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Boiler
Suggested
Operating Guide
The
following is a suggested
operating guide for safe and
reliable operation of the unit.
Routine monitoring of the
controls and safety systems by
the operator is imperative.
Water
Levels
The
water level must be continually
checked whether the feedwater
system is operated automatically
or when an operator is in
attendance. Proper water level
in the steam drum must be
maintained at all times. High
water level can result in damage
to internal separation equipment
with a corresponding reduction
in separation efficiency. This
will result in water carryover
and mineral deposition inside
the downstream components. If
the water level reaches too low
a point, the unit is in danger
of overheating with possible
catastrophic damage. If the
level is automatically
controlled by the feedwater
regulator, it should be adjusted
per the manufacturer's
recommendations so that the
level remains stable near the
centerline of the gauge glass.
The
water column and water gauge
glass should be drained once at
the beginning of each shift.
This will insure that sludge or
sediment will not have a chance
to accumulate in the column or
gauge glass and can cause an
erroneous level indication. The
boiler attendant, by observing
drained liquid and return of
liquid to glass, will be assured
of proper actuation of one of
the most important safety
devices of the unit. Daily
testing of level alarms and low
water cutoff is also
recommended.
Boiler
Water Blowdown
Boiler
water blowdown is done to remove
some of the concentrated water
from the pressure vessel while
it is under pressure. The
removed water containing
suspended and dissolved solids
is replaced with relatively pure
feedwater even though this water
is treated prior to use through
external processes designed to
remove the unwanted substances
which contribute to scale and
deposit formations. Regardless
of their high efficiency, none
of these processes in themselves
are capable of removing all
substances and a small amount of
solids will be present in the
boiler water. The solids become
less soluble in the high
temperature of the boiler water
and as the water boils off as
relatively pure steam, the
remaining water becomes thicker
with either suspended or
dissolved solids.
Internal
chemical treatment, based on
water analysis, is used
primarily to precipitate many of
the solids and to maintain them
as "sludge" in a fluid
form. This sludge along with
suspended solids that may be
present must be removed by the
blowdown process. If the
concentration of solids is not
lowered through blowdown but
rather accumulates, foaming and
priming will occur along with
scale and other harmful
deposits.
The
scale forming as salts tend to
concentrate and crystallize on
the heating surfaces. Scale has
a low heat transfer value. It
acts as an insulation barrier
and retards the heat transfer.
This not only results in low
operating efficiency and
consequently higher fuel
consumption, but also presents
the possibility of overheating
the boiler metal. The result can
be tube failures or other
pressure vessel metal damage.
There
are two principal types of
blowdown, they are intermittent
and continuous. Intermittent is
done manually and is necessary
for the operation of the boiler
regardless of whether or not
continuous blowdown is employed.
Continuous blowdown is a
continuous and automatic removal
of concentrated boiler water.
Intermittent
Blowdown
The
manual blowdown valve and
discharge lines are located at
the bottom or low point of the
blower. This also provides a
means of draining the boiler
when it is not under pressure.
The intermittent blowdown should
be opened fully for a short
duration (approximately 10 to 20
seconds), at least once per
shift thus insuring proper
removal of accumulated solids
that have settled out in the mud
drum. In cases where the
feedwater is exceptionally pure,
blowdown may be employed less
frequently since less sludge
accumulates in the pressure
vessel.
Frequent
short blows are preferred to
infrequent length blows. This is
particularly true when the
suspended solids content of the
water is high. With the use of
frequent short blows, a more
uniform concentration of the
pressure vessel water is
maintained. Blowing down is most
effective at a time when the
generation of steam is at the
lowest rate since the feedwater
input then is also low,
providing a minimum dilution of
the boiler water with low
concentration feedwater.
It
is recommended that the blowdown
valve nearest the boiler be
opened first and closed last,
with blowing down being
accomplished by the valve
furthest from the boiler. The
sequence of operation once
established should insure that
the valve last opened should be
the first closed so that the
other valve is saved from
throttling service to insure a
tight closing. The downstream
valve should be cracked slightly
to allow the discharge line to
warm up, after which this valve
opened slowly. Quickly close the
downstream valve tightly, then
close the valve next to the
boiler. The frequency and amount
of each blow should be
determined by actual water
analysis.
The
water level should be observed
during periods of intermittent
blowdown. If the glass cannot be
viewed by the person operating
the valve, another operator
should watch the glass and
direct the valve operator. The
blow-off valves should never be
left open and the operator
should never leave until the
blowdown operation is completed
and the valves closed. Be sure
the valves are shut tight.
Repair any leaking valves as
soon as possible.
Continuous
Blowdown
The
boiler is equipped with an
internal continuous blowdown
pipe. The collector pipe is
located several inches below the
normal water level, at a point
where the most concentrated
water is found. A manual
controlled metering valve is
normally utilized to control the
flow of concentrated water.
Periodic adjustments are made to
the valve setting to increase or
decrease the amount of blowdown
and water testing. Proper
monitoring and maintenance of
appropriate water conditions in
the boiler are mandatory to
assure long term integrity of
the boiler.
The
amount of water lost through a
continuous surface blowdown is
usually considerably less than
the water lost through bottom
blow-off in order to remove a
given amount of suspended
solids. The amount of blowdown
depends upon the rate of
evaporation and the amount of
sludge forming material in the
feedwater.
Foaming
or priming may occur in the
steam drum and cause large
quantities of water to pass over
into the steam lines. It can be
detected by violent fluctuations
or sudden dropping of the water
level in the gauge glass. This
trouble may be caused by dirt or
oil in the boiler water, an
overdose of treatment chemicals,
carrying too high a water level
in the steam drum, or excessive
rates of change of evaporation.
In case of serious trouble,
decrease the load on the boiler,
then alternately blowdown and
feed fresh water several times.
If foaming does not stop, cool,
empty, and wash out the boiler
and refill with fresh, treated
water. Any problem in regard to
extreme foaming or priming,
scale in boiler, corrosion or
pitting, should be referred
immediately to a company
specializing in boiler water
chemistry consulting. Do not
experiment with
"home-made" treatment
chemicals.
Saturated
Steam Sampling
When
a new sample line is being put
into service, flow steam and
condensate thought it for 24
hours before the samples are
collected. Before the sampling
period, blow steam though the
sample line to remove any
material that may have been
deposited. Adjust the flow rate
to that desired during sampling
and flow the sample at this rate
for one hour or longer before
conductivity measurements are
recorded before a sample is
collected for other methods of
analysis.
When
samples of condensate are
collected for evaporative
analysis, the flasks or other
types of containers should be
meticulously cleaned prior to
use. Borosilicate glass is a
satisfactory material for such
containers but they should be
aged to by allowing them to
stand for several days full of
distilled water. This aging of
borosilicate glass may be
hastened by a preliminary
treatment with dilute caustic
soda (ten grams/liter).
Containers fabricated from
suitable metals or plastics may
also be used.
Samples
should be analyzed as soon as
possible after collection. After
use, the flasks should be rinsed
with hydrochloric acid. These
flasks should be reserved and
used for no other purpose than
steam samples. When the
condensed sample is to be
analyzed by the electrical
conductance method, cool it to
25°C. When dissolved gases are
to be determined, cool the
sample to 20°C or lower.
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