Transactions of the American Society of Civil Engineers, vol. LXXII, June, 1911: Water Purification Plant, Washington, D. C. Results of Operation.American Society of Civil Engineers
Science
Transactions of the American Society of Civil Engineers, vol. LXXII, June, 1911: Water Purification Plant, Washington, D. C. Results of Operation.
American Society of Civil Engineers
Civil engineering -- Periodicals; Water treatment plants
Although this preliminary filter was operated at a high rate, its
efficiency was quite satisfactory. In fact, at times when the
applied water was comparatively good, very little work was left for
the slow sand filter. At times of high turbidity, however, some of
the exceedingly fine mud in the applied water passed through this
filter, as well as the slow sand filter connected with it, and it
proved to be absolutely impossible to produce a clear effluent at
all times with this combination.
Filter Plant No. 2 proved more economical and convenient in
operation, but somewhat less efficient than Filter Plant No. 1.
Neither filter could be depended on to give a clear effluent when
the applied water was turbid.
In the operation of Filter Plant No. 3, sulphate of alumina was used
when the applied water contained too much turbidity to be treated
satisfactorily by slow sand filters.
When the water was comparatively clear, either one of the three
systems, or slow sand filtration alone, was entirely satisfactory.
At times of high turbidity, however, Filter Plant No. 3 was the only
one which could be depended on to produce a clear effluent.
A fair comparison between the results of the three systems when
treating turbid water in January, 1908, is given in Table 16.
Table 16 shows very clearly that neither Filter Plant No. 1 nor No.
2 would prove at all satisfactory when treating turbid water, while
No. 3 could be depended on under all conditions. The results of
operation are shown in detail in Tables 17, 18, and 19. It will be
noticed in Table 17, that on March 10th, 1908, Filter Plant No. 1
was put out of service and a Puech system of preliminary filters was
substituted for it.
The Puech preliminary filters consisted of five units containing
gravel of varying sizes through which the water was filtered
successively before it was finally applied to the final slow sand
filter. A general idea of this system may be obtained by referring
to Figure 8.
~Table 16--Turbidity Results with Experimental Filters,
During Period of High Turbidity, January, 1908.~
Columns:
A - Effluent preliminary filter.
B - Effluent sand filter.
C - Effluent preliminary filter.
D - Effluent sand filter.
E - Effluent coagulant basin.
F - Effluent sand filter.
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