Waste Management Structures: Philippine Agricultural Engineering Standards Agricultural Liquid Waste
Waste Management Structures: Philippine Agricultural Engineering Standards Agricultural Liquid Waste
Waste Management Structures: Philippine Agricultural Engineering Standards Agricultural Liquid Waste
ALINSO, Haskin D.
MADAYAM, Red M.
TIW-AN, Espino C.
SANTIAGO, Filemore C.
Anaerobic
Presence of free oxygen is not required
Clean runoff
Runoff not contaminated with manure such as runoff from roofs, grassed areas, drives
and other areas which are not animal alleys
Disinfection
Process of killing all pathogenic microorganisms
Dissolved
Solids part of total solids passing through the filter in a filtration procedure
Effluent
Liquid waste, partially or completely treated, flowing out of a reservoir, basin, or
wastewater treatment plant
Facultative lagoons
Lagoons that can function as aerobic or anaerobic depending on the environment
Fixed solids
Part of total solids remaining after volatile gases driven off at 600oC
Grit
Non-biodegradable component of liquid waste composed of sand, gravel, cinders or other
heavy solid materials
Holding pond
Storage where liquid waste is stored before final disposal
Influent
Liquid that flows into a containing space
Lagoon
pit in the ground where liquid waste is stored to produce a higher quality effluent
Liners
System of clay layers and/or geosynthetic membranes used to contain leachate and
reduce or prevent contaminant flow to groundwater
Lot runoff
Rainfall containing animal manure
Manure
Accumulated moist animal excrement that does not undergo decomposition or drying; it
include feces and urine which may be mixed with bedding material, spilled feed or soil
Pathogenic microorganism
Microorganism capable of causing diseases
Slurry
Primary treatment Watery mixture of insoluble solid
Treatment that causes substances in liquid waste
to readily settle or float
Secondary treatment
Treatment used to convert dissolved or
suspended materials into a form more readily
separated from the liquid waste being treated
Sludge
Precipitate resulting from coagulation or
sedimentation of liquid waste
Suspended solids
Solids removed by filtration
Total solids
Residue remaining after water is removed from waste material by evaporation
Volatile solids
Part of total solids driven off as volatile gases when heated to 600oC
5-day Bio-Chemical Oxygen Demand (BOD5 )
Quantity of oxygen needed to satisfy biochemical oxidation of organic matter in waste
sample in 5 days at 20oC
Location
The location of liquid waste facility shall conform with the existing zoning, land
use standards, rules and regulations set by Department of Environment and
Natural Resources (AO 34 and 35) and other national policies such as Water Code
(PD 1067) and Environmental Code on Solid and Liquid Waste Disposal (PD 1152).
It shall be constructed on soils with at least 15% clay content. If constructed in
other soil types, sealant shall be provided.
Liquid waste facility should be located so that the prevailing winds tend to
disperse and transport the odor away from residences.
The site shall be provided with landscaping.
Typical Processing Diagrams for Liquid Waste
AERATED TREATED
SLUDGE SOLID LIQUID
HOLDING DISPOSAL WASTE
TANK
Biological Processing Without Primary
Sedimentation c
Conventional Liquid Waste Treatment Plant
SOLID GRID
SLUDGE
SLUDGE
LAND ANAEROBIC FINAL
DRYING
DISPOSAL DIGESTION SETTLING
Reception pit
Flush Alley
To storage
Reception pit or treatment
To storage
or treatment
There should be provision for washing grits to remove the organic materials and
provision for proper disposal of screenings and grits.
ii. Sedimentation Tanks
Tanks should either be rectangular or circular. Length to width ratio of rectangular tanks
should be 3:1 – 5:1.
iii. Setting Channel
Side slopes should be 3:1 or less and the bottom slopes should be 0.1 % - 0.3 % to maintain
low velocities and rapid settling.
Side slopes should be 3:1 or less and the bottom slopes should be 0.1 % - 0.3 % to maintain
low velocities and rapid settling.
For the first 15 m – 30 m section, 0.6 m/s velocity should be designed to settle out
relatively large solids and debris. For the next 30 m – 91 m, the velocity should be as low as
0.15 m/s to settle out smaller solids.
iv. Screening
The organic content of animal waste slurries can be reduced by
filtering. Screened solids can be dried or composted (Refer to PAES
414-2:2002).
v. Evaporation
Dries or dehydrates solids in a pond or can be aided by supplemental
heat in a dryer.
Functional Requirements
6. OIL AND GREASE INTERCEPTOR
The volume for interceptor tank should be 1 – 3 times the average daily
flow rate. Inlet should be situated below the water surface and the
outlet should be placed closer to the bottom of the tank.
7. STORAGE
i. Storage Gutters
Gutters should have a minimum depth of 760
mm and width of 150 mm with a bottom slope of 1%.
ii. StorageTank
Storage capacities should depend on the number and size of animals, amount of dilution by spilled
and cleaning water, amount of runoff to be stored and the desired length of time between emptying.
Tank depth should be the sum of the depth for computed storage capacity plus freeboard above the
lowest inlet opening and additional 0.2 m for the liquid always left in the tank.
Tanks should be designed to withstand all anticipated earth, hydrostatic, and live loads.
Sidewalls and partitions of the tank should be properly
reinforced. For deep tanks, cast-in-place concrete should be
used.
Storage tanks should be provided with a submerged centrifugal
chopper pump.
Covers for tank opening should be non-floating and weigh at
least 18 kg.
Provide a permanent ladder or steps below all openings with a
minimum dimension of 381 mm.
Pit ventilation should be provided to reduce gasses and odors.
iii. Storage Pond
Liquid waste storage ponds and structures shall be sized to hold all of the manure, bedding, and
liquid waste from animal housing, animal and crop processing plants, and contaminated runoff that
can be expected during the storage period.
In addition to the waste volume, there shall be provision for the following depth adjustment to:
Account for a freeboard of 0.3 m.
It shall be the sum of waste volume, minimum treatment volume, and sludge volume for
the treatment period.
Functional Requirements
8. TREATMENT
Crest of spillway or other outflow
device(where permissible)
0.3M
1.5 m Max.
Water source
Holding pond
i. Filtration
The surface area required for filters should be based on the peak filtration and peak plant flow rates.
The width-to-length ratios for filter bed should 1:1 – 1:4.
Filter medium such as sand should have an effective diameter of at least 0.45 mm and shall have a minimum depth of
280 mm.
There should be provision for backwashing to clean the material within the filter effectively. Backwashing should be
achieved using waster backwash with auxiliary surface water-wash agitation, water backwash with auxiliary air scour,
and combined air-water backwashing.
Typical granular-medium
filter:
a) conventional monomedium
downflow filter, and
b) conventional dual-medium
downflow filter
ii. Disinfection
There should be provision for disinfection through the use either
chemical agents, physical agents, mechanical means and radiation.
Disinfection shall be required if the treated wastewater will be
irrigated for food crops unless the crops are processed
commercially prior to use, disinfected effluent is acceptable.
iii. Quality
The quality of the effluent before final disposal to the environment
shall conform with water quality standards of the Department of
Environment and Natural Resources (Refer to DAO No. 35, Series of
1990).
11. SLUDGE TREATMENT
i. Biogas Production
Refer to PAES 413:2001 Agricultural Structures – Biogas Plant.
ii. Drying
The bed should consist of 300 mm fine sand underlaid by 200 mm –
460 mm of gravel.
The sand should have an effective size of 0.3 mm – 0.75 mm, free from
fines and should have a maximum uniformity coefficient of 3.5. The
gravel size should be 2.5 mm – 25 mm.
Underdrains should be 100 mm in diameter and should slope at 1%.
ii. Drying
Beds should be divided every 3 m by 0.6 m partitions. The drying bed
wall should be concrete.
Seepage collected in the underdrains should be returned to the
treatment area with the raw wastewater.
iii. Sludge Lagoon
Sludge lagoon should either be designed for sludge drying,
intermediate storage in conjunction with land application and long-
term storage.
Sludge drying lagoon should have a sludge depth of 0.62 m – 1.25 m.
Storage lagoon should have a depth of 3 m – 5 m and should be
provided with mechanical aerator.
13. ODOR CONTROL
Odor control methods to treat foul air should either with the use of chemical scrubbers, activated
carbon and bulk medium biofilters.
Bulk medium biofilters such as soil, peat and compost should have sufficient porosity, near-uniform
particle size and pH-buffering capacities.