Excess air from any
source (except that which is provided through the combustion air intake for complete
combustion) needs to be eliminated to maximize efficiency. Just as excess combustion air reduces efficiency, air leaking in through
boiler cleanout and access doors reduces the flame/flue gas temperature and increases the
volume and velocity of flue gases required in order to be vented properly.
More importantly, before
a reliable tune up can be performed, these
sources of unnecessary air need to be eliminated, as combustion tests are
taken downstream from the burner. This air
leakage will effect the combustion test readings which are being used to determine proper
fuel and air adjustments.
For example, if the
burner combustion air intake is providing the proper amount of combustion air to produce
clean, efficient combustion, air being drawn in through access doors, cleanout ports,
etc., will increase O2 readings on the combustion analyzer and likely result in
readings that suggest the burner is operating with too much excess air. Attempts to fine tune the burner by
closing the combustion air intake damper or increasing fuel pressure will likely result in
starving the flame for air.
Check any access doors
for leakage with a smoke source to identify leakage. During service, replace any deteriorated gaskets and if necessary use high
temperature silicone chalk to insure an airtight seal.
One method to determine
the amount of unnecessary excess air from leakage in a boiler or forced air
unit is to take an overfire O2 reading and compare with the stack O2 reading. A higher stack O2 reading
indicates unwanted air leakage into the combustion chamber, flue passages or boiler
sections. These areas must be sealed to
attain accurate test results.
Miscellaneous Notes
A negative pressure
switch on sidewall vented or fan assist heating equipment, only proves a certain level of
negative pressure in the vent. It does not
necessarily prove flue gas flow. A
restriction of the combustion air supply will not necessarily cause the pressure switch to
lock out. Meanwhile, inadequate combustion
air may be responsible for CO production and possibly soot - both of which will increase
fuel consumption and safety concerns.
Newer systems use a
number of pressure switches to sense pressure drop across the heat exchanger to address
this issue.
While it is required to
size combustion air intakes in accordance with local codes, continuous readout combustion
test instruments can verify that the combustion air intakes are operating as designed. By simply opening a door or window to the outside
(of the boiler/furnace room) and noting changes in any of the readings, sufficient
combustion air intake can be verified.
By the same token,
observing combustion test readings while an exhaust system, air handler or clothes dryer,
for example, are operated may provide information regarding the need for additional air
intake to offset the indoor air removed by theses type systems.
Heat stress (thermal
shock) compounds the stress of the materials. Thermal
shock is one of the most common causes of boiler accidents.
As a rule of thumb,
return water should never be more than 60° cooler than supply
water. Generally, boiler manufacturers
recommend a 20° to 40° difference and that the
burner be run at low fire or cycled for a programmed period of time before the burner
brings the system to full operating capacity.
Keep this in mind when
combustion testing during periods of time when the boiler hasnt been running
regularly or during the summer when a chiller is in operation and there is any way for
chilled water to return to the boiler.
Finally, remember other
safety concerns identifiable during the course of your exposure to a particular
installation are critical as well. Domestic
hot water heating systems are a good example. Draft
and combustion tests will help verify safe and efficient combustion. However, measuring the temperature of the water
will determine the potential for scalding building occupants and is just as important.
Lowering tank
temperatures have direct influences on the amount of corrosion and scale produced as well. Every 20° increase in water
temperature doubles the corrosive effects of the water and increases lime scale deposits
by as much as four times. This simultaneously
reduces both operating efficiency and service life.