The most effective is a coarse to fine pore size (the hydraulic radius of the stream line between particles). This allows for a more complete use of the bed area and reduced backwash frequency. Mixed media filter beds are the most common. An ideal mixed media bed may be composed of approximately 30-60 inches of granular media with the following makeup, from inlet to outlet:
12 - 18 inches of anthracite coal with a specific gravity of 1.5 and grain size of 0.7 - 2 mm.. The anthracite has a larger, more angular particle size to trap particulate matter before it gets to the sand layer and clogs it. Anthracite's lower specific gravity allows it to remain on top of the sand layer after backwashing. The anthracite layer also allows a lower backwash velocity to give the same bed expansion than if sand alone were used.
9 - 16 inches of sand - this can be composed of two types.
- Silica sand is used in the top 10 - 16 inches. Specific gravity is 2.5 and grain size ranges from 0.4 - 0.8 mm.
- Garnet sand may be used in the bottom 3 - 6 inches. Specific gravity is 4.2 and grain size ranges from 0.3 - 8 mm.
The higher specific gravity of garnet allows a finer pore size without the danger of mixing layers during backwashing. After the larger particles have been trapped by the anthracite, the sand media traps the remaining particulate matter by a combination of adhesion and straining.
16-24 inches of 3-6 carefully graded layers of successively coarser gravel. Preferred gravel size is 5 - 60 mm. The gravel maintains a consistent and diffused flow during filtration and prevents disruption of the sand layer during backwash.
Filter media selection (both size and type) may be the most important decision in a rapid sand filter design. Its selection is specific to each treatment plant and depends on the type of influent being filtered, media available and expected quality of effluent.
The inlet consists of a method of maintaining a set water level during filtration and removing waste during the backwash cycle.
Weirs are the most common method used to maintain the water level.
Wash trough photos courtesy of Dr. Daniel L. Gallagher
A series of wash troughs are used to collect and remove backwash water. Wash troughs are usually located 3.5 - 4 feet above the bed, 6 - 10 feet apart. Correct spacing and height of troughs ensures the dirty wash water is efficiently skimmed off, without washing out any of the filter media.
The outlet consists of a method to collect and remove filter water, distribute backwash water and control flow rate through the filter. Collection and distribution is accomplished with an under drain, commonly called a filter floor as it may also support the filter bed. There are three main designs commonly used:
- Perforated lateral
- Suspended nozzle
- Combination lateral and nozzle
The underdrain must be maintenance and corrosion free. Uniform collection and distribution is important to the integrity of the filter bed. Short circuiting or stagnation caused by the under drain can greatly reduce the effectiveness of the filter.
If the filter design is decreasing flow, then no flow control is used. As the filter bed fills with particulate matter the flow is reduced as more energy is expended in head losses. When head loss reaches a set maximum, cleaning by backwashing is required.
Steady flow type filters are the most common. In this design head losses, and consequently flow rate, are held constant. At the start of operation (clean filter) head losses are maintained at the designated level through external mechanical means. As the filter media fills with particulate matter, increasing the internal head loss, the external losses are reduced to maintain a constant. When external losses reach their minimum value, cleaning is required.
The main factors influencing the filtering and trapping processes are:
Different Types of Pressure Sand Filters
- Suspended particle size: Filtration efficiency improves with larger particulate size.
- Pore size: The space between the grains determines the size of particulate that can be trapped.
- Grain shape: Angular grains participate more in the mechanical straining process.
- Filtration velocity: Filtration efficiency decreases with increased velocity.
- Temperature of liquid: Increased water temperature, although it normally cannot be controlled, results in more efficient filtration.
- Chemical properties of the water and particle: A chemical filter aid may be added to promote adhesion.
In addition to the gravity fed, other versions are available:
- Deep coarse beds employ only a single media in 6 - 10 ft deep beds. These filters are best used on industrial wastewater with a known particulate matter.
- Upflow filters employ filtration from the bottom up, using coarse to fine filtration. Backwashing is accomplished in the same direction (upflow) but with a greater velocity.
- Biflow filters use a divided flow - upflow from the bottom and downflow from the top which permits filtration in opposite directions at the same time.
- Pressure filters are sand filters with the filter bed enclosed in a cylindrical steel or iron shell. The water is passed through at a pre-determined pressure. The filter can be connected directly to the water main and clean water delivered to the point of use with no additional pumping. It is most useful for smaller quantities of water.