UFC 3-280-03
23 JULY 2003
Parameter1,2
Applicability
Typical Design
Conditions2
Typically sized to are 1.5
-Filter Media Acid Wash
Used as required to reduce lime scaling
times the capacity of the
(Subparagraph 2-4.6.3.2)
on filter media for lime conditioning
press.
applications.
-Compressed Air
(Subparagraph 2-4.6.4)
Instrument Air
Used as required for pneumatic control.
Typically requires 690 kPa
pressure.
Air Blow/Core Blow
Used as desired to reduce excessive
filter media washing and provide drier
sludge cake.
690-1380 kPa.
Membrane Air
Typically used with variable-volume
Inflation
presses for no more than 150 psi
pressure applications.
Filter Press Control
Application specific.
Applicable type (i.e., manual,
Systems (Paragraph 2-10)
semiautomatic, and automatic systems)
based on the degree of desired
and use of accessories and auxiliary
systems.
Sludge Cake Handling and
Typically involves only direct discharge
4 days' minimum storage
Storage
into storage container.
required if no other
dewatering facilities exist.
(Paragraph 2-4.10)
Sludge Cake Transport
Application specific.
Typically involves use of either
(Paragraph 2-4.11)
conveyor, auger, or sludge cake
pumping system when further sludge
treatment is required.
Sludge Cake Disposal
Application specific.
Several ultimate disposal methods are
(Paragraph 2-4.12)
available and are dependent on the
specific sludge generated.
1
More details are provided on design considerations and specific applications in the paragraphs
referenced.
2
Conversion Factors:
1 kPa = 0.15 psi
1 kg/m2 = 0.2 lb/ft2
1 L/m2s = 1.45 gpm/ft2
2-4.3.1.1 The feed system should be designed to achieve the initial fill cycle at initial
pressure (typically 70 to 140 kPa [10 to 20 psig]) within the first 5 to 15 minutes to
ensure even sludge cake formation. Any imbalance in the sludge feed rate or cake
formation can result in a nonuniform cake of high resistance, cloth binding, or initial poor
filtration quality, and longer cycle times (EPA 1979). After this initial fill period and as the
2-28