New York Continental Jewell Filtration Co. v. City of Harrisburg

208 F. 10, 1913 U.S. Dist. LEXIS 1185
CourtDistrict Court, M.D. Pennsylvania
DecidedAugust 25, 1913
DocketNo. 43
StatusPublished
Cited by1 cases

This text of 208 F. 10 (New York Continental Jewell Filtration Co. v. City of Harrisburg) is published on Counsel Stack Legal Research, covering District Court, M.D. Pennsylvania primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
New York Continental Jewell Filtration Co. v. City of Harrisburg, 208 F. 10, 1913 U.S. Dist. LEXIS 1185 (M.D. Pa. 1913).

Opinion

BUFFINGTON, Circuit Judge.

In this case the New York Continental Jewell Filtration Company charges the city of Harrisburg with infringing two of its patents in the operation of that city’s municipal water filtration plant. As the patents concern such public uses, the case is one of widespread municipal importance. The large sand bed through which the confined water seeps or percolates gives to such plants the name of “sand-filtration.” At the base of such bed the purified water passes' into draining channels, and is carried to the filter [11]*11outlet. Over these channels are graded layers, beginning with those of large stone and followed by those of gravel or coarse sand. On top of these lies the fine sand bed which gives the plant its name. The usual practice is to run the raw or unfiltered water into a sediment basin, where the coarser suspended matter settles. The partially clarified water then goes to a filter basin and lies, to the depth of several feet, on the sand bed. The constant head of water, weighing as it does many tons to the acre area, which is the usual- size of the basins, exerts a forcing, percolating pressure, and gives to such filters the name of “positive head” or “gravity” filters. In them the effective filtering or purifying agent is a sediment layer or mud crust, which gradually gathers on top of the sand and forms a complete and unbroken scum or cover. This layer, well recognized everywhere as the vital factor in filtration, is usually known as tile “Schmutz-Decke,” German words, meaning, literally, “the dirty covering.” The formation thereof and the general operation of filtering are thus described in the respective briefs. That of the plaintiff says:

“When a slow-sand filter is first started, the outlet valves are so set as to allow the water to percolate slowly through the bed, say at about one-tenth the normal rate of filtration, and each day thereafter the rate is progressively increased so that at the end of a few days it is miming at the normal rate of speed, and so maintained, this being necessary 1o insure proper building up of the sediment layer or Schmutz-Decke. In a month or so this sediment layer accumulates on the surface of the filter, and becomes so thick as to practically prevent the passage of water through it, and then the filter has to he shut down and drained; and itJs cleaned by manually scraping off, with shovels, from half an inch to an inch or more of the surface material. The filter is then again filled >vitli filtered water, applied from below the bed, the raw water turned on, and filtration resumed, at slow rate at first and gradually increasing this rate as before.”

From these workings it will be seen the process requires the maintenance of a deep head; it involves the gradual building up of the surface layer; it necessitates frequent stoppages of filtration, washing, and subsequent upbuilding of the layer; such washings require the use of filtered water. The account in defendant’s brief reads:

"In slow-sand filters, hfter they have been in operation a little time, there is ail accumulation upon the surface, including certain helpful bacteria, the growth of which form gelatinous sticky coatings on the sand grains and tend to reduce Hie pore spaces between the grains and thus intercept the impurities suspended in the water, and further bring about the oxidation and nitrification of the organic matter dissolved in the water, to a large extent, and thus purify the water to a high degree without the addition of chemicals.
••In the operation of mechanical filters the water is passed through the filter bed so rapidly that there is not sufficient time for the bacterial growths to develop in the top layers of the sand, as above described for slow-sand filters, and it is necessary to produce an artificial gelatinous clogging of the top of the filter to take the place of the bacterial jelly formed in slow filters. This is done by adding to the water certain chemicals, like sulphate of alumina or sulphate of iron, which hare the property of becoming insoluble in the presence of alkaline constituents like the carbonates of lime and magnesia, which are found in most natural waters, or can be cheaply added if the water be naturally deficient thereof. When solutions of iron or aluminum sulphate are added to waters having an alkaline reaction, therefore, the soluble sulphates of iron or alumina are chemically changed' into the insoluble hydrate, or hydrated oxide, which gradually appears in the water in the form of a floccu-[12]*12lence, scattered throughout the entire mass to which the chemicals may have been added, and catches in its flakes many of the particles of impurities suspended in the water. When .water which has been treated, in this way is passed upon filters, and goes down through the sand bed, the fiocculent particles produced by the chemical reactions are caught in the filter bed and retained there, the clarified water passing on down through the bed and issuing througn the outlet pipe and controller. The floce'ulent matter, or coagulum, which has been retained in the filter bed is like the bacterial jelly in the slow filters, gelatinous and sticky in its nature, and serves to reduce the pore-space between the sand and thus intercept and hold back the suspended matters in the water being filtered. After about 12 to 20 hours (on the average) of operation, rapid filters generally become clogged so that they will not yield their rated quota of water, and then it becomes necessary to clean them.”

It would thus seem that in slow-filtration plants, the efficient agent of filtration is the surface sediment layer. Where more rapid or mechanical filtration was necessary, coagulants were used, and what corresponded to the Schmutz-Decke was by them formed in a few minutes, the coagulants forcing the impurities together like curd in milk. The proofs, as will be seen in extracts quoted below, show that this surface sediment layer usually is found in a stratified zone, distinct from the sand bed beneath, and that there is little, if any, penetration of the gelatinous sediment matter into the latter. It also appears from such proofs that as the surface sediment layer.thickened, it was so compacted by the water head pressing on it that little water passed through it. But not only did such surface layer tend to‘ eventually prevent percolation, but its compact shell tended to create a vacuum beneath, which latter, by liberating the air in the passing water, still further impeded percolation. This arose from the fact that water, under high pressure, retains very considerable air, which, as a vacuum is formed and the water is subjected to less pressure, is released. But this released air tends to fill and clog the interstices between the sand grains and thereby clogs the water flow. In that regard, the Fuller report, made prior to this suit, in the Cincinnati filtration tests, is illuminative. There Mr. Fuller, who was subsequently accredited by the defendant in making him its witness, in speaking of slow-sand, or English, filters, then said:

“In English filters the section of maximum frictional resistance is always at and just below the surface of the sand layer. Accordingly, when the active head exceeds the depth of the water above the sand, there is a united clogging action at this portion of the filter, due both to suspended matter removed from the water and the air evolved from it. As a result of this confined action, the yield of water after this time is very small.”

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208 F. 10, 1913 U.S. Dist. LEXIS 1185, Counsel Stack Legal Research, https://law.counselstack.com/opinion/new-york-continental-jewell-filtration-co-v-city-of-harrisburg-pamd-1913.