Coordinated master Control in Thermal Power pLant
Short Description
for thermal power-plant familiarization...
Description
CMC (COORDINATED MASTER CONTROL) Atul Anand Soni
CMC ensure proper coordination between Auxiliaries, boiler and turbine to attain efcient and sae running o the plant. (1)CMC – coordinated mode ()!"#$%& ollow mode' !oiler ollow turbine ()urbine ollow mode' urbine ollow !oiler (critical *r. *r. Mode) M ode)
CMC coordinate sensiti+e turbine slow response boiler Auxiliaries. $imited with help o turbine control (%-C) and %. CMC
!oiler master on Auto urbine master on Auto /nit master ' &ecei+ing load demand
1)
CMC3
!asicall to control internal parameter4s o unit li2e (1) M *ressure, () $oad. Also to coordinate sensiti+e turbine and slow response o boiler auxiliaries, 5ood or networ2 and /nit stabilit. !oth !oiler and urbine control "6 Auto. )
!8M3
!oiler ollow turbine. urbine on $oad control' !oiler "6 Auto'control pressure with !$# as eed orward. M9 demands are met b urbine :rstl and lesser importance to unit stabilit. )
8M3
urbine ollow !oiler. !oiler Master on manual control. *ressure control. urbine maintains pressure b +aring MC; ,/nit load depends on
&/6!AC< M"0%. under runbac2 conditions the :ring or the boiler must be reduced to preset +alues, as close as possible to the tolerable limits. hereore the swings o :ring rate caused b the action o the *#0 controller must be a+oided. As conse=uence o this condition the sstem has to switched to pure eed orward to control where the :ring rate set point is directl proportional to load capabilit signal. o a+oid an mismatch between steam production o the boiler and the turbine load turbine has to be switched to initial pressure control. c ontrol.
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&/6!AC)
!"#$%& MA%&3 !asicall a pressure controller 8@8
*re. et point
BM 8%%0 8"&9A&0 #56A$ 56# "/*/ ' CMC !$# ' !.8.M *&0 ' .8.M 5% !B*A%0 ' &@!
Actual pressure
>D) 5 6 # 3 Control trac2ing generator or set point control module. 5enerates increase@decrease rate. arget to 56#3 CMC Ere=uenc
3
$oad dispatch center or unit' master
correctedF !8M
3
!oiler demand (!M "@*)
8M
3 Actual $oad.
&@!
3 /nit capabilit capabil it..
>G) /6# CA*A!#$#B3 Capabilit to produce M9 at that instant, 9.C signal depends on the number o auxiliaries in ser+ice and their contribution is expressed as M9 signal, which
>H) 85M"3 8ree 5o+erning mode o operation #ntro duce critical external parameter i.e. re=. o networ2 to our control sstem. o ensure stabilit o networ2 or grid it is necessar to ha+e re=uenc regulation in CMC@%-C. !ut re=uenc is networ2 parameter, which cannot be controlled b ew units in the networ2. otal disturbance in networ2 will be passed on to the units ha+ing regulation b the man units do not ha+e regulation. >I)Mode CMC CM C
Boiler A!$% controls A!
%$BFM
Throttle Pressure
CMC
Pressure
TFM
,# B)C'
MW & Pressure [Manual at '$B)] Produces steam as per unit capabilit-
Input
Feed Forward
Input To turbine control
MW
Pressure error
Steam Flow [BLI]
MW
Pressure error
MW error "#I $%P
MW error (Load controller actie! MW error (Load controller actie!
Throttle* pressure (Pressure controller actie!
Pressure error
PT+ Turbine load set point
Pressure error
Throttle* pressure (Pressure controller actie!
,#IT CapabilitSi.nal
BM B-passed
Pressure error
Turbine controls
To Boiler
Controls
!"#$%& 8"$$"9 M"0% 1. urbine on load control . !oiler master on Auto'controls throttle steam *ressure with steam Jow as eed orward. ;aring uel #@* (:ring rate) in the urnace. #n this mode boiler has to suppl the steam or whate+er load has been set rom urbine des2. #n this wa i the throttle steam reaches a limit (1> 2g below the set throttle steam *r.) Klimit *r. %ngagedL condition comes and load would be scari:ed to maintain@restore the throttle steam *r.
%$%C#"6 "8 !"#$%& 8"$$"9 M"0% ( !8M)
1. Pu Putt air air contr control ol on auto auto (at (at least least one FD fan) fan) 2. Put Put feeder feeders s sp speed eed cont contro roll on auto auto after after vary varying ing fuel fuel master(FM) output and making feeder speed controller error zero. . !ary "lr "lr. Master Master #$P #$P so t%at FM erro errorr &ecomes &ecomes zero zero.. '%en '%en put FM on auto. . Make Make t%rottle t%rottle pr. pr. et point point and and actual actual pr pr. Di*eren Di*erence ce zero. zero. +. Put "M on au auto. ,f unit in tur&ine follo- or coordinated mode c%ange over to &oiler follo- occurs under follo-ing condition / tur&ine goes to manual &ecause of any reason or operator action Pr 0M0 / Pr im 34M5
/&!#6% 8"$$"9 M"0%3 ' 1. !oile !oiler r manu manuall all cont control rolled led . urbine urbine master master "n Auto 'controls 'controls thrott throttle le steam *re. (9ith steam Jow as eed orward) b +aring load. #n .8.M *r. Controller comes into picture and the throttle team *re. ;aries the opening o MC; to maintain the set throttle steam *re.
/&!#6% 8"$$"9 M"0%
-
P
PR. R. SETPT.
+
B
PI
MW SET PT. FUEL FI RI NG DEVI CE
T
G N
+ PI
-
-
F
!"#$%& 8"$$"9 M"0%
P
+
-
PR. R.
B
PI D
PI
FUEL FI RI NG DEVI CE
T
G MW U
+ MW SET PT.
-
F F
%$%C#"6 "8 /&!#6% 8"$$"9 M"0% ( 8M)
1. "oil "oiler er maste asterr on on ma manua nual. 2. '%r '%rottl ottle e pres pressu surre devi deviat atio ion n zer zero. . 'ur&in r&ine e in auto uto. . Press. Press. 'ur&ine ur&ine 6o6o- pus% pus% &utton &utton along along -it% manual manual releas release e on 0M0 desk and tur&ine goes to initial pressure mode from M' mode &y itself. +. 7o- load load set set point point can &e c%an c%anged ged &y vary varyin ing g t%e t%e &oile &oilerr master manually.
" M ''
A section station and a setter or oxgen set point are pro+ided to achie+e the desired excess air. # +ariable " set point (*) is selected, set point is generated b a unction generator which is a unction o max ( air Jow * and total air Jow). #n other mode * is set rom /C!. " in Jue gas is compared with this * and error is ed to *# controller, output o which is limited between >.H and 1. o total air Jow.
Pressure Correction in CMC 8nder normal operating conditions including small load (pressure) variation &oiler and tur&ine are controlled independently as per set point from 97,. :ny un&alance in po-er generation and po-er consumption due to fre;uency variation in F9M# < t%rottle pressure may increase or decrease -%ic% may cause dangerous condition in t%e &oiler. ,f DP (et t%rottle pre./ :ctual t%rottle t%rottle pre.) pre.) variation goes &elo- set point ( / ve pressure deviation) < &oiler storage capacity is used. =o-ever< any large variation in t%rottle pressure s%all restrict t%e 'ur&ine output till t%e "oiler %as produced t%e additional output to matc% t%e increased demand. imilarly in case of >ve pressure deviation tur&ine output -ill increase. increase. MW
#$MW 2 K ! D" #$MW
# K
# K
2 K % D"
6ote3' '=?#''@ P?@8?@ (DP) correction starts at >$/ 1Ag and acts upto upto >$/ 2Ag. ,t -ill add or su&tract >$/ 1+ M5 to t%e 97, output< t%ere&y generating pressure corrected 97, output to @=0.(B unit +)
RE'ENC INLENCE ON CMC K F Min Unit Master
+
O/p + -
P
+ --
Max Min Min n M I N
.,
Fre&'enc% ( Pr. Connected GNI O/P to )*C
GNI Adder
Pre. Correction M A
+ +Adder
M
$e"a% Fre&'enc% connected GNI O/P
P
Th.Pre. Set.Pre
F/F !oi"er #aster PI+$
2 M
21 001
12 M
Air #aster #aster
F'e"
Fre&'enc% in="'ence M I N
5$C Unit Master
5OA$ UNIT
M A
+ + -
P
MA
T'r6ine "oad "i#iter CM C
UNIT Capa6i"it% M I N
TFM !FM
Tar3et o= 'nit
MA
MIN
UNIT "oad rate M I N
NIT COORDINATER *NI
4'n6ac7 "i#it
MIN M A
5IMITING !5OCK
Act'a" M !oi"er de#and
TS) 'pper #ar3in
+
TFM
P
+
M I N
TS) "o8er #ar3in
$ action
!FM
+ P
$e" a%
P
!5I
CMC
PU5; A -< PA FAN A PA FAN !
F9x:
!FM P4T$ M I N
Capa6i"it% + -
TFM
4'n6ac7 in action
Set.Pre Th.Pre
F/$
+
+
-
!oi"er #aster PI+$
"oad Air #aster #aster
F'e"
P4 9CMC set Pt to t'r6ine:
Max
5oad Setter
9
Min
Max / Min. 5i#iter
E+C TS) In="'ence
+
=:
+
+
5oad
5oad 4e=erence
+
+ + +
GNI 5oad
+
2$MW
+ $e"a%
+
Thrott"e Press're Set. +
-. 2+/ -. #2$ +/ ,-MW
!
!oi"er Master
%
Fre&
5oad 5i#iter
+
Act'a" Press're
M I N
Fre&'enc% In="'ence ON
Press're Correction
Fre&'enc% Un"oadin3 Characteristic
5oad contro""e r
TOTA5 COA5 F5O
21.3 1$.43 B TOTA5 OI5 F5O 22
0
M2 #
P2 2
"
! PT
22
A
A B
%
"
! %
.2
M G)N)4AT G) N)4AT)$ )$ 2 #
% P2
!/M O/P
AI4
C; Correction "oop #anip'"ates the coa" ="o8 #eas're#ent si3na" 6% increasin3 or decreasin3 it> to sho8 "ess coa" is 3oin3 8hen coa" &'a"it% is 6ad and #ore 8hen coa" is 3ood the e==ect is "i#ited to ?, to 22 o= act'a" coa" ="o8
% MIN
"
C; CO44)CT)$ COA5 F5O
EL MASTER
A
B
5
TOTA TOTA5 5 FU)5 FU)5 F5O F5O
!OI5) !OI5)4 4 $)MA $)MAN$ N$
Max
N2 N2
Max TOTA5 AI4 F5O *KBB,$
P2
P
PI
45
4S2@ OG)N MAST)4
Ui M21
?2
N2
Max TOTA5 AI4 F5O
+
AIR MASTER
DA
+
∑
+
N2
MIN AI4 F5O
DB
9α 2..:
12
AI4 F5O $)MAN$
Ua Ui
α
" Correction loop manipulates the total airJow measurement b increasing or decreasing " master to show less air@more air is Jowing. his inJuence is limited to > o the total air Jow E*resentlF
TOTALFUELFLOW
A/M
P AFL OW FROM MI LLS
BOI LER DEMAND
O2PROB OBE( L)
MAX
MAX
ANY6MI LLS
A B C J
SEC. AI R FLOW ( L)
D E
AW02
MW AI RFLOW SEC. AI R FLOW ( R) 80 %
Σ +
TOTALAI R
+ - -
P
AW0 2 FLUE GAS O2
PI RL OOO
MAN
Σ
O2 - O2PROBE( R)
RS04
A /M
P
O2
+ +
+
Σ/n
+ 20 %
( =0. 1)
=UiX∞ Ua
Σ PI
GAI N CHANGE
A#& 8$"9 C"6&"$ C-% ( %NC% A#&)
RL Y
-
+ +
- - + PI
PI RL YAc t
RL
OOO
Y
YAc t
Y
+
+ P
AW0 2
-
+ -
+ -
AW0 2
-
OOO
%$%C#"6 "8 CMC 1. Pu Putt air air cont contrrol on auto auto (at (at leas leastt one one FD FD fan) fan) 2. Put Put feeder feeders s sp speed eed cont contro roll on auto auto aft after er varyi varying ng fuel fuel master(FM) output and making feeder speed controller error zero. . !ary "lr. "lr. Master Master #$P so so t%at t%at FM error error &ecomes &ecomes zero. zero. '%en put FM on auto. . Make Make t%rottle t%rottle pr. pr. et point point and actual actual pr. pr. Di*eren Di*erence ce zero. zero. +. Put "M on auto. 3. ,ncre ,ncreas ase e $decre $decrease ase unit unit mast master er outpu outputt so t%at t%at it &ecom &ecomes es e;ual to actual load. (-ait unit load set value and load value matc%es as s%o-n in t%e 0M0 panel digital indicator). C. Form orm '9 '9 desk desk put tur&in tur&ine e contr control ol on auto. auto. . Press Press coor coordin dinate ated d pus% pus% &utton &utton alon along g -it% -it% manual manual rele release ase on 0M0 desk.
FEED RATE
C,23 "3#3)T$ "enerator UCB Set Point
Ma0 Mill PA Flow
/ Controller
1)+
*
C,23 "3#3)T$ "3#3)T$ S3TTI#"S U2 CA4$ *A$ S)T POINT FO4 PA F5O AS P)4 F))$ 4AT)
F33+ )T3 (T%1!
MILL P) FL$W S3TP$I#T (T%1!
4
54
6578
58
94
55
:4
;978
C,23 C,23 "3#3)T "3#3)T $ S3TT S3T T I#" 140
120 105
! 100 1 % T ( T # I $ 80 P T 3 S W $ L 60 F ) P L L I M 40
108
100 96.5 92.5
77 75 70
20
0 0
17.5
20
30
40
50
60
70
T+ANK O
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