- Open Access
- Total Downloads : 263
- Authors : Mr. Sunil Kumar, Dr. Jaydeep Chakravorty, Mr. Abhishek Bhardwaj
- Paper ID : IJERTV3IS030254
- Volume & Issue : Volume 03, Issue 03 (March 2014)
- Published (First Online): 19-03-2014
- ISSN (Online) : 2278-0181
- Publisher Name : IJERT
- License: This work is licensed under a Creative Commons Attribution 4.0 International License
Four-Area in AGC Interconnected System under the Deregulated Environment using BF Controller
Sunil Kumar Birthlia Assistant professor ,EE Dept. |
Dr. Jaydeep Chakravort y Associate Professor, EE Dept. |
Abhishek Bhardwaj Assistant Professor, EE Dept |
IITM, MURTHAL |
BUEST, Baddi |
BUEST, Baddi |
Abstract In this paper the bacterial foraging(BF) optimization control technique is developed for the design of integral controller gain, which is applied to AGC in interconnected four area system with GRC based controller under the deregulated environment to control the tie line power and frequency of the interconnected system. All four areas have different number of GENCOS, DISCOS and TRANSCOS. A DISCO can individually and multilaterally contracts with a GENCO for power requirements and these transactions are done under the ISO supervision. After deregulation, the bilateral contract on the dynamics of automatic generation control (AGC), DPM has been used. The performance of system is obtained by MATLAB- SIMULINK.
Index TermsGENCO, DISCO, TRANSCO, DPM, CPF ,AGC
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INTRODUCTION
Automatic Generation Control plays a very important role in an interconnected power system operation and control. It improves the reliability of system and makes the system more adequate. AGC also maintains the system frequency constant and makes the system more stable. As the load demand increases or decreases, the speed of generator prime mover set also changes which cause deviation in frequency of the system and hence affect the steady state stability of the system. Automatic generation control regulates the power output of generator in accordance with the change in system frequency, tie line power, so as to maintain the system frequency with in the permissible limit (constant). To attain zero steady state error and to maintain the system frequency constant, a control scheme is needed. Here study of the four area restructured power system is done in which each area has its own automatic generation controller (AGC) which maintains the tie line power and system frequency constant [11]-[13] by varying the generation according to the area control error (ACE). AGC varies the set position of generators of that area, which minimize the average time of ACE. In a deregulated system DISCOs buy power from GENCOs at competitive price. Hence, DISCOs have various options for the transaction of power from any of the GENCOs of its own area or different area.
In each area, an automatic generation controller (AGC) Supervises the tie line power and system frequency, also computes the net change in the generation required which is related to the area control error-ACE and change the set position of the generators with in that area due to which net average time of ACE is at minimum. Optimization of auxiliary
controller gains has been the main area of attraction. In this paper the gain of proportional controller is controlled by the use of Bacterial Foraging Technique. The frequency and tie line power is compared for the LFC in deregulated environment by the use of this technique [8]. The most frequently used controller in LFC is Proportional Integral Controller (PI). It is simple and has better dynamic response in comparison to other controller but it fails to operate when the complexity of system increases because of the sudden load change occurs or dynamics of boiler changes. Bacterial Foraging Technique improves [10] the performance of PI Controller by varying its gain as per the requirement of load. The main contribution of this paper is comparison of frequency and tie line power for the LFC in deregulated environment. Bacterial Foraging (BF) technique is used to control the gain of proportional controller.
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RESTRUCTURED POWER SYSTEM Power system is restructured to improve the system
reliability and to maintain a proper balance in between the demand and supply. Restructured power system is basically divided into three parts GENCOs (generating companies), TRANSCOs (transmission companies), and DISCOs (distribution companies). The GENCOs generates power and DISCOs have freedom to have contract with any GENCO for the sake of power trading [2]-[3]-[11]-[13]. To visualize the contracts between GENCOs and TRANSCOs, the concept of DISCO participation matrix (DPM) is used. DISCO participation matrix is in the form of rows and columns where row represents number of GENCOs and columns represents number of DISCOs. Some of the areas may have the un- contracted loads which cause sudden load change in the system and hence the frequency of the system deteriorate. The total load on the GENCOs of an area is the sum of cpf s (elements of DPM) and the pu MW load of all the DISCOs of that area. Entry in DPM is a fraction of total load power contracted by bilateral contract. Due to this, DPM column entries belong to that disco is unity. Load frequency control is provided by the ISO which is an ancillary service in the deregulated power system that are required to maintain the real time balance between generation and load demand for minimizing frequency deflections and governing tie-line, allow enough Security level for predicted energy transactions and network configuration. The research work in deregulated AGC is contained in [2],[4],[5],[11].The load demand is fluctuating time to time thats why introducing new potential generating
plants such as gas fired, diesel etc are connected to the system to avoid the disturbance in the system.
.
Fig-1 Configuration of power system under deregulated environment The DMP will be:-
The steady system consists of four-area. Area-1 consists of three GENCOs and two DISCOs. Their contracts at some instant of time is taken as per DPM matrix shown above.
The actual and scheduled steady state power flows on the given tie line is:-
Ptiei-j, schedule = [ Demand from genco of area i by disco of area j Demand from genco of area j by disco of area i ]
The tie line error is given by:-
Ptiei-j, error = Ptiei-j, actual – Ptiei-j, schedule.
The tie line error disappear the steady state error. The ACE signal given to the ISO is:-
ACEi = Bi fi + Ptiei-j, error
fi is change of frequency of area i and Bi is frequency Biase factor of area i
Genco1(scheduled) = (0.2+0.1)*0.01 = 0.03 pu Genco2(scheduled) = (0.2+0.4)*0.01 = 0.06 pu Genco3(scheduled) = 0 pu
Genco4(scheduled) = (0.1+0.2)*0.01 = 0.03 pu
Genco5(scheduled) = (0.1+ 0.2 + 0.3)*0.01 = 0.06 pu
1,1 1,2 1,3
2,1 2,2 2,3
3,1 3,2 3,3
4,1 4,2 4,3
1,8
2,8
3,8
4,8
Genco6(scheduled) = ( 0.2 + 0.4 + 0.3)*0.01 = 0.09 pu Genco7(scheduled) = 0 pu
Genco8(scheduled) = 0 pu
Genco9(scheduled) = ( 0.1 + 0.3 + 0.4)*0.01 = 0.08 pu
= :
:
:
:
: : :
: : :
: : :
: : :
Genco10(scheduled)=(0.2)*0.01=0.02pu
Genco11(scheduled) = ( 0.2 + 0.3 + 0.2+0.5+0.5)*0.01 = 0.17 pu Genco12(scheduled) = ( 0.2 + 0.1 + 0.2+0.2+0.5)*0.01 = 0.12 pu Genco13(scheduled)=(0.2+0.3+0.2+0.2+0.2+0.2+0.1)*0.01=
0.14pu
15,115,215,3
15,8
Genco14(scheduled) = 0 pu Genco15(scheduled) = 0 pu
0.2
0
0 0
0.2 0
0.1 0
0 0
0 0 0
0 0 0.4
The schedule tie line powers are:-
0 0
0 0
0 0.1
0
0.1
0
0 0
0 0
0.2 0/p>
0
0.2
0
0 0
0 0
0.3 0
Ptie1-2, schedule = (0.2 + 0.1)*0.1 (0.1×0.1) = 0.02pu
Ptie1-3, schedule = (0.1×0.1) = 0.01pu
Ptie1-4, schedule = [(0.2 + 0.2 + 0.2)*0.1 + (0.3 + 0.3)*0.1]
0.2 0
0.4
0.3 0
0 0 0
(0.4×0.1) = 0.08pu
0
= 0
0
0
0.2
0.2
0.2
0 0
0 0
0.1 0
0 0
0.3 0.2
0 0.1
0.3 0.2
0 0
0 0
0 0.3
0 0
0 0.5
0.2 0
0.2 0.2
0 0 0
0 0 0
0.4 0 0
0.2 0 0
0 0.5 0
0.2 0 0.5
0 0.2 0.1
Ptie2-3, schedule = – 0.2×0.1 = – 0.02pu
Ptie2-4, schedule = -0.3×0.1 + [(0.2 + 0.1 + 0.2)*0.1 + (0.2 + 0.2)*0.1] = 0.06pu
Ptie3-4, schedule = (0.5 + 0.2+ 0.2)*0.1 = 0.09pu
For optimal design, we must formulate the state model. This is achieved by writing the differential equations
describing each individual block of figure in terms of state
0 0 0
0 0 0
0 0 0 0 0
0 0 0 0 0
variable. In this paper the dynamic performance is obtained using MATLAB software for , for
The cpf is the contract participation factor. In DPM diagonal element shows the local demand. The demand of one regions discos value to the another regions GENCO value is shown by the off diagonal element.
different load disruption.
Fig-2 Block diagram of four area interconnected power system under the deregulated environment
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Bacterial foraging optimization technique
It is recently epoch computation technique, named as Bacterial foraging(BF) which has been projected by Passino. The bacterial foraging optimized the controller gains and other parameters. The BF technique dependent on the deportment of E.coli bacteria which is found in the human intestine.[7] This
The bacteria generally found in groups and they will try to find food in minimum time with maximum energy and avoid the bruising phenomena. The detail algorithm is presented in Ref. [ 12]. In this simulation work the parameter for coding is to be S=10, Nc=10, Ns=3, Nre = 15, Ned=2, Ped=0.25.
D(attr.)=0.061, W(attr.) = 0.04, H(repellent)= 0.061,W(repellent)= 10 and P=18 considered.
= ( )2 + ( )2}
0
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Result And Analysis
The simulation is carried out on Four-Area interconnected deregulated system. The PI controller is implemented with and without bacterial foraging technique. The integral constant Ki is optimized and used in simulation in two different model of the system. In this system frequency of the system is compared. The tie line power is also considered before and after the deregulation. The simulation result are shown in fig(3) to fig(14). Using Simulink/MATLAB formulation the optimum AGC controller gain value, representing the scheduling of generators, tie line power exchange are done. With the help of BF algorithm frequency of the system are shown in fig(7) for four-Area conventional controller, with BF controller are considered.
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Frequency comparison of different areas
Fig (3) Frequency comparison of Area-1
Fig (4) Frequency comparison of Area-2
Fig(5) Frequency comparison of Area-3
FIG (6) Frequency comparison of Area-4
Fig (7) Frequency comparison with and without BF controller
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Tie-line power comparison
Fig8. DelPtie1-2 with and without BF controller
Fig9. DelPtie1-3 with and without BF controller
Fig10. DelPtie1-4 with and without BF controller
Fig11. DelPtie2-3 with and without BF controller
Fig12. DelPtie2-4 with and without BF controller
Fig13. DelPtie3-4 with and without BF controller
Fig14. Del-P tie line power of all four area with and without BF controller.
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Nomenclature
Deviation
s Derivative in terms of Laplace
f frequency
Angular speed
Tg Governor time Constant
Tij Coefficient of i-j tie Line
aij Operator
Bi Bias Factor
Pref The Output of ACE
Pl Electric Load Variations
R Regulation Parameter
apfi ACE Participation Factors DPM DISCO Participation Matrix cpfi Contract Participation Factors ACE Area Control Error
Pi-jactual Real Tie Line Power
Pi-jscheduled Scheduled Tie Line Power Flow
Pi-jerror Tie Line Power Error BF Bacterial foraging
Kp1,2,3 Generator Gain Constant Tp1,2,3 Generator Time Constant Pt Turbine output power
Tt Turbine time Constant
Pg Governor Output power
Tg Governor Time Constant
-
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CONCLUSION
This Paper encapsulates automatic generation control of the power system after deregulation includes bilateral contracts.DPM facilitates bilateral contracts simulation. Controller gains are optimized by both Bacterial Foraging and Proportional integral controller. This is study using simulation on a Four area power system considering different contracted scenarios. The dynamic and steady state responses for generated power change, for the frequency change and tie line powers change are shown in figure(7,) The simulation reveals that the proposed Bacterial Foraging based integral controller gives better performance than Proportional integral controller. This method reduces the peak deviation in frequencies and improves the tie line power.
APPENDIX-1
Base=1000MVA
Time constant Tps=2H/D
Tps1=16.669, Tps2=8.89, Tps3=16.669, Tps4=8.89
Power system Gain Kps=1/D
Kps1=1.66, Kps2=1.11, Kps3=1.66, Kps4=1.11,
Governor time constant (Tg) Tg1= Tg2= Tg3=0.067
Tg4= Tg5= Tg6 Tg7= Tg8=0.167 Tg9= Tg10=0.06
Tg11= Tg12= Tg13 Tg14= Tg15=0.06
Turbine time constant (Tt) Tt1= Tt2= Tt3=0.167
Tt4= Tt5= Tt6 Tt7= Tt8=0.06 Tt9= Tt10=0.25
Tt11= Tt12= Tt13 Tt14= Tt15=0.1
Murthal, So
Speed Regulation(R)
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-
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1 = 1 = 1
R1 R2 R3
=6.67
1 = 1
R4 R5
1 = 1
R1 R2
= 1 = 1 = 1
R6 R7 R8
= 10
= 3.2
1
R11
= 1
R12
= 1
R13
= 1
R14
= 1
R15
= 3.2
Frequency Bias Factor (B)
B1=20.9, B2=16.9, B3=20.9, B4=20.9, a12= a13= a14= a23= a24= a34=1