N.J. Admin. Code § 7:14A-23.19 - Trickling filters
(a) Trickling filters of
the "standard rate" or "high rate" type may be used for the treatment of sewage
amenable to treatment by a biological process.
(b) Filters shall be preceded by effective
preliminary treatment and shall be followed by individually controlled and
mechanically cleaned settling tanks.
(c)
When the average five-day B.O.D. of the raw sewage exceeds 325 parts per million,
two stages of trickling filter treatment are required, with or without intermediate
sedimentation. Consideration may be given to designs providing supplementary
preliminary treatment in the case of strong sewages or industrial wastes.
(d) The sewage shall be distributed uniformly over
the filter so that at least 95 percent of the surface area receives sewage directly.
1. Distribution devices may be actuated by twin
siphons, pumps or gravity discharge from preceding treatment plant units.
(e) The filter media may be crushed
rock, manufactured material, or other approved material. Manufactured media shall be
resistant to ultraviolet degradation, disintegration, erosion, aging, all common
acids and alkalies, organic compounds, and fungus and biological attack. In
addition, manufactured media shall be structurally capable of supporting a person's
weight or a suitable walkway shall be provided to allow for distributor maintenance.
1. Where applicable, the upper 18 inches of the
filter bed shall have a loss, measured by the 20-cycle sodium sulfate test, of less
than ten percent and the balance shall pass the 15-cycle test.
2. Wear shall not exceed 20 percent after 500
revolutions of Los Angeles Rattler Test as determined by the current ASTM Standard,
Designation No. C-131.
3. Rock media
shall be approximately cubical in shape, free from dust, clay, sand or fine material
and of a size that passes a four-inch screen and is retained on a 2 1/2 inch
screen.
4. Material shall be screened or
forked, and washed to remove fine grains and shall be so placed as to avoid breaking
the underdrains.
(f) The
underdrainage system shall be resistant to the action of sewage wastes and shall
cover the entire floor. Inlet openings into the underdrains shall have an
unsubmerged gross combined area equal to at least 15 percent of the surface area of
the filter. Use of half-tile for underdrains will not be approved.
1. Lateral underdrains shall have a minimum slope
of one percent.
2. Main underdrains and
effluent channels shall be designed to provide a velocity of not less than two feet
per second.
3. The entire underdrainage
system shall be designed to permit free passage of air, and be of such size that not
more than 50 percent of the cross sectional area of the flow channels in the
underdrains will be submerged during operation of the filter at the maximum design
rate. Provisions shall be made for flushing lateral underdrains from the main drain
or head channel.
(g) Standard
rate trickling filters shall be designed as follows:
1. The volume of sewage to be treated by standard
rate filters shall not exceed 14,400 gallons per day per 1,000 cubic feet of
filtering media and the average rate of organic loading shall not exceed 15 pounds
of five-day B.O.D. per thousand cubic feet per day.
2. The average rate of application during dosing
periods shall not exceed 22 gallons per thousand cubic feet of media per minute. The
time intervals between dosing cycles to the filter shall not exceed five minutes at
design flow.
3. The minimum depth of
filtering media at any point in the filter, measured from the top of the underdrains
to the surface of the media, shall not be less than five feet, and the maximum depth
shall not exceed eight feet.
4. Means
for Psychoda fly control, such as provisions for backflooding and filter flushing,
shall be provided. The application of chemicals is discouraged unless other forms of
control have been ineffective and the use of chemicals shall be in conformance with
all other applicable laws, ordinances and regulations.
5. Means shall be provided for recirculating a
portion of the effluent from intermediate or final settling tanks during periods of
low flow.
6. The Department will
consider other suggested loading rates to address manufactured media if supported by
appropriate engineering documentation.
(h) High rate trickling filters shall be designed
as follows:
1. Organic loading to high rate filters
shall not exceed 67 pounds of five-day B.O.D. per thousand cubic feet of filter
media per day, based on the total volume of the filters.
2. The depth of filtering media at any point in
the filter, measured from the top of the underdrain block to the surface of the
media, shall not be less than five feet nor more than eight feet. The distributor
shall clear the media by not less than eight to nine inches; and the filter
retaining walls shall not be less than three inches higher than the media.
3. High rate trickling filters shall be equipped
with rotary distributors and flushing devices shall be provided at the outer end of
each distributor arm.
4. Provisions
shall be made for controlled recirculation to maintain a continuous application rate
of not less than 230,000 gallons per 1,000 square feet per day. Devices to measure
flows to the filter and the recirculated effluent shall be provided.
5. The number and capacities of the recirculation
pumps shall be such that the conditions of (h)4 above can be met if the largest pump
for each point of return is out of service unless other provisions are made which
will achieve adequate and effective degree of treatment if power or pump failure
occurs.
6. The Department will consider
other suggested loading rates to address manufactured media if supported by
appropriate engineering documentation.
(i) Under conditions where treatment of unusually
strong sewage is necessary and two-stage filtration is adopted, intermediate
settling tanks may be required, with suitable sludge and scum removal devices to
provide a detention period of one hour based upon projected flow.
Notes
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