Steam, Its Generation and UseBabcock & Wilcox Company
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Steam, Its Generation and Use
Babcock & Wilcox Company
Steam-boilers, Water-tube
For a stack lined with masonry--
diameter in inches = 4.92 (H. P.)^{2/5} (29)
In both of these formulae H. P. = the rated horse power of the boiler.
From this formula the curve, Fig. 33, has been calculated and from it
the stack diameter for any boiler horse power can be selected.
For stoker practice where a large stack serves a number of boilers, the
area is usually made about one-third more than the above rules call for,
which allows for leakage of air through the setting of any idle boilers,
irregularities in operating conditions, etc.
Stacks with diameters determined as above will give an available draft
which bears a constant ratio of the theoretical draft, and allowing for
the cooling of the gases in their passage upward through the stack, this
ratio is 8. Using this factor in formula (25), and transposing, the
height of the chimney becomes,
d^{1}
H = ----- (30)
.8 K
Where H = height of stack in feet above the level of the grates,
d^{1} = available draft required,
K = constant as in formula.
Losses in Flues--The loss of draft in straight flues due to friction and
inertia can be calculated approximately from formula (26), which was
given for loss in stacks. It is to be borne in mind that C in this
formula is the actual perimeter of the flue and is least, relative to
the cross sectional area, when the section is a circle, is greater for a
square section, and greatest for a rectangular section. The retarding
effect of a square flue is 12 per cent greater than that of a circular
flue of the same area and that of a rectangular with sides as 1 and 1½,
15 per cent greater. The greater resistance of the more or less uneven
brick or concrete flue is provided for in the value of the constants
given for formula (26). Both steel and brick flues should be short and
should have as near a circular or square cross section as possible.
Abrupt turns are to be avoided, but as long easy sweeps require valuable
space, it is often desirable to increase the height of the stack rather
than to take up added space in the boiler room. Short right-angle turns
reduce the draft by an amount which can be roughly approximated as equal
to 0.05 inch for each turn. The turns which the gases make in leaving
the damper box of a boiler, in entering a horizontal flue and in turning
up into a stack should always be considered. The cross sectional areas
of the passages leading from the boilers to the stack should be of ample
size to provide against undue frictional loss. It is poor economy to
restrict the size of the flue and thus make additional stack height
necessary to overcome the added friction. The general practice is to
make flue areas the same or slightly larger than that of the stack;
these should be, preferably, at least 20 per cent greater, and a safe
rule to follow in figuring flue areas is to allow 35 square feet per
1000 horse power. It is unnecessary to maintain the same size of flue
Public-domain text, read in full here on John Shaqi.
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