Steam:
Its Generation and Use
År: 1889
Forlag: Press of the "American Art Printer"
Sted: New York
Sider: 120
UDK: TB. Gl. 621.181 Bab
With Catalogue of the Manufacturers.of The Babcock & Wilcox Co.
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Many boilers show a high apparent evapora-
tion in consequence of furnishing “wet steam,”
while practically they are anything but economi-
cal. Parties have been known to claim an evap-
oration of 19 to 20 pounds per pound of coal,
where the highest practically possible is not over
13. Such boilers are dear at any price.
The cause of priming may be either impure
water, too much water, or improper proportions
in the boiler. When a boiler is found to form
wet steam with good water, carried at a proper
height, it is a proof of wrong design.
The amount of priming in different boilers
varies greatly, and as yet there is not sufficient
data to establish any definite ratio for boilers in
ordinary use. The experiments of M. Hirn, at
Mulhouse, showed an average of at least 5 per
cent. ; Zeuner sets it down as approximately
from 7% to 15 per cent.; the careful experiments
at the American Institute in 1871 show in cylin-
drical tubulars 7.9 per cent., and in the tests at
the Centennial Exposition one boiler showed as
high as 18.57 per cent, priming.
In sixteen different tests of the dryness of the
steam from Babcock & Wilcox boilers made by
twelve different engineers, the average moisture
in the steam was only 1.116 per cent. The high-
est was 4.16 per cent., which was less than the
same engineer with the same apparatus found in
large two-flue boilers, working very lightly.
SUPERHEATED STEAM.
Steam which has a higher temperature than
that normal to its pressure, is termed “super-
heated ” or “gaseous.” Dr. Seimens found that
when steam at 2120 was heated separate from
water it increased rapidly in volume up to 2300,
after which it expanded uniformly as a permanent
gas. If this superheating could be carried to such
an extent as to avoid the ‘ ‘ initial condensation
within the cylinder of an engine, there would be
a marked economy in its use, but this involves
so high a temperature as to burn the lubricating
material and destroy the engine in a short time.
Dixwell found superheating so as to maintain in
the cylinder a temperature of 400° with steam
at a pressure of 70 lbs., to be the limit of possible
lubrication. With a higher pressure that degree
of superheating would not afford sufficient
additional heat for the purpose. The present
tendency to high pressures seems, therefore, to
preclude the possibility of much gain through
superheating, because the temperatures are
already carried to very nearly the limit at which
lubrication can be maintained. For other pur-
poses the use of superheated steam adds little if
anything to the economy, while it greatly increases
the cost and the wear and tear. Where super-
heating is required it should always be done by a
separate apparatus, and pains must be taken to
separate the entrained water from the steam
before it enters the superheater. The use in any
steam boiler of superheating surface exposed to
the gases of combustion, is highly objectionable
and is of doubtful efficiency. Attempts to super-
heat steam by means of the waste gases, are
usually failures because in a well proportioned
boiler the low temperature of such gases necessi-
tates an unreasonably large surface to produce
the desired effect. Steam cannot be superheated
when it is in contact with water.
FEEDING BOILERS.
The relative value of injectors, direct-acting
steam pumps, and pumps driven from the engine,
is a question of importance to all steam users.
The following table has been calculated by D. S.
Jacobus, M. E., from data obtained by experi-
ment. It will be noticed that when feeding cold
water direct to boilers, the injector has a slight
economy, but when feeding through a heater a
pump is much the most economical.
Method of Supplying Feed Water
to Boiler.
Temperature of feed water as deliv-
ered to the pump or to the injector, b0°
Fah. Rate of evaporation of boiler, 10
pounds of water per pound of coal from
and at 212Q Fah.
Direct acting pump, feeding
water at 6o°, without a
heater.......................
Injector feeding water at 1500,
without a heater.............
Injector feeding through a
heater in which the water is
heated from 150 to 2000......
Direct acting pump feeding
water through a heater, in
which it is heated from 60
tO 200°......................
Geared pump, run from the
the engine, feeding water
through a heater, in which
it is heated from 60 to 200°..
Relative amount of coal required per unit of time, the amount for a direct acting pump, feed- ing water at 60°, without a heater, being taken as unity. Saving of fuel over the amount re- quired when the boiler is fed by a direct acting pump without heater
1.000 .0 \
•985 1.5 per ct.
•938 6.2 “
.879 12.1 “
.868 13.2
ECONOMY OF HIGH PRESSURE STEAM.
Higher steam pressure is the tendency ot the
times, and with good reason, for the higher the
pressure the greater the opportunity for economy
in generating power. The compound and triple
expansion engines of the present day, which have
reduced the cost of power some 40 per cent, over
the best performance of a few years ago, require
higher pressure than can with safety be carried
on shell boilers, but there is no difficulty in
carrying any desirable pressure on a sectional
water-tube boiler properly constructed. Babcock
& Wilcox boilers in special cases, carry as high
as 500 lbs. pressure in regular work.