Presented
to:
Instrument Society of America Power Symposium
Instrumentation in the Power Industry, Vol. 31
St. Petersburg, FL, May 23-25, 1988
The Evolution of Coordinated Control
H.C. Gery
Leeds & Northrup Company
North Wales, Pennsylvania
ORIGIN
The concept of coordinated control began in the late 1950's as a means
by which European designed once-through boilers could be adapted to American
operating practice. The concern was that the perceived limited storage
of once-through boilers could not respond to the rapid load swings needed
to meet the tight control of area regulation and close frequency regulation
that is the usual American operating practice. The concept of coordinated
control was to keep the turbine and boiler operations together by providing
them with a common demand signal. In this manner, the energy input to
the boiler would be matched to the energy demanded by the turbine. Thus
the expression "Direct Energy Balance." The initial designs
were provided on six once-through boilers of Combustion Engineering/Sulzer
Brothers design. The operation of these units was successful. In fact,
the last of the operating units has only recently been modernized after
over 25 years of service. Later, it was recognized that the Direct Energy
Balance concept was equally useful on drum-type boilers. This discussion
will cover the application of the Direct Energy Balance concept to drum-type
boilers and how it has evolved into the present configuration.
ORIGINAL CONCEPT-REQUIRED OUTPUT
The original concept is shown in Figure 1. The increase-decrease pulses
from the load dispatcher were integrated to produce a desired generation
value that was limited by operator adjusted Maximum Generation, Minimum
Generation, and Maximum Rate-Of-Change limits. The resultant value became
the demand for both generation and firing rate. This signal was called
Required Output. The Required Output signal was sent in equal measure,
to the demand signals for generation, fuel input, and air flow, thus assuring
that all three variables moved together. The direct, proportional action
of the Required Output Signal was modified by three corrections.
GENERATION CORRECTION
First, Required Output was compared to actual generation and the resulting
corrective action was added to the generation, fuel feed and air flow
demands. Any generation correction was sent in parallel to the boiler
inputs as well as the turbine valves.
THROTTLE PRESSURE CORRECT1ON
The second correction was from throttle pressure which was applied in
a positive direction to the fuel feed and air flow demands and in a negative
direction to the generation demand since the governor acts as a back pressure
regulator when controlling throttle pressure.
EXCESS AIR CORRECTION
The third correction was from the oxygen content of the flue gas which
was applied in a positive direction to the air flow demand and in a negative
direction to the fuel flow demand. The wisdom of the time was that variations
in excess air are more likely to be caused by changes in fuel heat-value.
So it seemed reasonable to correct the problem at its source. It should
be noted that the first paramagnetic oxygen analyzers were just being
introduced at this time so that automatic correction was, in itself, a
new control concept.
GENERATION CONTROL
Generation demand consisted of the summation of three values. The first
is the feedforward from Required Output. The second is the correction
for generation and the third is the negative correction from throttle
pressure. The summation of these three signals was compared to a signal
which we called turbine valve position, but in reality was the cam shaft
position of the mechanical governor. The generation controller pulsed
the turbine speed changer motor to change generation.
FUEL FEED CONTROL
Fuel Feed Demand was the summation of four signals, as follows: First,
Required Outputs as a positive feed-forward. Second, the positive correction
for generation. Third, the positive correction for throttle pressure.
And finally, a negative correction from excess air. This resultant value
was compared to metered fuel input using flow meters for oil and gas and
feeder speeds or other indices for pulverized coal. The fuel regulating
equipment was controlled from this action.
AIR FLOW CONTROL
Air flow demand was the summation of four signals as follows: First, Required
Output as a positive feed-forward. Second, the positive correction for
generation so that air flow kept in step with fuel feed. Third, the positive
correction for throttle pressure. And finally, a positive correction for
excess air. This resultant value was compared to actual air flow and the
air regulating equipment was adjusted. In the early 1960's air flow primary
elements were seldom provided and air flow was inferred by measuring the
pressure drop of the flue gas across the economizer. Air flow was often
regulated by the Induced Draft Fans and furnace pressure by the force
draft fans. This, of course, is in violation of current practice.
FREQUENCY BIAS
Theoretically, the system which has been described will cancel out any
governor frequency correction. A speed change will move actual generation
away from required output and the generation controller will seek to move
generation back, thus canceling the effect of the governor action. To
compensate for this effect, a speed correction which was called frequency
bias, was introduced. The intent was to adjust this correction to match
the droop characteristic inherent in the governor and therefore, bias
required output in an equal amount. In actual practice, with mechanical
governors, the governor seldom behaved in a uniform way and the frequency
bias setting seldom matched the actual governor action. In fact, sometimes
frequency bias would act and the governor would not.
ASSESSMENT OF THE FIRST GENERATION
The first applications of the Direct Energy Balance Concept proved that
better generation control could be realized if the boiler and turbine
were controlled by a common strategy. However, the initial operating experience
revealed a number of problems. First, governor cam shaft position was
not a reliable measurement of turbine valve positions, since it does not
recognize valve points, governor deadbands or hysteresis. Second, it was
found that the throttle pressure correction on the generation control
tended to override the generation correction since, on a load change,
they tended to work in opposite directions. This meant that generation
response would be sluggish. In actual practice, the throttle pressure
correction was set at minimum if not cut out entirely. Similarly, the
excess air correction on fuel, which seemed theoretically correct, was
found to introduce upsets in throttle pressure. As you might expect, it
was set to zero in the field. In addition, inferential measurements of
the fuel input by damper positions, feeder speeds etc. did not accurately
measure the strategy input to the boiler, either quantitatively or dynamically.
This required the throttle pressure controller and the excess air controller
to correct any mismatch through their integrating actions. Finally, the
use of a common demand for both turbine and boiler did not recognize that
the energy storage of the boiler would change whenever load was changed.
The integrating action of the throttle pressure had to supply all of this
correction.
EARLY IMPROVEMENTS
The first improvements to the Direct Energy Balance are shown on Figure
2. The non linearities of the governor valve system were overcome by replacing
cam shaft position with the pressure ratios signal. Pressure ratio is
the ratio of turbine first stage pressure to throttle pressure and is
an index of effective throttle valve position. The effect of pressure
ratios is to treat the turbine valve complex as if it were a single, linear
valve. Introduction of this measurement stabilized generation control
and significantly improved unit response. The interaction of the throttle
pressure on generation and the excess air correction on throttle pressure
were dealt with in a positive manner. They were simply removed. The problem
of variable heat value, mill lags and other non-linearities in the fuel
delivery system was overcome on drum-type boilers by the introduction
of the Heat Release Calculation. Heat Release infers the energy delivered
by combining the change in energy storage, as determined by the rate of
change of drum pressure, with the energy delivered to the turbine as determined
by the turbine first stage pressure. Properly calibrated, this measurement
is linear over the entire load range, recognizes changes in fuel heating
value and fuel delivery, and dynamically recognizes the lags that are
inherent in the operation of pulverizers. Finally the problems associated
with changes in energy storage were reduced by introducing the rate of
change of Required Output (ROR) into each of the demand signals. This
rate signal could be adjusted to provide the increment of overfiring that
is necessary to change the boiler storage when load is changed.- The results
of these improvements were: Pressure Ratio and Heat Release linearized
two critical measurements. This meant that the common loading signal could
be matched to calibrated process feedbacks. The result was more stable
operation, particularly during load changes. The introduction of Required
Output Rate (ROR) provided the increments of energy storage needed during
load changes, which in turn stabilized throttle pressure during and after
a load change.
INTELLIGENT GOVERNORS
One of the most significant improvements in power plant control was the
replacement of the mechanical governors with electronic and, later, digital
devices, that linearized the valve operations, provided protective limits
and overrides and in many cases, duplicated the generation control shown
on the left side of this drawing. Since the turbine was selected well
in advance of the boiler control system, it made little sense to duplicate
the generation control functions that were already included in the turbine
governor control.
THE THIRD GENERATION
As shown in Figure 3, we investigated the use of pressure ratio as a feed
forward signal to firing rate demand. We determined that the ratio of
turbine first stage pressure to throttle pressure accurately detected
any movement of the turbine valves for whatever reason. When pressure
ratio is multiplied by the throttle pressure set point, it becomes a linear
and stable index of turbine energy demand and is therefore a valid feedforward
signal for firing rate. This meant that full coordination of the turbine
and the boiler could be achieved without a complex interface and without
duplicating functions in both the turbine and boiler controls. The energy
demand signal is compatible with any form of turbine control, from the
most complex, to no control at all. The Required Output Rate signal was
replaced by an equivalent signal which we called dynamic compensation
which performed the same function in a simpler manner and the demands
for fuel feed and air flow were simplified. In addition to eliminating
the need for a complex turbine interface, this third generation control
greatly simplified the internal self-balancing circuits that are needed
when fuel feed and air flow were not in full automatic. One of the characteristics
of conventional boiler control systems is that they overshoot and cycle
on a sustained load change. This is because the throttle pressure controller
and the fuel feed controller, act in cascade control and any sustained
throttle pressure error causes the throttle pressure controller to wind-up.
When variable throttle pressure operation was introduced, the amount of
throttle pressure deviation, and therefore, the amount of wind-up became
even more severe.
PRESENT GENERATION
We discovered the best way to eliminate the throttle pressure wind-up
was to eliminate the throttle pressure controller. Figure 4 shows the
present DEB configuration. Generation control may or may not be present,
or it may be executed in the governor control. The fuel feed controller
compares the calculated turbine energy demand with calculated boiler heat
release. The operation of the fuel feed controller is shown on Figure
5. The heat release calculation, shown on the right, is balanced to the
energy demand signal, shown on the left. If throttle pressure is less
than its set point, the resultant ratio is a value greater than one. Since
first stage pressure occurs on both sides of the equation, the equation
can only be balanced by obtaining a positive rate of change of drum pressure.
In other words, it is necessary to overfire to restore throttle pressure.
Note that the controller can be balanced even if there is a throttle pressure
error, as long as the amount of overfiring balances the relationship.
As throttle pressure approaches its set point, the amount of overfiring
is reduced. The configuration is self-dampening. When throttle pressure
equals its set point, there is no overfiring and the boiler stabilizes
at desired value without any overshoot and without any cycling.
BENEFITS
This stability of throttle pressure reflects itself in improved stability
in generation. Which means that units with this configuration will more
closely match generation to their demand. The heat release calculation
is linear and reproducible over a 20:1 range. Many gas fired boilers operate
stably below 5 % load. Since the heat release calculation represents actual
energy input, the fuel/air ratio is more uniform, which, in turn, stabilizes
steam temperatures during load swings. This is of particular benefit on
coal fired boilers where pulverizer dynamics as well as uncertainties
in the fuel heat value make it difficult to measure heat input with conventional
means. Like Ulysses, we have been on an Odyssey of thirty years and hopefully
we have returned home somewhat wiser and better for the experience. However,
unlike Ulysses, we cannot afford to stay at home, for our world is a very
dynamic one. We have developed correct feedforward signals and accurate
feedback signals which have simplified, yet improved, boiler controls.
The next improvements should be in the area of adaptive tuning and in
more refined feedforward inputs.





© 1989, Leeds & Northrup
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