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Pressure Sand Filter |
PROCESS |
The filter is equipped with certain valves and devices which are incorporated in the outlet – pipe system. The purpose of these devices is to maintain a constant rate of filtration. An important component of the regulation system is the “ Venturi meter” which measures the bed resistance or “loss of head”. When the resistance builds up, the operator opens the regulating valve so as to maintain a steady rate of filtration. When the “ loss of head” exceeds 1.3 meter it is uneconomical to run the filter.
Normally the filter may run for weeks or even months without cleaning. When the bed resistance increases to such an extent that the regulating valve has to be kept fully open, it is time to clean the filter bed, since any further increase in resistance is bound to reduce the filtration rate. At this stage, the supernatant water is drained off, and the sand bed is cleaned by “ scraping” off the top portion of the sand layer to a depth of 1 or 2 cm. This operation may be carried out by unskilled laborers using hand tools or by mechanical equipment. After several years of operation, and say 20 or 30 scrapings, the thickness of the sand bed will have reduced to about 0.5 to 0.8 meter. Then the plant is closed down and a new bed is constructed. |
Pressure sand filters are made in two types. Vertical ad Horizontal. The principles of operation and method of working are similar and available in different size and capacities. SWT filters are very efficient to reduce the suspended solids. The different type of filtering media like Gravel, Silex, work as sand rest bed. In both filter water admitted at the top and passed away from the filter. The incoming water is directed on a baffle to prevent disturbance of the sand . |
Scope Of Supply |
Main Pressure Vessel of S.S. / M.S. / F.R.P. provided with stainer plates at top and bottom, & internally protected with plastic paint to prevent corrosion . Set of frontal piping & valves to control the Inlet,Outlet, Wash Out, Wash Out, Drain and Air supply for backard. One charge of filtering media/ Activated Carbon of required quality and sizes along with unit. The carbon filter will have steam-bath reactivation arrangement. |
Application |
- Rapid sand filter can deal with raw water directly. No preliminary storage is needed
- The filter beds occupy less space
- Filtration is rapid, 40-50 times that of a slow sand filter
- The washing of the filter is easy
- There is more flexibility in operation.
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Comparison Of Rapid And Slow Sand Filters |
Sr. No. |
Particulars |
Rapid sand
Mechanical filter |
Slow sand filter |
1 |
Space Occupies |
very little space |
large area |
2 |
Rate of filtration |
200 m.g.a.d. |
2-3 m.g.a.d. |
3 |
Effective size of sand |
0.4-0.7 mm |
0.2-0.3 mm |
4 |
Preliminary treatment |
Chemical coagulation and sedimentation |
Plain sedimentation |
5 |
Washing |
By back-washing |
By scraping the sand bed |
6 |
Operation |
Highly skilled |
Less skilled |
7 |
Loss of head allowed |
6-8 feet |
4 feet |
8 |
Removal of turbidity |
Good |
Good |
9 |
Removal of colour |
Good |
Fair |
10 |
Removal of bacteria |
98-99 per cent |
99.90 to 99.99 per cent |
Our Other Models
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Model No. |
Diameter of Unit in mm. |
Size of Piping in mm. |
Flow Rate M3/hr. |
Qty. of Activated Carbon |
PSF – 3 |
300 |
20 MM |
1.2 |
25 Kgs. |
PSF – 4 |
400 |
25 MM |
2.1 |
40 Kgs. |
PSF – 5 |
500 |
25 MM |
3.4 |
65 Kgs. |
PSF – 6 |
600 |
40 MM |
5.0 |
90 Kgs. |
PSF – 7 |
700 |
40 MM |
6.6 |
125 Kgs. |
PSF – 8 |
800 |
50 MM |
8.6 |
165 Kgs. |
PSF – 9 |
900 |
50 MM |
11.3 |
210 Kgs. |
PSF – 10 |
1000 |
50 MM |
13.5 |
260 Kgs. |
PSF – 11 |
1100 |
50 MM |
16.3 |
310 Kgs. |
PSF – 12 |
1200 |
60 MM |
20.0 |
375 Kgs. |
PSF – 13 |
1300 |
60 MM |
22.8 |
650 Kgs. |
PSF – 14 |
1400 |
80 MM |
26.5 |
500 Kgs. |
PSF – 15 |
1500 |
80 MM |
31.5 |
580 Kgs. |
PSF – 16 |
1600 |
100 MM |
34.5 |
650 Kgs. |
PSF – 17 |
1700 |
100 MM |
39.0 |
750 Kgs. |
PSF – 18 |
1800 |
100 MM |
45.0 |
840 Kgs. |
PSF – 19 |
1900 |
100 MM |
48.7 |
935 Kgs. |
PSF – 20 |
2000 |
100 MM |
54.0 |
1000 Kgs. |
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