CHAPTER XII.

REMOVAL OF IRON FROM GROUND-WATERS.

The filtration of ground-waters is a comparatively recent development.

Ground-waters are filtered by their passage through soil generally

much more perfectly than it is possible to filter other waters, and

any further filtration of them is useless. Such waters, however,

occasionally contain iron in solution as ferrous carbonate.

Waters containing iron have been used as mineral waters for a very long

time. Such waters have an astringent taste, and have been esteemed

for some purposes. As ordinary water-supplies, however, they are

objectionable. The iron deposits in the pipes when the current is

slow, and is flushed out when it is rapid, and makes the water turbid

and disagreeable; and still worse, the iron often gets through the

pipe-system in solution, and deposits in the wash-tub, coloring the

linen a rusty brown and quite spoiling it.

An organism called crenothrix grows in pipes carrying waters containing

iron, and after a while this organism dies, and decomposes, and

gives rise to very disagreeable tastes and odors. It thus happens

that ground-waters containing iron are unsatisfactory as public

water-supplies, and are sources of serious complaint.

AMOUNT OF IRON REQUIRED TO RENDER WATER OBJECTIONABLE.

Three hundredths of a part in 100,000 of metallic iron very rarely

precipitate or cause any trouble. Five hundredths occasionally

precipitate, and this amount may be taken as about the allowable

limit of iron in a satisfactory water. One tenth of a part is quite

sure to precipitate and give rise to serious complaint. Two or three

tenths make the water entirely unsuitable for laundry purposes, and

are otherwise seriously objectionable, and will hardly be tolerated

by a community. Under some conditions ground-waters carry as much

as 1 part in 100,000 of iron, and such waters are hardly usable. In

iron-removal plants an effluent containing less than 0.05 is regarded

as satisfactory. One containing less than 0.02, as is the case with

many plants, is all that can be desired. The percentage of removal is

of no significance, but only the amount left in the effluent.

CAUSE OF IRON IN GROUND-WATERS.

Natural sands, gravels, and rocks almost always contain iron, often in

considerable amount. The iron is usually combined with oxygen as ferric

oxide, and in this condition it is insoluble in water. Water passing

through iron containing materials will not ordinarily take up iron.

When, however, the water contains a large amount of organic matter in

solution, this organic matter takes part of the oxygen away from the

iron, and reduces the ferric oxide to ferrous oxide. The ferrous oxide

combines with carbonic acid, always present under these conditions,

forming ferrous carbonate, which is soluble and which goes into

solution.

Surface-waters nearly always carry free oxygen, and when such waters

enter the ground they carry oxygen with them, and the organic matters

in the water use up the free oxygen before they commence to take oxygen

away from the iron of the ground. It is thus only in the presence of

organic matters, and in the absence of free oxygen, that the solution

of iron is possible. It sometimes happens that the organic matters

which reduce the iron are contained in the soil itself, in which

case iron may be taken up even by water originally very pure, as for

instance, by rain-water.

Generally speaking, iron is everywhere present in sufficient quantity

in the strata from which ground-waters are obtained, and wherever the

conditions of the organic matters and oxygen necessary for solution

occur, iron-containing waters are secured, and the iron is usually

present in the earth in such quantity that the water can dissolve as

much as it will take up for a long series of years, or for centuries,

without exhausting the supply. There is thus little prospect of

improvement of such waters from exhaustion of the supply of iron.

The circumstances which control the solution of iron are very

complicated and difficult to determine. Wells near a river, and drawing

their water largely from it by seepage, are apt to yield a water

containing iron sooner or later, especially where the river-water

carries a large amount of organic matter in solution. Waters drawn from

extensive gravel deposits, in which the water is renewed principally by

the rainfall upon the surface of the deposits themselves, often remain

entirely free from iron indefinitely. The rain-water is almost free

from organic matter, and the air is able to take care of decomposing

organic matters in the surface soil, and below this there are no

accumulations of organic matter sufficient to cause the solution of

iron. Under other conditions there are subterranean sources of organic

matter which result in the solution of iron under conditions which, on

the surface, appear most favorable for securing good water. Wells are

often used for many years without developing iron, when suddenly iron

will appear. This appearance of iron is often connected with increasing

consumption of water. In some cases it may result from drawing water

from areas not previously drawn upon.

When iron once makes its appearance in a water, it seldom disappears

completely afterward, although it often fluctuates widely at different

seasons of the year and under different conditions of pumping. In some

cases a decrease in the quantity of iron is noted after a number of

years, but in other cases this does not happen.

In a few cases manganese has been found in ground-waters. Manganese in

water behaves much like iron, but there are some points of difference,

so that the possibility of the presence of this substance should be

borne in mind.

Iron-containing waters are generally entirely free from oxygen, and

when first drawn from the ground they are bright and clear and do not

differ in appearance from other ground-waters. On exposure to the air

they quickly become turbid from the oxidation of the iron, and its

precipitation as ferric hydrate. At West Superior, Wisconsin, a water

was found containing both iron and dissolved oxygen. It was turbid

as pumped from the well. This condition of affairs seemed abnormal,

but was repeatedly checked, and the theory was advanced by Mr. R. S.

Weston, who made the observations, that it resulted from a mixture in

the wells of two entirely different waters, namely, a water resulting

from the rainfall on sand deposits back of the wells, containing

dissolved oxygen and no iron, and water from the lake which had seeped

through the sand, and which contained a considerable amount of iron

in solution but no dissolved oxygen. The wells thus drew water from

opposite directions, and the two waters were entirely different in

character, and the mixture thus had a composition which would not have

been possible in a water all of which came from a single source.

TREATMENT OF IRON-CONTAINING WATERS.

The removal of iron from ground-water is ordinarily a very simple

procedure. It is simply necessary to aerate the water, by which process

the ferrous carbonate is decomposed, and oxidized with the formation

of ferric hydrate, which forms a flocculent precipitate and is readily

removed by filtration. The aeration required varies in different cases.

The quantity of oxygen required to oxidize the iron is only a small

fraction of the amount which water will dissolve, and allowing water to

simply fall through the air for a few feet in fine streams will usually

supply several times as much oxygen as is necessary for this purpose.

Aerating devices of this kind have proved sufficient in a number of

cases, as at Far Rockaway, L. I., and at Red Bank, N. J. In some cases,

however, a further aeration is necessary, not for the purpose of

getting more oxygen into the water, but to get the excess of carbonic

acid out of it. Carbonic acid seems to retard in some way the oxidation

of the iron, and it is occasionally present in ground-waters in

considerable quantity, and quite seriously interferes with the process.

It can be removed sufficiently by aeration, but the necessary amount of

exposure to air is much greater than that required to simply introduce

oxygen.

Coke-towers have sometimes been used for this purpose. The towers are

filled with coarse coke and have open sides, and water is sprinkled

over the tops of them and allowed to drip through to the bottoms. In

general the simple exposure of water to the air for a sufficient length

of time, in any form of apparatus or simply in open channels, will

accomplish the desired results.

Mr. H. W. Clark[45] has called attention to the fact that in some cases

coke seems to have a direct chemical action upon the water which is

entirely independent of its aerating effect. In his experiments there

seemed to be some property in the coke which caused the iron to oxidize

and flocculate in many cases when it refused to do so with simple

aeration and filtration.

When the right conditions are reached the oxidation of the iron is

very rapid, and it separates out in flakes of such size that they can

be removed by filtration at almost any practicable rate. Mechanical

filters have been used for this purpose, with rates of filtration

of 100 million gallons per acre daily. In Germany, where plants for

the removal of iron are quite common, modified forms of sand filters

have usually been employed which have been operated at rates up to 25

million gallons per acre daily.

In experiments made by the Massachusetts State Board of Health rates

from 10 to 25 million gallons per acre daily have been employed.

The sand used for filtration may appropriately be somewhat coarser than

would be used for treating surface-waters, and the thickness of the

sand layer may be reduced. Owing to the higher

rates the underdrainage system must be more ample than is otherwise

necessary.

The rate of filtration employed is usually not a matter of vital

importance, but by selecting a rate that is not too high it is possible

to use a moderate loss of head. It is thus not necessary to clean the

filters too often, and the expenses of operation are not as high as

with an extreme rate. In some cases it is desired to accomplish other

results than the removal of iron by filtration, and this may lead to

the selection of a rate lower than would otherwise be used.

Under normal conditions of operation all of the iron separates on the

top of the sand. No appreciable amount of it penetrates the sand at

all. With open filters at Far Rockaway and at Red Bank there is an algæ

growth in the water upon the filters which, with the iron, forms a

mat upon the surface of the filter; and when the filter is put out of

service and allowed to partially dry, this mat can be rolled up like a

carpet and thrown off without removing any sand, and the filters have

been in use for several years without renewing any sand and without any

important decrease in the thickness of the sand layer.

Some waters contain iron in such a form that it cannot be successfully

removed in this manner. Thus at Reading, Mass., it was reported by

Dr. Thomas M. Drown that the iron was present in the form of ferrous

sulphate instead of ferrous carbonate, and that it was not capable of

being separated by simple aeration and filtration. A Warren mechanical

filter was installed, and the water is treated by aeration and with

the addition of lime and alum. The cost of the process is thereby much

increased, and the hardness of the water is increased threefold.

Several other cases have been reported where it was believed that

simple aeration and filtration were inadequate; but the advantages of

the simple procedure are so great as to make it worth a very careful

study to determine if more complete aeration, or the use of coke-towers

and perhaps slower filtration, would not serve in these cases without

resorting to the use of chemicals and their attendant disadvantages.

IRON-REMOVAL PLANTS IN OPERATION.

Iron-removal plants are now in use at Amsterdam and The Hague in

Holland, at Copenhagen in Denmark, at Kiel, Charlottenburg, Leipzig,

Halle, and many other places in Germany; at Reading, Mass.; Far

Rockaway, L. I.; Red Bank, Asbury Park, Atlantic Highlands, and

Keyport, N. J.

Among the earliest plants for the removal of iron were the filters

constructed at Amsterdam and The Hague in Holland. At Amsterdam the

water is derived from open canals in the dunes draining a large area.

The water has its origin in the rain-water falling upon the sand. The

sand is very fine and contains organic matter in sufficient amount

so that the ground-water is impregnated with iron. In flowing to a

central point in the open canals the water becomes aerated and the iron

oxidized. There are also algæ growths in the water which perhaps aid

the process. Sand filters of ordinary construction are used, and remove

both the iron and the algæ, and the rate of filtration is not higher

than is usually used in the treatment of river-waters, although it

could probably be largely increased without detriment to the supply.

The works at The Hague are very similar to those at Amsterdam, but

covered collectors are used to supplement the open canals. Both

of these plants were built before much was known about iron in

ground-waters and the means for its removal, but they have performed

their work with uniformly satisfactory results. In the more recent

German works various aerating devices are employed, and filters similar

in general construction to ordinary sand filters, but with larger

connections suited to very high rates of filtration, are employed.

The plant at Asbury Park was the first of importance constructed in

America. The water is raised from wells from 400 to 1100 feet deep

by compressed air by a Pohle lift. It is delivered into a square

masonry receiving-basin holding some hours’ supply. The aeration of

the water by this means is very complete. It is afterwards pumped

through Continental pressure filters direct into the service-pipes. The

reservoir for the aerated water was not a part of the original plant,

but was added afterwards to facilitate operation, and to give more

complete aeration before filtration.

At Far Rockaway, L. I., the water is lifted from wells by a Worthington

Pump, and is discharged over the bell of a vertical 16-inch pipe,

from which it falls through the air to the water in a receiving

chamber around it. The simple fall through the air aerates the water

sufficiently. From the receiving-chamber the water is taken to either

or both of two filters, each with an area of 20,000 square feet. These

filters are open, with brick walls and concrete bottoms, three feet

of sand and one foot of gravel, and the underdrains are of the usual

type. The water flows through regulator-chambers to a well 25 feet in

diameter and 12 feet deep, from which it is pumped to a stand-pipe in

the town. The plant was built to treat easily three million gallons

per day, and has occasionally treated a larger quantity. Either filter

yields the whole supply while the other is being cleaned. The rate of

filtration in this case was made lower than would have otherwise been

necessary, as there was an alternate supply, namely, the water from

two brooks, which could be used on occasions, and to purify which a

lower rate of filtration was regarded necessary, than would have been

required for the well-water. The removal of iron is complete.

[Illustration: FIG. 25.]

The plant of the Rumson Improvement Company at Red Bank, N. J., is

quite similar to that at Far Rockaway, but is much smaller. The outlet

is a 6-inch pipe perforated with 1/4-inch holes which throws the water

out in a pine-tree shape to the receiving-tank, thoroughly aerating

it. Each of the two filters has 770 square feet of area. The filtering

material is three feet of beach sand. From the regulator-chamber the

water flows to a circular well 18 feet in diameter, covered by a brick

dome and holding 17,000 gallons, from which it is pumped to the

stand-pipe. Either of the filters will treat ten thousand gallons of

water per hour, which is equal to the capacity of the pumps; and as

the consumption is considerably less than this figure, they are only

in use for a part of each day, the number of hours depending upon the

consumption. These filters are shown by the accompanying plan. The cost

of the work was as follows:

Filters and pure-water reservoir, with piping

and drains complete $3,799.47

New pump and connections 492.68

Engineering and superintendence 992.91

---------

Total cost of plant $5,285.06

The engineer who operates the pumps takes care of the filters, and no

additional labor has been required. The entire cost of operation is

thus represented by the additional coal required for the preliminary

lift from the wells to the filters. The effluent is always free from

iron.

The plant at Reading,[46] Mass., was installed by the Cumberland

Manufacturing Company, and combines aeration, treatment with lime and

sulphate of alumina and rapid filtration. The aeration is effected

by pumping air through the water, after the water has received the

lime. It afterwards receives sulphate of alumina and passes to a

settling-tank holding 40,000 gallons, in which the water remains for

about an hour. There are six filters of the Warren type, each with an

effective filtering area of 54 square feet.

The cost of coagulant is considerable. The chief disadvantage of the

process is that it hardens the water, which is naturally soft. From

the completion of the plant in July, 1896, to the end of the year the

hardness of the water was increased, according to analyses of the State

Board of Health, from 4.1 to 11.3 parts in 100,000, and for the year

1897 the increase was from 4.0 to 12.7. The iron, which is present in

the raw water to the extent of about 0.26 part in 100,000, is removed

sufficiently at all times.

Prior to the erection of this plant Mr. Desmond FitzGerald advised

aeration followed by sedimentation in two reservoirs holding half a

million gallons each, and by rapid filtration. Mr. Bancroft states that

in his opinion, if the reservoir recommended by Mr. FitzGerald had been

built, the filters could be run with very little or no coagulation, and

consequently without increase in hardness, which is the most obvious

disadvantage to the procedure. The nominal capacity of the plant is

one million gallons, and the average consumption about 200,000 gallons

daily.

The plant at Keyport, N. J., is similar, but smaller.

The filtration of public water-supplies Third edition, revised and enlarged. · 第 12 / 16 章