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1
AGC 2
1.0 Introduction
In the last set of notes, we developed a model of
the speed governing mechanism, which is given
below:
)ˆ
1ˆ(
1
ˆ 


R
P
sT
K
x C
G
G
E (1)
In these notes, we want to extend this model so
that it relates the actual mechanical power into
the machine (instead of ΔxE), so that we can
then examine the relation between the
mechanical power into the machine and
frequency deviation.
What lies between ΔxE, which represents the
steam valve, and ΔPM, which is the mechanical
power into the synchronous machine?
2.0 Extended model
Your text does not go into great detail in regards
to the turbine model but rather argues that it
responds much like the speed governing system,
which is a single time-constant system.
2
Being a single time-constant system implies that
there is only one pole (the characteristic
equation has only one root). Thinking in terms
of inverse LaPlace transforms, this means that
the response to a step change in valve opening
will be exponential (as opposed to oscillatory)..
We simply confirm here that this is the case.
Analytically, this means that the relation
between the change in valve opening ΔxE and
the change in mechanical power into the
generator ΔPM is given by:
E
T
T
M x
sT
K
P ˆ
1



(2)
Substituting (1) into (2) results in








 )ˆ
1ˆ(
11

R
P
sT
K
sT
K
P C
G
G
T
T
M
(3)
which is
   





 ˆ
1ˆ
11 R
P
sTsT
KK
P C
GT
GT
M
(4)
3
Let’s assume that KT is chosen so that KTKG=1,
then eq. (4) becomes:
   





 ˆ
1ˆ
11
1
R
P
sTsT
P C
GT
M (5)
A block diagram representing eq. (5) is given in
Fig. 1.
R
1
Σ
  sTsT GT  11
1
-
+
ΔPC
Δω
ΔPM
Fig. 1
3.0 Mechanical power and frequency
Let’s examine expand (5) so that
      RsTsTsTsT
P
P
GTGT
C
M
ˆ
11
1
11
ˆ
ˆ 





(6)
Consider a step-change in power of ΔPC and in
frequency of Δω, which in the LaPlace domain
is:
4
s



 ˆ (7a)
s
P
P C
C

 ˆ
(7b)
Substitution of (7a) and (7b) into (6) results in:
      RsTsTssTsTs
P
P
GTGT
C
M
1
1111
ˆ







(8)
One easy way to examine eq. (8) is to consider
ΔPM(t) for very large values of t, i.e., for the
steady-state.
To do this, consider that the variable ΔPM in eq.
(8) is a LaPlace variable. To consider the
corresponding time-domain variable under the
steady-state, we may employ the final value
theorem, which is:
)(ˆlim)(lim
0
sfstf
st 
 (9)
Applying eq. (9) to eq. (8), we get:
5
     
     
R
P
RsTsTsTsT
P
RsTsTs
s
sTsTs
Ps
PstPP
C
GTGT
C
s
GTGT
C
s
M
s
M
t
M

































1
1111
lim
1
1111
lim
ˆlim)(lim
0
0
0
(10)
Therefore,
R
PP CM

 (11)
This is eq. (11.6) in your text.
Make sure that you understand that in eq. (11),
ΔPM, ΔPC, and Δω in eq. (11) are
 Time-domain variables (not LaPlace variables)
 Steady-state values of the time-domain
variables (the values after you wait along time)
Because we developed eq. (11) assuming a step-
change in frequency, you might be mislead into
thinking that the frequency change is the
initiating change that causes the change in
mechanical power ΔPM.
6
However, recall Fig. 3 of AGC1 notes, repeated
below for convenience as Fig. 2 in these notes.
Fig. 2
The frequency change expressed by Δω in eq.
(11) is the frequency deviation at the end of the
simulation. The ΔPM in eq. (11), associated with
Fig. 2, is
 not the amount of generation that was outaged,
 but rather the amount of generation increased
at a certain generator in response to the
generation outage.
7
So ΔPM and Δω are the conditions that can be
observed at the end of a transient initiated by a
load-generation imbalance. They are not
conditions inherent to the synchronous
generator, but rather conditions that result from
the action of the primary governing control.
In other words, the primary governing control
will operate (in response to some frequency
deviation caused by a load-generation
imbalance) to change the generation level by
ΔPM and leave a steady-state frequency
deviation of Δω.
Although we have not developed relations for ω,
PM, and PC (but rather Δω, ΔPM, and ΔPC), lets
assume we have at our disposal a plot of PM vs.
ω for a certain setting of PC=PC1. Such a plot
appears in Fig. 3. (The text makes the following
assumption on pg 383 (I added italics): “The
local behavior (as characterized by eq. (13)) can
be extrapolated to a larger domain.”)
8
PM
ω
R
PM


Slope=-1/R
PC1
ω0
Δω
ΔPM
Fig. 3
An important assumption behind Fig. 3 is that
the adjustment to the generator set point,
designated by PC=PC1, is done by a control
system (as yet unstudied), the secondary or
supplementary control system, which results in
ω=ω0. The plot, therefore, provides an
indication of what happens to the mechanical
power PM, and the frequency ω, following a
disturbance from this pre-disturbance condition
for which PM=PC1 and ω= ω0.
It is clear from Fig. 3 that the “local” behavior is
characterized by R
PM

 .
9
If we were to change the generation set point to
PC=PC2, under the assumption that the secondary
control that actuates such a change maintains
ω0, then the entire characteristic moves to the
right, as shown in Fig. 4.
PM
ω
PC1
ω0
PC2
Fig. 4
We may invert Fig. 3, so that the power axis is
on the vertical and the frequency axis is on the
horizontal, as shown in Fig. 4.
10
PM
ω
MPR
Slope=-R
PC1
ω0
Δω
ΔPM
Fig. 5
Fig. 6 illustrates what happens when we change
the generation set point from PC=PC1 to PC=PC2,
PM
ω
PC1
ω0
PC2
Fig. 6
11
It is conventional to illustrate the relationship of
frequency ω and mechanical power PM as in
Figs. 5 and 6, rather than Figs. 3 and 4.
(Regardless, however, be careful not to fall into
the trap that it is showing PM as the “cause” and
ω as the “effect.” As repeated now in different
ways, they are both “effects” of the primary
control system response to a frequency
deviation caused by a load-generation
imbalance).
From such a picture as Figs. 5 and 6, we obtain
the terminology “droop,” in that the primary
control system acts in such a way so that the
resulting frequency “droops” with increasing
mechanical power.
The R constant, previously called the regulation
constant, is also referred to as the droop setting.
12
4.0 Units
Recall eq. (11), repeated here for convience.
R
PP CM

 (11)
With no change to the generation set point, i.e.,
ΔPC=0, then
R
PM

 (12)
where we see that
MP
R




(13)
We see then that the units of R must be
(rad/sec)/MW.
A more common way of specifying R is in per-
unit, where we per-unitize top and bottom of eq.
(13), so that:
Mpu
pu
rM
pu
PSP
R







/
/ 0
(14)
where ω0=377 and Sr is the three-phase MVA
rating of the machine. When specified this way,
R relates fractional changes in ω to fractional
changes in PM.
13
It is also useful to note that
pupu f
f
f
f
f







000 2
2




 (15)
Thus, we see that per-unit frequency is the same
independent of whether it is computed using
rad/sec or Hz, as long as the proper base is used.
Therefore, eq. (14) can be expressed as
Mpu
pu
Mpu
pu
pu
P
f
P
R







(16)
5.0 Example
Consider a 2-unit system, with data as follows:
Gen A: SRA=100 MVA, RpuA=0.05
Gen B: SRB=200 MVA, RpuB=0.05
The load increases, with appropriate primary
speed control (but no secondary control) so that
the steady-state frequency deviation is 0.01 Hz.
What are ΔPA and ΔPB?
14
Solution:
pufpu 000167.0
60
01.0



pu
R
f
P
puA
pu
puA 0033.0
05.0
)000167.0(





pu
R
f
P
puB
pu
puB 0033.0
05.0
)000167.0(





Note!!! Since RpuA=RpuB (and since the steady-
state frequency is the same everywhere in the
system), we get ΔPpuA=ΔPpuB, i.e., the
generators “pick up” the same amount of per-
unit power (given on their own base).
But let’s look at it in MW:
MWSPP RApuAA 33.0)100(0033.0 
MWSPP RBpuBB 66.0)200(0033.0 
Conclusion: When two generators have the
same per-unit droop, they “pick-up”
(compensate for load-gen imbalance) in
proportion to their MVA rating.
15
In North America, droop constants for most
units are set at about 0.05 (5%).
6.0 Multimachine case
Now let’s consider a general multimachine
system having K generators. From eq. (16), for
a load change of ΔP MW, the ith
generator will
respond according to:
60/
60/ f
R
S
P
SP
f
R
pui
Ri
Mi
RiMi
pui





(17)
The total change in generation will equal ΔP, so:
60
...
1
1 f
R
S
R
S
P
Kpu
RK
pu
R 









(18)
Solving for Δf results in












Kpu
RK
pu
R
R
S
R
S
Pf
...
60
1
1 (19)
Substitute eq. (19) back into eq. (17) to get:
16













Kpu
RK
pu
Rpui
Ri
pui
Ri
Mi
R
S
R
S
P
R
Sf
R
S
P
...
60
1
1 (20)
If all units have the same per-unit droop
constant, i.e., Rpui=R1pu=…=RKpu, then eq. (20)
becomes:
 RKR
Ri
pui
Ri
Mi
SS
PSf
R
S
P





...60 1
(21)
which generalizes our earlier conclusion for the
two-machine system that units “pick up” in
proportion to their MVA ratings. This
conclusion should drive the way an engineer
performs contingency analysis of generator
outages, i.e., one should redistribute the lost
generation to the remaining generators in
proportion to their MVA rating, as given by eq.
(21).

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Automatic Generation Control-2

  • 1. 1 AGC 2 1.0 Introduction In the last set of notes, we developed a model of the speed governing mechanism, which is given below: )ˆ 1ˆ( 1 ˆ    R P sT K x C G G E (1) In these notes, we want to extend this model so that it relates the actual mechanical power into the machine (instead of ΔxE), so that we can then examine the relation between the mechanical power into the machine and frequency deviation. What lies between ΔxE, which represents the steam valve, and ΔPM, which is the mechanical power into the synchronous machine? 2.0 Extended model Your text does not go into great detail in regards to the turbine model but rather argues that it responds much like the speed governing system, which is a single time-constant system.
  • 2. 2 Being a single time-constant system implies that there is only one pole (the characteristic equation has only one root). Thinking in terms of inverse LaPlace transforms, this means that the response to a step change in valve opening will be exponential (as opposed to oscillatory).. We simply confirm here that this is the case. Analytically, this means that the relation between the change in valve opening ΔxE and the change in mechanical power into the generator ΔPM is given by: E T T M x sT K P ˆ 1    (2) Substituting (1) into (2) results in          )ˆ 1ˆ( 11  R P sT K sT K P C G G T T M (3) which is           ˆ 1ˆ 11 R P sTsT KK P C GT GT M (4)
  • 3. 3 Let’s assume that KT is chosen so that KTKG=1, then eq. (4) becomes:           ˆ 1ˆ 11 1 R P sTsT P C GT M (5) A block diagram representing eq. (5) is given in Fig. 1. R 1 Σ   sTsT GT  11 1 - + ΔPC Δω ΔPM Fig. 1 3.0 Mechanical power and frequency Let’s examine expand (5) so that       RsTsTsTsT P P GTGT C M ˆ 11 1 11 ˆ ˆ       (6) Consider a step-change in power of ΔPC and in frequency of Δω, which in the LaPlace domain is:
  • 4. 4 s     ˆ (7a) s P P C C   ˆ (7b) Substitution of (7a) and (7b) into (6) results in:       RsTsTssTsTs P P GTGT C M 1 1111 ˆ        (8) One easy way to examine eq. (8) is to consider ΔPM(t) for very large values of t, i.e., for the steady-state. To do this, consider that the variable ΔPM in eq. (8) is a LaPlace variable. To consider the corresponding time-domain variable under the steady-state, we may employ the final value theorem, which is: )(ˆlim)(lim 0 sfstf st   (9) Applying eq. (9) to eq. (8), we get:
  • 5. 5             R P RsTsTsTsT P RsTsTs s sTsTs Ps PstPP C GTGT C s GTGT C s M s M t M                                  1 1111 lim 1 1111 lim ˆlim)(lim 0 0 0 (10) Therefore, R PP CM   (11) This is eq. (11.6) in your text. Make sure that you understand that in eq. (11), ΔPM, ΔPC, and Δω in eq. (11) are  Time-domain variables (not LaPlace variables)  Steady-state values of the time-domain variables (the values after you wait along time) Because we developed eq. (11) assuming a step- change in frequency, you might be mislead into thinking that the frequency change is the initiating change that causes the change in mechanical power ΔPM.
  • 6. 6 However, recall Fig. 3 of AGC1 notes, repeated below for convenience as Fig. 2 in these notes. Fig. 2 The frequency change expressed by Δω in eq. (11) is the frequency deviation at the end of the simulation. The ΔPM in eq. (11), associated with Fig. 2, is  not the amount of generation that was outaged,  but rather the amount of generation increased at a certain generator in response to the generation outage.
  • 7. 7 So ΔPM and Δω are the conditions that can be observed at the end of a transient initiated by a load-generation imbalance. They are not conditions inherent to the synchronous generator, but rather conditions that result from the action of the primary governing control. In other words, the primary governing control will operate (in response to some frequency deviation caused by a load-generation imbalance) to change the generation level by ΔPM and leave a steady-state frequency deviation of Δω. Although we have not developed relations for ω, PM, and PC (but rather Δω, ΔPM, and ΔPC), lets assume we have at our disposal a plot of PM vs. ω for a certain setting of PC=PC1. Such a plot appears in Fig. 3. (The text makes the following assumption on pg 383 (I added italics): “The local behavior (as characterized by eq. (13)) can be extrapolated to a larger domain.”)
  • 8. 8 PM ω R PM   Slope=-1/R PC1 ω0 Δω ΔPM Fig. 3 An important assumption behind Fig. 3 is that the adjustment to the generator set point, designated by PC=PC1, is done by a control system (as yet unstudied), the secondary or supplementary control system, which results in ω=ω0. The plot, therefore, provides an indication of what happens to the mechanical power PM, and the frequency ω, following a disturbance from this pre-disturbance condition for which PM=PC1 and ω= ω0. It is clear from Fig. 3 that the “local” behavior is characterized by R PM   .
  • 9. 9 If we were to change the generation set point to PC=PC2, under the assumption that the secondary control that actuates such a change maintains ω0, then the entire characteristic moves to the right, as shown in Fig. 4. PM ω PC1 ω0 PC2 Fig. 4 We may invert Fig. 3, so that the power axis is on the vertical and the frequency axis is on the horizontal, as shown in Fig. 4.
  • 10. 10 PM ω MPR Slope=-R PC1 ω0 Δω ΔPM Fig. 5 Fig. 6 illustrates what happens when we change the generation set point from PC=PC1 to PC=PC2, PM ω PC1 ω0 PC2 Fig. 6
  • 11. 11 It is conventional to illustrate the relationship of frequency ω and mechanical power PM as in Figs. 5 and 6, rather than Figs. 3 and 4. (Regardless, however, be careful not to fall into the trap that it is showing PM as the “cause” and ω as the “effect.” As repeated now in different ways, they are both “effects” of the primary control system response to a frequency deviation caused by a load-generation imbalance). From such a picture as Figs. 5 and 6, we obtain the terminology “droop,” in that the primary control system acts in such a way so that the resulting frequency “droops” with increasing mechanical power. The R constant, previously called the regulation constant, is also referred to as the droop setting.
  • 12. 12 4.0 Units Recall eq. (11), repeated here for convience. R PP CM   (11) With no change to the generation set point, i.e., ΔPC=0, then R PM   (12) where we see that MP R     (13) We see then that the units of R must be (rad/sec)/MW. A more common way of specifying R is in per- unit, where we per-unitize top and bottom of eq. (13), so that: Mpu pu rM pu PSP R        / / 0 (14) where ω0=377 and Sr is the three-phase MVA rating of the machine. When specified this way, R relates fractional changes in ω to fractional changes in PM.
  • 13. 13 It is also useful to note that pupu f f f f f        000 2 2      (15) Thus, we see that per-unit frequency is the same independent of whether it is computed using rad/sec or Hz, as long as the proper base is used. Therefore, eq. (14) can be expressed as Mpu pu Mpu pu pu P f P R        (16) 5.0 Example Consider a 2-unit system, with data as follows: Gen A: SRA=100 MVA, RpuA=0.05 Gen B: SRB=200 MVA, RpuB=0.05 The load increases, with appropriate primary speed control (but no secondary control) so that the steady-state frequency deviation is 0.01 Hz. What are ΔPA and ΔPB?
  • 14. 14 Solution: pufpu 000167.0 60 01.0    pu R f P puA pu puA 0033.0 05.0 )000167.0(      pu R f P puB pu puB 0033.0 05.0 )000167.0(      Note!!! Since RpuA=RpuB (and since the steady- state frequency is the same everywhere in the system), we get ΔPpuA=ΔPpuB, i.e., the generators “pick up” the same amount of per- unit power (given on their own base). But let’s look at it in MW: MWSPP RApuAA 33.0)100(0033.0  MWSPP RBpuBB 66.0)200(0033.0  Conclusion: When two generators have the same per-unit droop, they “pick-up” (compensate for load-gen imbalance) in proportion to their MVA rating.
  • 15. 15 In North America, droop constants for most units are set at about 0.05 (5%). 6.0 Multimachine case Now let’s consider a general multimachine system having K generators. From eq. (16), for a load change of ΔP MW, the ith generator will respond according to: 60/ 60/ f R S P SP f R pui Ri Mi RiMi pui      (17) The total change in generation will equal ΔP, so: 60 ... 1 1 f R S R S P Kpu RK pu R           (18) Solving for Δf results in             Kpu RK pu R R S R S Pf ... 60 1 1 (19) Substitute eq. (19) back into eq. (17) to get:
  • 16. 16              Kpu RK pu Rpui Ri pui Ri Mi R S R S P R Sf R S P ... 60 1 1 (20) If all units have the same per-unit droop constant, i.e., Rpui=R1pu=…=RKpu, then eq. (20) becomes:  RKR Ri pui Ri Mi SS PSf R S P      ...60 1 (21) which generalizes our earlier conclusion for the two-machine system that units “pick up” in proportion to their MVA ratings. This conclusion should drive the way an engineer performs contingency analysis of generator outages, i.e., one should redistribute the lost generation to the remaining generators in proportion to their MVA rating, as given by eq. (21).