTION IS REQUIRED BY AN
RBC SYSTEM THAN AN ACTIVATED
SLUDGE SYSTEM?
 Little operator intervention and monitoring and
generally use simple, low maintenance equipment.
 A typical ASP requires continual monitoring of :
 the wastewater quality
 type of microorganisms in the aeration basin
 the amount of dissolved oxygen in the aeration basin
 the rate at which the biological solids settle and how
well they compact
 high speed rotating equipment and aeration devices
that require frequent maintenance.
A plant treating
approximately
2.5 mgd using
an RBC
process would
use less than
one-half the
labor required
by a
conventional
activated
sludge plant
using
mechanical
aeration
- “Treatability
Q12. HOW IS THE RBC
PROCESS DESIGNED?
Key considerations:
 Mass transfer of oxygen and substrate to the microorganisms growing on the
discs.
 Overall mass of microorganisms in the system in relation to the BOD,
ammonia, and/or nitrogen.
First stage limited
by oxygen
transfer, organic
loading must be
limited.
The overall RBC
surface area is
then dependent on
the effluent results
required.
Determined using
2 dimensional
mass transfer
models, such as
Biowin, GPS-X, or
Pro2D.
More stages may
be required for
nitrification
(ammonia to
nitrate).
Submerged discs
are used to
achieve
denitrification
(nitrate to nitrogen
gas).
THANK YOU

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Rbc

  • 2. OVERVIEW  Wastewater treatment processes in use today may be broadly categorized as either fixed film processes or suspended growth processes.  RBCs may be the best process choice for some wastewater treatment plants because of their proven simplicity, reliable performance, and low energy usage (particularly important when considering LEED qualification).
  • 3. Q1. HOW DOES THE ROTATING BIOLOGICAL CONTACTOR SYSTEM WORK?
  • 4. Q2. WHY ARE FIXED FILM SYSTEMS, SUCH AS RBCS, BECOMING MORE POPULAR?  Low Energy Usage  Process Stability with Load Variations  Low Solids Generation  More Reliable Liquid/Solids Separation  Easy to Operate  No Sludge Return  Less Land Required
  • 5. Q3. CAN RBCS PRODUCE HIGH QUALITY EFFLUENT? “Properly designed the RBC system can achieve superior performance to suspended growth biological treatment systems as well as other fixed film systems due to lower organic loading per mass of biological solids, longer solids detention time, and better control of short circuiting.” (emphasis added) United States Environmental Protection Agency (1992) Rotating Biological Contactors, EPA/540/S-92/007, Washington.
  • 6. Q4. CAN RBCS BE USED FOR LARGER WASTEWATER TREATMENT PLANTS?
  • 7. Peoria, Illinois, where eighty four (84), 8 meter long, 3 meter diameter RBCs are used to remove ammonia from a design average flow of 37 mgd (140,000 cubic meters per day).
  • 8. Q5. CAN THE ENERGY SAVINGS OF RBCS BE QUANTIFIED? RBC  0.0023 lbs of BOD per square foot of disc surface area.  motors drawing 3 kW per 100,000 square feet of disc surface area.  will need approximately 26,700,000 square feet of disc surface area.  approximately 800 kW of power ASP  1.2 pounds of oxygen per pound of BOD removed.  need to generate 75,000 pounds of oxygen per day.  1 kWh of power is required to provide approximately 2 pounds of oxygen.  This will require 1,500 kW of power.  Process total over 1,650 kW Designing a plant for 30 mgd, 250 mg/l of BOD (62,000 pounds per day)
  • 9. Q6. HOW DO RBCS REDUCE THE COST OF OTHER PLANT PROCESSES? By the nature of the excess biosolids  ASP sludge finely divided nature and occasional problems with filamentous bacteria.  RBCs, on the other hand, generate larger, more rapidly settling sludge particles.  Secondary clarifiers for RBC plants approx. 20% smaller than for activated sludge plants.  Difference in solids separation also leads to reduced operator attention.  RBC sludge is more concentrated than waste activated sludge and thickens better.  Volume reduction of approx. 25%.  reduces the size of sludge processing facilities, such as digesters by a similar percentage and can also reduce operating costs.
  • 10. Q7. HOW MUCH LESS LAND IS USED BY THE RBC PROCESS THAN THE ACTIVATED SLUDGE PROCESS? RBC  26,700,000 square feet of RBC media are required.  A 10 foot by 25 foot tank will contain 100,000 square feet of media.  Therefore, 270 RBCs are needed, occupying a surface area of approximately 98,000 square feet, including three feet on all sides of the tank. ASP  An aeration basin with about 8 hours of detention time is needed.  For 15 feet deep basin, the area required is 90,000 square feet.  The blower and control building will typically occupy approximately 10,000 square feet.
  • 11. Q8. CAN RBCS PROVIDE NUTRIENT REMOVAL SIMILAR TO THAT PROVIDED BY ACTIVATED SLUDGE SYSTEMS?  For ammonia conversion to nitrates (nitrification), more surface area must be provided, just as more microorganisms (higher sludge age) are required for activated sludge to nitrify. For nitrogen removal, submerged RBCs are used following nitrification.  With regard to phosphorus removal, conventional biological processes remove phosphorus with excess cell mass. If further phosphorus removal is required, the addition of iron or aluminum salts to RBCs is the way in which phosphorus levels can be reduced to less than 1 mg/l.
  • 12. Q9. WHY ARE FIXED FILM SYSTEMS MORE RESISTANT TO PROCESS UPSETS THAN ACTIVATED SLUDGE? RBCs are more resistant to process upsets for two reasons: 1. The microorganisms are attached to the media and are not washed out of the system by high flows. Also, since the microorganisms are attached to the media, recovery from toxic discharge upsets is much more rapid. 2. Second, there are more kilograms of microorganisms in an RBC plant than an activated sludge plant. The more microorganisms in a system the better able it is to withstand increased organic loads and toxic discharges.
  • 13. Q10. WHY HAS THE WASTEWATER INDUSTRY PRIMARILY USED ACTIVATED SLUDGE TREATMENT?  Fixed film processes, mainly rock trickling filters, predominated formerly. Drawbacks:  Plugging  Odors  Seasonally poor performance Relatively tall, plastic media trickling filter facilities. Rotating biological contactors, which were developed as an even more energy efficient fixed film process than synthetic media trickling filters, were developed in the late 1960s and began to be commercialized in the mid-1970s.
  • 14. Q11. HOW MUCH LESS OPERATION AND MAINTENANCE ATTENTION IS REQUIRED BY AN RBC SYSTEM THAN AN ACTIVATED SLUDGE SYSTEM?  Little operator intervention and monitoring and generally use simple, low maintenance equipment.  A typical ASP requires continual monitoring of :  the wastewater quality  type of microorganisms in the aeration basin  the amount of dissolved oxygen in the aeration basin  the rate at which the biological solids settle and how well they compact  high speed rotating equipment and aeration devices that require frequent maintenance. A plant treating approximately 2.5 mgd using an RBC process would use less than one-half the labor required by a conventional activated sludge plant using mechanical aeration - “Treatability
  • 15. Q12. HOW IS THE RBC PROCESS DESIGNED? Key considerations:  Mass transfer of oxygen and substrate to the microorganisms growing on the discs.  Overall mass of microorganisms in the system in relation to the BOD, ammonia, and/or nitrogen. First stage limited by oxygen transfer, organic loading must be limited. The overall RBC surface area is then dependent on the effluent results required. Determined using 2 dimensional mass transfer models, such as Biowin, GPS-X, or Pro2D. More stages may be required for nitrification (ammonia to nitrate). Submerged discs are used to achieve denitrification (nitrate to nitrogen gas).