Available online at www.sciencedirect.com
ScienceDirect Energy Procedia 105 (2017) 2871 – 2878
The 8th International Conference on Applied Energy – ICAE2016
Multi-objective Optimal Hybrid Power Flow Algorithm for Integrated Community Energy System Wei Lina, Xiaolong Jina, Yunfei Mua*, Hongjie Jiaa, Xiandong Xub, Xiaodan Yua a Key Laboratory of Smart Grid of Ministry of Education, Tianjin University, Tianjin 300072, China School of Electronics, Electrical Engineering and Computer Science, Queen’s University Belfast, Belfast BT9 5 AH, UK
b
Abstract A multi-objective optimal hybrid power flow algorithm was proposed for multi-objective scheduling and management of the integrated community energy system (ICES). Firstly, an energy conversion analysis model for the energy center was developed based on the energy hub model. Then, a multi-objective optimal hybrid power flow algorithm is proposed to minimize the operation cost and total emission of the ICES considering the constraints from unbalanced three-phase electric distribution network, the natural gas network and the energy centers. Numerical results showed that the proposed multi-objective optimal hybrid power flow algorithm can be further used in the optimal day-ahead scheduling for the ICES, which considers the ICES’s multiple operation needs in aspects of security, economy and environmental friendliness. © Published by ElsevierPublished Ltd. This is an access article ©2017 2016 The Authors. byopen Elsevier Ltd. under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/). under responsibility Selection and/or peer-review Peer-review under responsibility of the scientific committee of theof 8thICAE International Conference on Applied Energy. Keywords: Integrated community energy system (ICES); energy hub; multi-objective optimal hybrid power flow; optimal day-ahead scheduling.
1. Introduction The increasing level of environmental pollution and energy crisis are the two main factors that restrict the development of future low-carbon cities [1]. In order to tackle these problems, more and more attention has been paid on the integrated community energy system (ICES) with couplings and interactions among various energy systems (e.g. electric power systems, natural gas supply systems, and heating systems) at the community level [2][3]. ICES is able to coordinate the above energy systems to provide new solutions for more secure, sustainable and economical energy production, distribution and consumption in the future low-carbon cites [4]. There are a number of ICES demonstration projects in China, such as the Langfang Eco-city, Sino-German Eco-park, Ubiquitous Energy Network in Zhaoqing New District, etc., which are in need of an effective method to schedule and coordinate the interrelated
* Yunfei Mu. Tel.: +86-1582-250-9583; fax: +86-022-27892809. E-mail address:
[email protected].
1876-6102 © 2017 Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/). Peer-review under responsibility of the scientific committee of the 8th International Conference on Applied Energy. doi:10.1016/j.egypro.2017.03.638
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energy systems of the ICES in an optimal way. Thus, the optimization, coordination and management of these various energy systems of ICES are of significant importance. The existing research works have made good contributions to the scheduling of ICES. However, the previous researches consider only the total cost of operation as the objective function of the problem [5]. However, there are other objectives that might be observed in an optimization process. One of them is the total emission of the system which is an attention-grabbing criterion these days. Therefore, a multi-objective optimal hybrid power flow algorithm was proposed to minimize the operation cost and total emission of the ICES. The proposed algorithm is helpful to find out all possible optimized operating points, called Pareto optimal curve, which provides a more flexible way for the ICES operators to coordinate the interrelated power, gas, and heating systems in the ICES for cost and total emission reduction.
K AC
Nomenclature
Thermal energy conversion rate of the
Abbreviations
CAC
ICES
Integrated community energy system
CHP
Combined heat and power
CAC
Central Air-conditioning
K ge
CHP
Conversion efficiency of gas into electricity through CHP
K gh
CHP
Indices
through CHP
t
Index of time intervals
i,j
Indices of electric bus
m,k
Indices of natural gas nodes
N
Total
number
of
eelec polluting
Emission coefficient of polluting gas produced by electric network
gas
produced by electric network n
Conversion efficiency of gas into heat
Total number of the energy centers
F EC
Emission coefficient of energy center
min max Pelec , Pelec Limits of electricity purchase
Parameters and constants
U imin , U i
Limits of bus voltage magnitude
Celec ,t
Electricity price at time period t
Sijmax
Maximum capacity of electric feeder
C gas,t
Natural gas price at time period t
k min , kmax Limits of natural gas compressor ratio
k
Fraction parameter of pipelines
pmin , pmax Limits of natural gas node pressure
Tk
Temperature of pipelines
Pemin , Pemax Limits of electric power exchange of
D
Specific heat ratio
q gas
Gross heating value of natural gas
Le, Lh
Electric power and heat power output of the energy center
K T , K GB Efficiency of the power transformer and the gas-boiler
max
energy center Pgmin , P
max g
Limits of natural gas power exchange
of energy center Variables P, Q
Active and reactive power of electric feeder
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V,
θ
p, F
Bus voltage magnitude and phase angle
kcp
Natural gas compressor ratio
of electric feeder
vAC
Electric partition coefficient
vCHP
Natural gas partition coefficient
Gas node pressure and gas pipeline flow
2. Model of the integrated community energy system (ICES) The ICES investigated in this paper consists of three parts, i.e., electric distribution network, natural gas network and the energy center. 2.1. Electric distribution network model The general equations for calculating active and reactive power of the network branch ij are shown in Eqs. (1) - (2). (1) Pij g si gij Vi2 gijViV j sinθij bijViV j cosθij Qij
bsi bij Vi2 bijViV j sinθij gijViV j cosθij
(2)
2.2. Natural gas network model The general equations for calculating gas flow are shown in Eqs. (3) - (4) [6]. Fkn
k kn skn skn pk2 pn2 skn
(3)
1 pk t pn ® ¯ 1 pk pn
(4)
Compressor stations are installed on gas pipelines to provide the pressure needed to transport gas from one location to another. The model of a transmission link with compressor and pipeline is shown in Fig. 1. A gas-fired compression station connected between nodes m and k is mathematically represented by its power consumption and compression ratio as shown in Eq. (5).
pm
n
k Fmn Fcp
Compressor
m
Fkn Pipeline
pk
pn
Fig.1 Natural gas pipeline model
Pcp
D º ª «§ pm · D 1 » ¸ ¨ k cp FknTk «¨ 1» ¸ » «© pk ¹ ¼ ¬
(5)
The volume flow of gas consumption by the compressor is given by Eq. (6). Fcp
Pcp / qgas
(6)
2.3. Energy center model The energy centers physically link different energy systems and provide possibility and flexibility to coordinate the different energy systems in an optimal way. In this paper, the energy conversion processes of the energy center under the hybrid thermal-electric load following mode are characterized in the energy hub model incorporating interactions among different energy systems and component constraints, as shown in Fig. 2 [7].
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Power transformer
Power transformer Electricity
Electricity
Electricity
Outputs
Inputs
Electricity
CAC
Inputs
Outputs CHP
CHP
Gas-boiler
Heat
NG
Heat
NG
(a) Type I---CHP and CAC
(b) Type II---CHP and gas-boiler
Fig.2 Structure of the energy hub model
Two types of energy hub structure are considered in this paper, as shown in Fig. 2. The first type of energy hub is composed of a power transformer, a CHP and a CAC group. The input energy consists of electricity and natural gas while the output energy consists of electric and heat loads. The couple relationship between input and output energy can be expressed by Eq. (7). ª Le º « » Lh ¼ ¬, L
CHP º ª1 v AC K T K ge ªP º » e « AC CHP « P » K gh »¼ , «¬ v ACK ¬ h¼
(7)
P
C
The second type of energy hub is composed of a power transformer, a CHP and a gas-boiler. The coupling relationship of input and output energy can be expressed by Eq. (8). CHP º ª Pe º ªK T vCHPK ge » « CHP GB « P » «¬ 0 vCHPK gh 1 vCHP K »¼ ¬, h¼
ª Le º « » ¬ Lh ¼ , L
(8)
P
C
3. Model of the integrated community energy system (ICES) 3.1. Objective function Two objective functions are considered in this paper, including the operation cost and total emission of ICES. The operation cost is depicted in Eq. (9), which consists of two terms: (1) the cost of purchasing electric power; (2) the cost of purchasing natural gas. (9) F1t Celec,t Pelec,t Cgas,t Fgas,t The total emission of ICES is depicted in Eq. (10), which consists of two terms: (1) the emission of electric network; (2) the emission of energy centers. F2 t Eelec EEC
¦
Eelec,i,t
i 1
¦
n
N
n
N
EEC, j ,t
j 1
¦ i 1
eelec,i Pelec,t
¦F
EC, j Lh, j ,t
(10)
j 1
3.2. Constraints 3.2.1Electric distribution network constraints min max Pelec d Pelec d Pelec
U imin
d U i d U imax
Sij d Sijmax
(11) (12) (13)
Eq. (11) is the electricity purchase constraint; Eq. (12) is the three-phase bus voltage constraint of the electric distribution network; Eq. (13) is the current constraint of the electric feeder. 3.2.2Natural gas network constraints kmin d kcp d kmax
(14)
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(15)
pmin d pk d pmax
Eq. (14) is the compressor ratio constraint; Eq. (15) is the node pressure constraint of the natural gas system. 3.2.3Energy center constraints Pemin d Pe d Pemax , Pgmin d Pg d Pgmax ° ° min max max Le PCHP , Pemax Le PAC / K AC ® Pe min max max CHP ° Pg 0 , Pg PCHP / K ge ° ¯
(16)
Pemin d Pe d Pemax , Pgmin d Pg d Pgmax ° max Pemin Le PCHP , Pemax Le ° ° min Pg Lh / K GB ® CHP · ° § ° P max P max / K CHP ¨ L P max u K gh ¸ / K GB g CHP ge h CHP CHP ¸ ¨ ° K ge © ¹ ¯
(17)
3.3. Solution The Non-dominated Sorting Genetic Algorithm II (NSAG-II) is widely used in dealing with multiobjective optimization problems. The proposed multi-objective optimal hybrid power flow algorithm in this paper is based on NAGA-II and the flowchart is shown in Fig. 3. 4. Case studies A typical ICES in Fig. 4 is utilized to verify the effectiveness of the developed multi-objective optimal hybrid power flow algorithm. Electric network
Selection, cross over, mutation
Start
Generate the initial population and set iteration count n=1
Satisfy all constraints ?
Solving hybrid power flow
Reproduce the population
799
Solving hybrid power flow
N
Y
Calculate the objective functions
Satisfy all constraints ? Y
712
742
705
729
744
Hub 9 (Type Ȼ)
Produce the offspring generation
N
Hub 3 (Type І)
Convergence condition is satisfied ?
722 704
702
727
730
Hub 6
736
Output the Pareto Optimal Front
Hub 8 (Type ȻȻ)
End
3
707 720
4
706
6 5
7
725
2
1 Hub 4 (Type ȻȻ)
Hub 1 (Type І)
8
10
731 9
733 710
718
709
708
N
Y
714
Hub 5 (Type І)
703
728 (Type ȻȻ)
Hub allocation
2
701
732
Calculate the objective functions
724
713
n=n+1
ICES initialization
Gas network Gas node Gas Gas network pipeline Gas load 1
Electric bus Electric branch
External grid
775
Hub 2 (Type ȻȻ)
734
13
Electric bus No.
Gas node No.
Hub 1
725
2
Hub 2
731
3
Hub 3
742
5
Hub 4
730
7
Hub 5
713
8
Hub 6
708
10
Hub 7
741
12
Hub 8
710
13
Hub 9
729
14
740
735 737
11 12
Hub No.
738
711
Fig.3 Flowchart of the multi-objective optimal hybrid power flow algorithm
741
Hub 7 (Type І)
14
Fig.4 Scheme of the ICES case
Electricity price
1
3
5
7
Natural gas price
9 11 13 15 17 19 21 23 Hour of day (h)
Fig.5. (a) Energy prices;
60 55 50 45 40 35 30 25 20
electirc load
100
heat load
90
Load of energy center (kW)
130 120 110 100 90 80 70 60 50
Natural gas price ($/MWh)
Electricity price ($/MWh)
The energy prices [8][9] and the electric and heat load of all energy centers are shown in Fig.5. The bus voltage is subject to the constraint of 0.9 dV d 1.1 and the pressure of natural gas pipelines is subject to the constraint of 0.2 d p d 1.3 . The emission coefficient of CO2, CO, SO2 and NOx are 0.8647, 0.008, 0.039 and 0.0309, respectively. The emission coefficient of the energy center is 0.04 [10]. 80 70 60
50 40 30 20 10 0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 Hour of day (h)
(b) Electric and heat load of energy centers
4.1. Single-objective optimization for operation cost minimization
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Energy price is an important factor for the optimization operation of ICES, so this paper compares two typical time periods (1 and 18) whose electricity prices are quite different. The optimal operation cost for time period 1 and 18 are 210.186 $ and 408.028 $, respectively. Tab.1 shows the operation of each energy center. Tab.1 Operation of energy centers Time period 1
Time period 18
Electric power (KWh)Natural gas power (KWh)Electric power (KWh)Natural gas power (KWh) EC1
65.375
0
84.250
0
EC2
55.750
64.167
1.750
225
EC3
65.375
0
84.250
0
EC4
55.750
64.167
1.750
225
EC5
65.375
0
84.250
0
EC6
55.750
64.167
1.750
225
EC7
65.375
0
84.250
0
EC8
55.750
64.167
1.750
225
EC9
65.375
0
84.250
0
As shown in Tab.1, for the first type of energy center, it tends to consume electricity only to meet the load in both the two time periods. For the second type of energy hub, it tends to consume both electricity and natural gas in time period 1 and consume natural gas mainly in time period 18. There are two main reasons for this phenomenon. Firstly, the primary energy efficiency of CAC for generating heat in the first type of energy hub is higher than that of the CHP for generating electricity and heat [11] [12]. Therefore, almost all heat loads are satisfied by CAC and electric load is satisfied by power transformer. Secondly, for the second type of energy center, it has more heat load and less electric load (high heat to power ratio) in time period 18, which matches the relative high heat to power ratio of CHP [13]. Therefore, all natural gas is utilized by CHP to meet electric and heat load. The electric bus voltage magnitude for time period 1 and 18 are shown in Fig. 6. The pressures of natural gas pipeline for two time periods are shown in Fig. 7. 1.02
0.98 0.96
C-phase
0.94
A-phase
0.92 0.9
0.98
C-phase
0.96 0.94
A-phase
0.92
1 0.9999 0.9998
0.9997 0.9996 0.9995 0.9994 0.9993
0.9
0.9992
799 775 702 713 727 704 720 712 725 724 708 732 710 736 741 718 734 738 729
799 775 702 713 727 704 720 712 725 724 708 732 710 736 741 718 734 738 729
Electric network buses number
Electric network buses number
Fig.6. (a) Electric bus voltage magnitude for time period 1
Time period 18
Time period 1
1.0001
B-phase
1
Node pressure/p.u.
B-phase
1
Voltage magnitude/p.u.
Voltage magnitude/p.u.
1.02
1
2
3
4
5
6
7
8
9
10
11
12
13
14
Natural gas network nodes number
(b) Electric bus voltage magnitude for time period 18
Fig.7 Natural gas network node pressure
4.2. Single-objective optimization for total emission minimization The optimal total emission of polluting gas for time period 1 and 18 are 1.929 ton and 1.966 ton, respectively. Tab.2 shows the operation of each energy center. Tab.2 Operation of energy centers Time period 1
Time period 18
Electric power (KWh)Natural gas power (KWh)Electric power (KWh)Natural gas power (KWh) EC1
-143.655
570.082
-129.066
581.772
EC2
12.452
EC3
-143.655
144.348
1.797
224.914
570.082
-129.066
581.772
EC4
12.452
144.348
1.797
224.914
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EC5
-143.655
570.082
-129.066
581.772
EC6
12.452
144.348
1.797
224.914
EC7
-143.655
570.082
-129.066
581.772
EC8
12.452
144.348
1.797
224.914
EC9
-143.655
570.082
-129.066
581.772
As shown in Tab.2, two types of energy centers tend to consume more natural gas and less electricity. And the first type of energy center injected extra electric power back into electric network. The reason is that the emission coefficient of energy center is lower than that of electric network. Therefore, all energy centers tend to purchase natural gas mainly. The electric bus voltage magnitudes for two time periods are shown in Fig. 8. The pressures of natural gas pipeline for two time periods are shown in Fig. 9. 1.02
1.02
0.99
C-phase
0.98
A-phase
0.97
1.01
1
B-phase
1 0.99
Node pressure/p.u.
Voltage magnitude/p.u.
Voltage magnitude/p.u.
B-phase
1
C-phase
0.98
A-phase
0.97
799 775 702 713 727 704 720 712 725 724 708 732 710 736 741 718 734 738 729
799 775 702 713 727 704 720 712 725 724 708 732 710 736 741 718 734 738 729
Electric network buses number
Electric network buses number
Fig.8. (a) Electric bus voltage magnitude for time period 1
0.998
0.996 0.994 0.992 0.99 0.988
0.96
0.96
Time period 18
Time period 1
1.002
1.01
0.986 1
2
3
4
5
6
7
8
9
10
11
12
13
14
Natural gas network nodes number
(b) Electric bus voltage magnitude for time period 18
Fig.9 Natural gas network node pressure
4.3. Multi-objective optimization The Pareto optimal curves of multi-objective optimization considering both the operation cost and total emission of ICES for time period 1 and 18 are shown in Fig. 10. The operation cost reduction and total emission reduction are two opposite objectives that decreasing one of them would increase the other one and vice versa. Furthermore, the results of single-objective optimization lie in the edges of the Pareto optimal curve, as shown in Fig. 10. Energy utilizations of the ICES for two time periods are shown in Tab. 3 and Tab. 4, from which the conclusion can be drawn that optimal schemes based on the proposed algorithm can balance both the operation cost and total emission of the ICES. The multi-objective optimal day-ahead scheduling schemes in a whole day for the ICES are shown in Fig. 11. Tab.3 Energy utilization of ICES for time period 1 Object
Electric power/KWh
Natural gas power/KWh
Cost optimization Emission optimization Multi-objective optimization
3061.800 2023.900 [2023.900,3061.800]
257.397 3425.300 [257.397,3425.300]
Object
Electric power/KWh
Natural gas power/KWh
Cost optimization Emission optimization Multi-objective optimization
2955.300 2050.500 [2050.500,2955.300]
912.219 3796.800 [912.219,3796.800]
Cost optimization
2.6 2.4 2.2 2 1.8 200
Emission optimization 220
240
260
Operation cost/$
280
300
Fig.10. (a) The Pareto optimal curve for time period 1
3
Total emission of polluting gas/ton
3 2.8
Total emission of polluting gas/ton
Total emission of polluting gas/ton
Tab.4 Energy utilization of ICES for time period 18
2.8
Cost optimization 2.6 2.4 2.2 2 1.8 405
Emission optimization 410
415
420
425
Operation cost/$
430
435
(b) The Pareto optimal curve for time period 18
440
3 2.5 2 1.5 500 30
400
20
300
Operation cost/$
10 200
0
Time/h
Fig.11 Day-ahead optimal scheduling scheme
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5. Conclusion A multi-objective optimal hybrid power flow algorithm for the ICES considering both the operation cost and total emission of the ICES was developed in this paper. The constraints from electric distribution network, the natural gas network and energy centers were considered in the proposed algorithm. The proposed algorithm is helpful to find out all possible optimized operating points, called Pareto optimal curve, which provides a more flexible way for the ICES operators to coordinate the interrelated power, gas, and heating systems in the ICES for cost and total emission reduction. Acknowledgements This work was financially supported by the National High-tech R&D Program of China (863 Program with No. 2015AA050403), the project National Natural Science Foundation of China (Grant No. 51307115, 51377117, and 51277128), Science and Technology Project of Tianjin Electric Power Corporation (Forecast and Coordination Control Technique of Smart Grid Park). References [1] Dong R,Yu Y,Zhang Z. Simultaneous optimization of integrated heat, mass and pressure exchange network using exergoeconomic method. Appllied Energy 2014;136:1098–1109. [2] Keirstead J, Jennings M, Sivakumar A. A review of urban energy system models: Approaches, challenges and opportunities. Renewable and Sustainable Energy Reviews 2012; 16(6):3846–3866. [3] Zhang X, Karady G G, Piratla K R, et al. Network capacity assessment of combined heat and power-based distributed generation in urban energy infrastructures. IEEE Trans Smart Grid 2013; 4(4):2131–2138. [4] Mendes G, Ioakimidis C, Ferrao P. On the planning and analysis of integrated community energy systems: A review and survey of available tools. Renewable and Sustainable Energy Reviews 2011; 15(9):4836–4853. [5] Zhou R, Li S, Chen R, et al. Combined cool and heat and power multi-objective scheduling considering carbon emissions trading using algorithm of fuzzy self-correction particle swarm optimization. Proceedings of CSSE 2014;34(34):6119-6126. [6] Jiang M, Xu Y, Wang S, et al. Simulation and analysis of gas transmission and distribution network. Beijing: Petroleum Industry Press, 1995. [7] Xu X, Jia H, Jin X, et al. Study on hybrid heat-gas-power flow algorithm for integrated community energy system. Proceedings of CSSE 2015; 35(14):3634-3642. [8] (2015, Jan) New Yorker Independent System Operator. Available: http://www.nyiso.com. [9] Pacific Gas& Electric Tariffs. A-10 TOU, 200-500kW. Available: http://www.pge.com/tariffs/electric.shtml. [10] Wei X, Zhou H. Evaluating the environmental value schedule of pollutions mitigated in China thermal power industry. Research of Environmental Science 2003; 16(1): 53-56. [11] Adnot J, Riviere P, Marchio D, et al. Energy efficiency and certification of central air conditioners. Study for the DG transportation-energy of the Commission of the EU-final report 2003. [12] Kaikko J, Backman J. Technical and economic performance analysis for a microturbine in combined heat and power generation. Energy 2007; 32(4): 378-387. [13] Huang Y, Mcllveen D R, Rezvani S, et al. Comparative techno-economic analysis of biomass fuelled combined heat and power for commercial buildings. Applied Energy 2013; 112:518-522.
Biography Wei Lin received the B.S. degree in electrical engineering from Tianjin University, China, in 2016. His research interests include the operation optimization and energy management of integrated energy systems.