Optimal operation of integrated energy system including power thermal and gas subsystems
Tongming LIU1(), Wang ZHANG1, Yubin JIA2, Zhao Yang DONG3()
1. Digital Grid Futures Institute, The University of New South Wales, Sydney NSW-2052, Australia 2. School of Automation, Southeast University, Nanjing 210000, China 3. School of Electrical & Electronics Engineering, Nanyang Technological University, Singapore 639798, Singapore
As a form of hybrid multi-energy systems, the integrated energy system contains different forms of energy such as power, thermal, and gas which meet the load of various energy forms. Focusing mainly on model building and optimal operation of the integrated energy system, in this paper, the dist-flow method is applied to quickly calculate the power flow and the gas system model is built by the analogy of the power system model. In addition, the piecewise linearization method is applied to solve the quadratic Weymouth gas flow equation, and the alternating direction method of multipliers (ADMM) method is applied to narrow the optimal results of each subsystem at the coupling point. The entire system reaches its optimal operation through multiple iterations. The power-thermal-gas integrated energy system used in the case study includes an IEEE-33 bus power system, a Belgian 20 node natural gas system, and a six node thermal system. Simulation-based calculations and comparison of the results under different scenarios prove that the power-thermal-gas integrated energy system enhances the flexibility and stability of the system as well as reducing system operating costs to some extent.
Corresponding Author(s):
Tongming LIU,Zhao Yang DONG
引用本文:
. [J]. Frontiers in Energy, 2022, 16(1): 105-120.
Tongming LIU, Wang ZHANG, Yubin JIA, Zhao Yang DONG. Optimal operation of integrated energy system including power thermal and gas subsystems. Front. Energy, 2022, 16(1): 105-120.
Indices of gas flow direction signal in pipeline ij
CHP
Indices of gas flow direction signal CHP unit
Set of pipelines with node i as the front section
Set of pipelines with node i as the end section
ψ
Thermal load power
The amount of gas consumption by the compressor/m3
rcp
Compressor pressure ratio
BE
The benefit of electricity consumers expect gas-fired generator
BG
The benefit of gas consumers expect gas-fired generator
CE
The cost of traditional electrical generation
CG
The cost of gas well
CCHP
The cost of CHP unit
PtG system of unit i at time tin the base case
Commitment statuses of unit i at time tin the base case
m
The water flow through pipeline in the system/(m3?s–1)
mn
The node water outflow in the system/(m3?s–1)
pCHP
Electric power output by CHP unit/MW
φCHP
Thermal power output by CHP unit/MW
pi
Gas subsystem node ipressure value/kPa
Active power outputs of gas-fired units/MW
PPtG
Active power outputs of PtG system/MW
QEB
The produced thermal energy (kJ) of electric boiler/MW
PEB
The consumed electricity of electric boiler/MW
Gas flow value of gas pipeline ij/(m3?h–1)
SG,cp
Gas flow value through compressor/(m3?h–1)
Startup cost of unit i at time t
Shutdown cost of unit i at time t
The mixed temperature at node iof water supply system/K
The mixed temperature at node iof water return system/K
The outlet water temperature of pipeline l/K
The inlet water temperature of pipeline l/K
The efficiency parameters of gas-fired generator
Vi
Voltage magnitude of bus i
ON counter of unit iat time t
OFF counter of unit iat time t
The coefficients of the gas compressor between node ij
The gas supply value at node i/m3
The gas demand value at node i/m3
The coefficients of non-gas generator cost
The coefficients of electrical consumer’s benefit
The coefficients of gas consumer’s benefit
Ccp
Scale factor of gas consumption by compressor
Ci
Scale factor of gas consumption by Well-head gas price/($?(109J)–1)
CG,F
Energy conversion coefficient of gas-fired units
Cp
The specific heat capacity of the heat medium of pipe l/m
λl
The specific heat capacity of the heat transfer coefficient of pipe l/m
L
The specific heat capacity of the length of pipe l/m
HPij
The horsepower of gas compressor (1 hp= 745.7 W)
K
The number of extreme operating points of CHP unit at time t
RAir
The air specific gravity at average temperature.
KG
The air constant in relation to RAir/gas specific gravity (air= 1.0, gas= 0.6)
Lij
Length of gas subsystem pipe ij
Dij
Internal diameter of gas subsystem pipe ij/m3
Fij
Dimensionless friction factor of gas subsystem pipe ij
NE
Total number of power subsystem buses
NG
Total number of natural gas subsystem nodes
NL
Total number of electric consumers
NH
Total number of heat consumers
Pk
Electric power value at kextreme point in CHP feasible region/MW
Φk
Thermal power value at kextreme point in CHP feasible region/MW
The lost active power at branch i/MW
The lost reactive power at branch i/MW
Forecast load value in power subsystem/MW
The gross heating value/()
Power flow in power subsystem at the head of branch/MW
Generated power from distributed generator/MW
Load demand at branch /MW
Lateral branch power flow of branch/MW
SRt
System spanning reserve at time t/MW
Minimum ON time of unit i
Minimum OFF time of unit i
URi
Ramp up rate of unit i
DRi
Ramp down rate of unit i
Z
Compressibility factor of natural gas/K
Ta
Average temperature of natural gas/K
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