This section is from the book "Principles And Practice Of Plumbing", by John Joseph Cosgrove. Also available from Amazon: Principles and Practice of Plumbing.
The bacterial efficiency of gravity filters depends upon the use of coagulants. If clear water for industrial purposes is wanted, it may be had by filtering through sand without coagulant, but for domestic water supply, where bacterial purity is required, coagulants must be used. The tabulated report of chemical and bacterial tests of gravity water filters, at Lorain, Ohio, for week ending March 12, 1904 (see Table XL), will serve to show the efficiency of rapid sand filters.
The standard sizes, weights, capacities, etc., of the
Jewell Subsidence Gravity Filter can be found in Table XLI.
A plan of a filter house for a small city plant, showing the layout of filters, piping and apparatus, is illustrated in Fig. 112.
Pressure filters are enclosed in water-tight chambers, so that water can be driven through the filter bed by hydraulic pressure. A Jewell pressure filter of the settling basin type is shown in Fig. 113. This filter is constructed and operated similar to the Jewell gravity type, from which it differs only by being enclosed in a water-tight case. Pressure filters are not as efficient as gravity filters, but owing to the ease with which they can be attached to a water supply system they are extensively used for house filters. Usually pressure filters are connected to the service pipe in the cellar, and all water used in the building passes through them. When so installed they should be provided with a by-pass to permit unfiltered water being supplied to fixtures in the building in case the filter is cut out. The bacterial efficiency of pressure filters like that of gravity filters depends upon the use of coagulants. When water is to be used for manufacturing purposes, however, a clear filtrate can be obtained without coagulants. An automatic apparatus is used to feed coagulant to pressure filters. The standard sizes, capacities, weights and dimensions of Jewell pressure filters, with settling basins, can be found in Table XLII.

Fig. 113
Size | Connections, in Inches | Capacity | Area | Bed | Shipping Weights (Approximate) | Total Wgt. | |||||||
Diameter in Feet | Supply and Discharge Pipe | Washout Pipes | Minimum and Maximum, U. S. Gallons | Effective Filtering Surface, Sq. Feet | Filtering Material Cubic Feet | Machine Work Pounds | Tank Material Cypress or Cedar Cwt. | Filtering Material Tons | Filter in Operation Tons, about | ||||
Filter Bed Tank (Inside) | Main Tank (Outside) | Minute | Hour | Day 24 Hours | Settling Basin | ||||||||
6 | 7 | 3 | 6 | 47-94 | 2,800-5,600 | 62,500-125,000 | 1,500 | 28 | 118 | 1,000 | 50 | 5 | 15 |
8 | 9 1/4 | 4 | 6 | 82 164 | 5 000 10 000 | 120 000 240 000 | 2 600 | 50 | 200 | 1 800 | 70 | 9 | 28 |
10 | 11 1/2 | 4 | 8 | 180-260 | 7,800-15,600 | 185,000-370,000 | 4,000 | 78 | 312 | 2,500 | 105 | 14 | 45 |
12 | 13 1/2 | 5 | 8 | 188-376 | 11,300-22,600 | 250,000-500,000 | 5,750 | 118 | 452 | 3,750 | 125 | 20 | 70 |
14 | 15 1/2 | 6 | 8 | 255-510 | 15,300-30,600 | 865,000-730,000 | 8,000 | 153 | 612 | 5,000 | 145 | 27 | 100 |
17 | 18 2/3 | 6 | 8 | 376-752 | 22 600-45,200 | 500,000-1,000 000 | 11,500 | 226 | 904 | 9,500 | 180 | 40 | 145 |
21 | 22 3/4 | 8 | 2- 8 | 565-1,130 | 33,900-67,800 | 750,000-1,500,000 | 17,000 | 339 | 1,356 | 12,000 | 220 | 60 | 200 |
24 | 26 | 10 | 2-10 | 753-1,506 | 45,200-90,400 | 1,000,000-2,000,000 | 23,000 | 452 | 1,808 | 17,000 | 300 | 80 | 295 |
Standard height of filters, 14 feet. Depths of filter beds, 4 feet.
 
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