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
~Table 15~--(_Continued._)
(_B_) ~Per Cubic Yard of Sand.~
=============+=======+=======+=======+=======+=======+=======+=========
Month. | Scrap-| Eject-| Wash- |Smooth-|Raking.| Re- | Total.
| ing. | ing. | ing. | ing. | |sanding.|
-------------+-------+-------+-------+-------+-------+--------+--------
1909.
-------------+-------+-------+-------+-------+-------+--------+--------
July | $0.08 | $0.15 | $0.03 | $0.01 | ... | $0.10 | $0.37
August | 0.07 | 0.15 | 0.03 | 0.01 | ... | 0.11 | 0.37
September | 0.07 | 0.17 | 0.03 | 0.01 | ... | 0.17 | 0.45
October | 0.06 | 0.15 | 0.03 | 0.01 | ... | 0.09 | 0.34
November | 0.10 | 0.23 | 0.02 | 0.02 | ... | ... | 0.37
December | 0.12 | 0.25 | 0.04 | 0.02 | ... | 0.08 | 0.51
-------------+-------+-------+-------+-------+-------+--------+--------
1910.
-------------+-------+-------+-------+-------+-------+--------+--------
January | 0.10 | 0.19 | ... | 0.02 | ... | ... | 0.31
February | 0.07 | 0.15 | ... | 0.01 | ... | 0.09 | 0.32
March | 0.06 | 0.11 | ... | 0.02 | ... | 0.08 | 0.27
April | 0.07 | 0.09 | 0.03 | 0.01 | ... | 0.05 | 0.25
May | 0.06 | 0.09 | 0.03 | 0.01 | ... | 0.06 | 0.25
June | 0.06 | 0.12 | ... | 0.01 | ... | 0.10 | 0.29
-------------+-------+-------+-------+-------+-------+--------+--------
Average | 0.07 | 0.14 | 0.02 | 0.01 | ... | 0.10 | 0.34
-------------+-------+-------+-------+-------+-------+--------+--------
Fiscal years:
-------------+-------+-------+-------+-------+-------+--------+--------
1905-06 | 0.07 | 0.35 | 0.04 | 0.07 | ... | 0.14 | 0.67
1906-07 | 0.06 | 0.19 | 0.03 | 0.02 | ... | 0.17 | 0.47
1907-08 | 0.09 | 0.15 | 0.03 | 0.01 | ... | 0.14 | 0.42
1908-09 | 0.06 | 0.14 | 0.03 | 0.01 | ... | 0.13 | 0.37
=============+=======+=======+=======+=======+=======+=======+=========
For convenience in referring to the different systems, the combined
rapid and slow sand filter will be designated as Filter Plant No. 1,
the combined Maignen scrubber and slow sand filter as Filter Plant
No. 2, and the combined coagulating basin and slow sand basin as
Filter Plant No. 3.
The length of run of Filter Plant No. 1 was relatively long at
first. The rapid rate of filtration, however, tended to carry the
clay, which was suspended in the applied water, to a considerable
depth in the filtering material, so that the runs gradually
decreased in length until they were reduced to about three days.
Unfortunately, it was necessary to use unfiltered water for washing,
which, together with the great penetration from the applied water,
finally made it necessary to remove all the filtering materials, and
wash them.
Public-domain text, read in full here on John Shaqi.
Reviews
Reviews
No reviews yet
Be the first to share your thoughts on this work.
Join the Discussion
Join the discussion
Sign in to leave a comment or review.
Sign InorCreate an account