CN115099007A - Comprehensive energy system optimized operation method based on comprehensive cost-energy consumption curve - Google Patents

Comprehensive energy system optimized operation method based on comprehensive cost-energy consumption curve Download PDF

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CN115099007A
CN115099007A CN202210608295.5A CN202210608295A CN115099007A CN 115099007 A CN115099007 A CN 115099007A CN 202210608295 A CN202210608295 A CN 202210608295A CN 115099007 A CN115099007 A CN 115099007A
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comprehensive
cost
energy consumption
gas
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CN115099007B (en
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李鹏
王加浩
王子轩
文淼
韩中合
潘有朋
殷云星
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North China Electric Power University
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    • GPHYSICS
    • G06COMPUTING; CALCULATING OR COUNTING
    • G06FELECTRIC DIGITAL DATA PROCESSING
    • G06F30/00Computer-aided design [CAD]
    • G06F30/20Design optimisation, verification or simulation
    • GPHYSICS
    • G06COMPUTING; CALCULATING OR COUNTING
    • G06QINFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES; SYSTEMS OR METHODS SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES, NOT OTHERWISE PROVIDED FOR
    • G06Q10/00Administration; Management
    • G06Q10/06Resources, workflows, human or project management; Enterprise or organisation planning; Enterprise or organisation modelling
    • G06Q10/063Operations research, analysis or management
    • G06Q10/0631Resource planning, allocation, distributing or scheduling for enterprises or organisations
    • G06Q10/06315Needs-based resource requirements planning or analysis
    • GPHYSICS
    • G06COMPUTING; CALCULATING OR COUNTING
    • G06QINFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES; SYSTEMS OR METHODS SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES, NOT OTHERWISE PROVIDED FOR
    • G06Q50/00Systems or methods specially adapted for specific business sectors, e.g. utilities or tourism
    • G06Q50/06Electricity, gas or water supply
    • GPHYSICS
    • G06COMPUTING; CALCULATING OR COUNTING
    • G06FELECTRIC DIGITAL DATA PROCESSING
    • G06F2111/00Details relating to CAD techniques
    • G06F2111/06Multi-objective optimisation, e.g. Pareto optimisation using simulated annealing [SA], ant colony algorithms or genetic algorithms [GA]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y04INFORMATION OR COMMUNICATION TECHNOLOGIES HAVING AN IMPACT ON OTHER TECHNOLOGY AREAS
    • Y04SSYSTEMS INTEGRATING TECHNOLOGIES RELATED TO POWER NETWORK OPERATION, COMMUNICATION OR INFORMATION TECHNOLOGIES FOR IMPROVING THE ELECTRICAL POWER GENERATION, TRANSMISSION, DISTRIBUTION, MANAGEMENT OR USAGE, i.e. SMART GRIDS
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    • Y04S10/50Systems or methods supporting the power network operation or management, involving a certain degree of interaction with the load-side end user applications

Abstract

An integrated energy system optimization operation method based on an integrated cost-energy consumption curve comprises the following steps: establishing a park comprehensive energy system integrated model considering variable working condition characteristics of energy conversion equipment; constructing a comprehensive cost-energy consumption curve facing the multi-energy consumption requirement of the park; calculating an optimized operation scheme of the comprehensive energy system based on the comprehensive cost-energy consumption curve; the invention establishes the integrated model of the comprehensive energy system considering the variable working condition running characteristics of the multi-type energy conversion equipment, and effectively reduces the energy deviation between the optimized scheduling scheme and the actual load requirement; a comprehensive cost-energy consumption curve facing the multi-energy consumption requirement of the park is constructed, and guidance can be provided for scheduling personnel in actual engineering application through analysis and calculation of a curve image guidance optimization operation strategy; the method can effectively give consideration to model precision and solving efficiency, greatly improves the accuracy of the optimized operation scheme, and ensures shorter optimized calculation time.

Description

Comprehensive energy system optimization operation method based on comprehensive cost-energy consumption curve
Technical Field
The invention relates to an optimized operation method of a comprehensive energy system. In particular to an optimized operation method of a comprehensive energy system based on a comprehensive cost-energy consumption curve.
Background
The comprehensive energy system can fully exert the comprehensive advantages of complementation and mutual assistance of various heterogeneous energy sources, and the development of the comprehensive energy system has great significance for building a clean, low-carbon, safe and efficient modern energy system. The park comprehensive energy system serves as a terminal for energy interconnection, and can provide reliable and economic energy supply for users in the park by coordinating various energy devices.
Because the collaborative optimization operation model of the park comprehensive energy system is extremely complex, the current research is usually simplified to a certain extent, and most typically, the efficiency of the energy conversion equipment is set to be a constant. In practice, the efficiency of the energy conversion device may vary with load factor, temperature, air pressure, etc. However, the overall consideration of the variable working condition operation characteristics of various types of energy conversion equipment by domestic and foreign researches is not enough, and the solution of the optimized operation strategy faces the contradiction between the requirement of solution precision and the complexity of the model.
The cooperative optimization operation problem of the park comprehensive energy system considering the variable working condition characteristics of the equipment is a typical non-convex optimization problem. The common solution thought of the non-convex optimization problem in engineering can be divided into piecewise linear function approximation and heuristic algorithm. However, error accumulation is easy to form by utilizing a piecewise linear function, and the solving precision is limited by the number of segments; the solution is unstable by using a heuristic algorithm, and the approximation degree of the obtained solution and the optimal solution is difficult to explain. In view of this, it is necessary to design an optimal operation scheme calculation strategy that takes model precision and solution efficiency into consideration.
Disclosure of Invention
The invention aims to solve the technical problem of providing an optimized operation method of a comprehensive energy system based on a comprehensive cost-energy consumption curve, which can take model precision and solving efficiency into consideration, in order to overcome the defects of the prior art.
The technical scheme adopted by the invention is as follows: an integrated energy system optimization operation method based on an integrated cost-energy consumption curve comprises the following steps:
1) establishing a park comprehensive energy system integrated model considering variable working condition characteristics of energy conversion equipment; comprises that
(1.1) establishing a variable working condition operation model of energy conversion equipment of a combined heat and power generation unit, a gas boiler, an absorption refrigerator and an electric refrigerator, wherein the variable working condition operation model of the energy conversion equipment is as follows:
Figure BDA0003672419740000011
wherein, P out For outputting energy, P, to energy-converting apparatus in Energy is input to the energy conversion device, eta is the energy conversion efficiency of the energy conversion device, eta R For the energy conversion efficiency of the energy conversion device under rated operating conditions,
Figure BDA0003672419740000012
the efficiency correction coefficient is the efficiency correction coefficient of a cogeneration unit or a gas boiler or an absorption refrigerator or an electric refrigerator;
(1.2) establishing an integrated model of the comprehensive energy system;
2) constructing a comprehensive cost-energy consumption curve facing the multi-energy consumption requirement of the park; the method comprises the following steps:
(2.1) integrating an objective function of the optimized operation of the comprehensive energy system;
(2.2) constructing a net cost-output curve of the energy conversion equipment;
(2.3) constructing a comprehensive cost-energy consumption curve facing the multi-element energy consumption requirement of the park;
and (2.4) carrying out regional division on the comprehensive cost-energy consumption curve of the diversified energy consumption requirements of the facing park.
3) Calculating an optimized operation scheme of the comprehensive energy system based on the comprehensive cost-energy consumption curve; comprises that
(3.1) calculating an optimized operation scheme of the comprehensive energy system without the energy storage equipment;
and (3.2) calculating an optimized operation scheme of the integrated energy system comprising the energy storage equipment.
The efficiency correction coefficients of the cogeneration unit, the gas boiler, the absorption chiller and the electric chiller in the step 1) and the step 1.1 are respectively as follows:
efficiency correction coefficient of cogeneration unit:
Figure BDA0003672419740000021
Figure BDA0003672419740000022
wherein the content of the first and second substances,
Figure BDA0003672419740000023
the efficiency correction coefficient of the cogeneration unit; k is a radical of CHP,n An n-order fitting coefficient of the electric efficiency of the cogeneration unit; n is a radical of CHP The electric load rate of the cogeneration unit;
Figure BDA0003672419740000024
the correction coefficient is the heat-electricity ratio of the cogeneration unit; k is a radical of α,n Fitting coefficients of an nth order of a thermoelectric ratio of the cogeneration unit;
efficiency correction factor of gas boiler:
Figure BDA0003672419740000025
wherein, the first and the second end of the pipe are connected with each other,
Figure BDA0003672419740000026
correcting the coefficient for the efficiency of the gas boiler; k is a radical of GB,n An n-order fitting coefficient of the gas boiler efficiency; n is a radical of GB Is the load factor of the gas boiler;
efficiency correction coefficient of absorption chiller:
Figure BDA0003672419740000027
wherein the content of the first and second substances,
Figure BDA0003672419740000028
correcting the coefficient for the efficiency of the absorption chiller; k is a radical of AC,n Is an n-order fitting coefficient of the efficiency of the absorption refrigerator; n is a radical of AC Is the load factor of the absorption chiller;
efficiency correction coefficient of electric refrigerator:
Figure BDA0003672419740000029
wherein the content of the first and second substances,
Figure BDA00036724197400000210
the efficiency correction factor of the electric refrigerator is obtained; k is a radical of EC,n Fitting coefficients of the n orders of the efficiency of the electric refrigerator; n is a radical of EC Is the load factor of the electric refrigerator.
Step 1) the integrated model of the comprehensive energy system in the step (1.2) is as follows:
Figure BDA00036724197400000211
wherein f is 1 ,f 2 ,…,f n An objective function for optimizing operation of the integrated energy system; g () is a supply and demand balance expression of the comprehensive energy system; g () is a device constraint expression of the comprehensive energy system; i represents the ith energy in the comprehensive energy system, C is cold, H is hot, E isElectricity, G is gas; x is the number of i A parameter representing the ith class of energy; t is a time scale; xi is an uncertain variable; l is the load demand; p is an output energy value of the energy supply equipment or the energy conversion equipment or the distribution network, namely an output value; h () is a coupling transformation matrix; η is the energy conversion efficiency of the energy conversion device.
The objective function of the optimized operation of the integrated comprehensive energy system in the step 2) and the step 2.1 is as follows:
Figure BDA0003672419740000031
f is the comprehensive cost of the optimized operation of the comprehensive energy system after multi-objective integration by using a membership function; f. of 1 ,f 2 ,…,f n Optimizing an objective function for operation of the integrated energy system; u is the energy conversion device type; f u Represents the net cost of the energy conversion device; s i Representing the energy cost of the ith type of energy; l is i Load demand for class i energy; f i The comprehensive cost of the i-th energy is obtained; delta is a repeated calculation part caused by the energy conversion equipment simultaneously generating multiple energies; omega is an energy conversion equipment set; i represents the ith type of energy in the comprehensive energy system of cold, heat, electricity and gas, C is cold, H is heat, E is electricity and G is gas.
Step 2) the net cost-output curve of the energy conversion equipment in the step (2.2) is a curve drawn according to the net cost-output function of the energy conversion equipment of the cogeneration unit, the gas boiler, the absorption refrigerator and the electric refrigerator; the net cost-out function of the energy conversion device is:
Figure BDA0003672419740000032
wherein, F u Represents the net cost of the energy conversion device;
Figure BDA0003672419740000033
for the output value of the energy conversion device u, the superscript ij represents the energyThe quantity conversion equipment u converts the ith type energy into the jth type energy; s i Representing the energy cost of the ith type of energy; s j Representing the energy cost of the j-th energy;
Figure BDA00036724197400000313
the energy conversion efficiency of the energy conversion device u; d u Loss of the energy conversion device u; i and j respectively represent the i and j energy in the cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is hot, E is electricity and G is gas.
Step 2) constructing a comprehensive cost-energy consumption curve facing the multi-energy consumption requirement of the park in the step (2.3), wherein the curve is drawn according to a comprehensive cost-energy consumption function; the integrated cost-energy consumption function is:
Figure BDA0003672419740000034
wherein, F i The comprehensive cost of the i-th energy is obtained; f u Net cost for energy conversion equipment;
Figure BDA0003672419740000035
is the output value of the energy conversion device u; s i Energy cost for class i energy; i represents the ith type of energy in cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is heat, E is electricity and G is gas;
Figure BDA0003672419740000036
for the actual energy demand of the ith type of energy in the park, the numerical value satisfies the following constraints:
Figure BDA0003672419740000037
Figure BDA0003672419740000038
wherein L is i Load demand for class i energySolving;
Figure BDA0003672419740000039
the energy conversion efficiency of the energy conversion device u;
Figure BDA00036724197400000310
is the output value of the energy supply device v; v is a set of energy supply devices;
Figure BDA00036724197400000311
outputting an energy value upper limit for the distribution network with the ith type of energy;
Figure BDA00036724197400000312
is the upper limit of the output value of the energy conversion device u;
Figure BDA0003672419740000041
is the upper limit of the output value of the energy supply device v.
Step 2), performing area division on the comprehensive cost-energy consumption curve of the diversified energy consumption demand of the facing park in the step (2.4), wherein the area division includes the division into an optimizable area and a conservation and supply area, and the optimizable area comprises: the energy supply system comprises a self-energy supply area, an energy purchasing area and an energy conversion area I, wherein a supply area is an energy conversion area II; wherein:
(2.4.1) self-energizing zone: the energy consumption of the park is generated by wind and light renewable energy sources in the park, and the unit energy consumption cost is lower than that of energy purchasing;
(2.4.2) energy purchase zone: energy consumption of the park is met by purchasing energy through an external network;
(2.4.3) energy conversion zone I: the energy consumption of the garden is met by energy conversion equipment, and the unit energy consumption cost is lower than that of energy purchasing;
(2.4.4) energy conversion zone II: the energy consumption of the park is met by energy conversion equipment, and the unit energy consumption cost is higher than the energy purchasing cost.
Step 3) the calculation of the optimized operation scheme of the comprehensive energy system without the energy storage device in the step (3.1) comprises the following steps:
(3.1.1) respectively constructing 24 groups of corresponding comprehensive cost-energy consumption curves 24 hours a day according to the comprehensive cost-energy consumption function in the step 2 and the step 2.3 in consideration of time-of-use electricity price, wherein each group of comprehensive cost-energy consumption curves comprises 4 curves of a cold energy comprehensive cost-energy consumption curve, a heat energy comprehensive cost-energy consumption curve, an electric energy comprehensive cost-energy consumption curve and a gas energy comprehensive cost-energy consumption curve;
(3.1.2) establishing 24 groups of energy distribution data tables containing output and purchased energy of park energy equipment according to 24 groups of comprehensive cost-energy consumption curves, wherein each group of energy distribution data tables comprises 4 tables of cold energy distribution, heat energy distribution, electric energy distribution and gas energy distribution;
(3.1.3) according to the comprehensive cost-energy consumption curve of the cold energy and by combining a cold energy distribution data table, obtaining the output conditions of the electric refrigerator and the absorption refrigerator;
(3.1.4) superposing the electric energy demand generated by the electric refrigerator to the total electric energy consumption amount, and obtaining the electricity purchasing quantity, the wind power and photovoltaic power generation quantity and the cogeneration output condition of the park according to the electric energy comprehensive cost-energy consumption curve and in combination with an electric energy distribution data table;
(3.1.5) superposing the heat energy demand generated by the absorption refrigerator to the total heat energy consumption, and combining a heat energy distribution data table according to a heat energy comprehensive cost-energy consumption curve to obtain the heat purchasing quantity of the park, the cogeneration output condition and the gas boiler output condition;
(3.1.6) judging whether the cogeneration output in the step (3.1.4) and the step (3.1.5) is the same, if not, taking a value with large cogeneration output according to a net cost-output curve of cogeneration if the cogeneration output is in a profit region; if the boiler is in a loss area and the gas boiler is not fully loaded, taking a value with small cogeneration output under the premise of meeting the equipment constraint of the comprehensive energy system; then, setting the cogeneration output as a fixed value, obtaining the park electricity purchasing quantity, the wind power generation quantity and the photovoltaic power generation quantity again according to the electric energy comprehensive cost-energy consumption curve and the electric energy distribution data table, and obtaining the park heat purchasing quantity and the gas boiler output condition according to the heat energy comprehensive cost-energy consumption curve and the heat energy distribution data table;
(3.1.7) superposing the gas energy requirements generated by cogeneration and a gas boiler to the total gas energy consumption, and combining a gas energy distribution data table according to a gas energy comprehensive cost-energy consumption curve to obtain the gas purchasing quantity of the park;
and (3.1.8) calculating the comprehensive cost of the optimized operation of the comprehensive energy system by combining 24 groups of comprehensive cost-energy consumption curves to obtain the optimized operation scheme of the comprehensive energy system.
Step 3) in the step (3.2), the energy storage using modes are firstly divided into an energy storage using mode 1 and an energy storage using mode 2, and the meanings are as follows:
energy storage usage mode 1: storing the energy which can meet the energy consumption requirement in the period a and can be supplied by the optimized area to replace the period b;
energy storage use mode 2: and storing the low-cost external network energy purchasing energy after the c-period optimizable area meets the energy consumption requirement, and replacing the high-cost external network energy purchasing energy needed by the d-period optimizable area.
Step 3) the calculation of the optimal operation scheme of the integrated energy system including the energy storage device in the step (3.2) comprises the following steps:
(3.2.1) calculating the residual energy value of each energy optimizing area and the using energy value of the reserve supply area in 24 periods of cold, heat, electricity and gas according to the optimized operation scheme of the comprehensive energy system obtained in the step (3.1), wherein the calculation formula is as follows:
Figure BDA0003672419740000051
Figure BDA0003672419740000052
wherein the content of the first and second substances,
Figure BDA0003672419740000053
optimizing the zone residual energy value for the ith type energy t period;
Figure BDA0003672419740000054
the energy using value of the supply area is guaranteed for the ith type energy t period;
Figure BDA0003672419740000055
outputting an energy value upper limit for the distribution network with the ith type of energy;
Figure BDA0003672419740000056
is the upper limit of the output value of the energy conversion device w; w is an energy conversion equipment set of the energy conversion I area;
Figure BDA0003672419740000057
is the upper limit of the output value of the energy supply device v; v is a set of energy supply devices;
Figure BDA0003672419740000058
the actual energy demand of the ith type of energy in the park; i represents the ith type of energy in cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is heat, E is electricity and G is gas;
(3.2.2) calculating an energy storage use scheme under the energy storage use mode 1, wherein the calculation formula of the energy storage use scheme is as follows:
Figure BDA0003672419740000059
wherein, y i For the optimization target of the ith type of energy in the energy storage use mode 1, i represents the energy generated by various types of energy sources such as cold, heat, electricity and gas of the comprehensive energy system; t is a scheduling period of 24 h;
Figure BDA00036724197400000510
the output energy value of the energy storage device t time period of the ith type of energy;
Figure BDA00036724197400000511
the upper limit of the energy storage/release power of the energy storage device for the ith type of energy in unit time;
Figure BDA00036724197400000512
judging the energy storage working mode for the ith type energy t time period, if so
Figure BDA00036724197400000513
Then
Figure BDA00036724197400000514
Otherwise, the reverse is carried out
Figure BDA00036724197400000515
M is a set constant;
Figure BDA00036724197400000516
storing an energy value for the energy storage device for the ith type energy t time period;
Figure BDA00036724197400000517
storing an energy value for the energy storage device in the ith type energy t-1 time period;
Figure BDA00036724197400000518
the self-discharge rate of the energy storage device for the ith type of energy;
Figure BDA00036724197400000519
and
Figure BDA00036724197400000520
the upper limit and the lower limit of the stored energy value of the energy storage device of the ith type of energy respectively;
(3.2.3) superposing the energy storage use scheme obtained in the step (3.2.2) to the total electric energy consumption, the total heat energy consumption, the total gas energy consumption and the total cold energy consumption in the step (3.1) in the step (3), and recalculating the optimized operation scheme of the comprehensive energy system;
(3.2.4) calculating the secondary residual energy value of each energy optimizing area and the secondary using energy value of the supply area in 24 time intervals, wherein the calculation formula is as follows:
Figure BDA00036724197400000521
Figure BDA00036724197400000522
wherein the content of the first and second substances,
Figure BDA00036724197400000523
the secondary residual energy value of the optimization area is the ith type energy t time period;
Figure BDA00036724197400000524
ensuring the secondary use energy value of the supply area for the ith type energy t period;
(3.2.5) respectively judging whether the sum of the secondary use energy values of 24 time-keeping supply areas of cold, heat, electricity and gas is 0, if so, performing the step (3.2.6); if not, performing the step (3.2.7);
(3.2.6) calculating the energy storage usage scheme in the energy storage usage mode 2 according to the following formula:
Figure BDA0003672419740000061
wherein, Δ y i An optimization target of the ith type of energy in the energy storage use mode 2 is obtained;
Figure BDA0003672419740000062
the correction quantity of the energy value is output for the ith type energy storage device in the t period;
Figure BDA0003672419740000063
outputting an energy value for the distribution network in the ith type energy t period;
Figure BDA0003672419740000064
the energy consumption unit cost of the energy storage device for the ith type of energy;
Figure BDA0003672419740000065
energy cost of ith type of energy in t period;
(3.2.7) the energy storage use scheme in the energy storage use mode 1, the energy storage use scheme in the energy storage use mode 2 and the recalculated comprehensive energy system optimized operation scheme jointly form an optimized operation scheme of the comprehensive energy system comprising the energy storage equipment; at the moment, the comprehensive energy cost calculation formula of the comprehensive energy system is as follows:
Figure BDA0003672419740000066
wherein F is the comprehensive cost of the optimized operation of the comprehensive energy system; f i The comprehensive cost of the i-th energy is obtained; delta is the iterative part of the calculation resulting from the simultaneous generation of multiple energies by the energy conversion device.
The comprehensive energy system optimization operation method based on the comprehensive cost-energy consumption curve has the following advantages:
1. the invention establishes the integrated model of the comprehensive energy system considering the variable working condition operation characteristics of the multi-type energy conversion equipment, and effectively reduces the energy deviation between the optimized scheduling scheme and the actual load requirement.
2. The comprehensive cost-energy consumption curve oriented to the multi-energy consumption requirement of the park is constructed, and guidance can be provided for scheduling personnel in actual engineering application through analysis and calculation of the curve image guidance optimization operation strategy.
3. The method can effectively give consideration to model precision and solving efficiency, greatly improves the accuracy of the optimization operation scheme, and ensures shorter optimization calculation time.
Drawings
FIG. 1 is a graphical representation of the overall cost-energy curve of the present invention;
FIG. 2 is a schematic diagram of an example of the integrated energy system of the intelligent town park of Xiandan according to the present invention.
Detailed Description
The method for optimizing the operation of the integrated energy system based on the integrated cost-energy consumption curve according to the present invention is described in detail below with reference to the following embodiments and the accompanying drawings.
The invention relates to an optimized operation method of a comprehensive energy system based on a comprehensive cost-energy consumption curve, which comprises the following steps:
1) establishing a park comprehensive energy system integrated model considering variable working condition characteristics of energy conversion equipment; comprises that
(1.1) establishing a variable working condition operation model of energy conversion equipment of a cogeneration unit, a gas boiler, an absorption refrigerator and an electric refrigerator, wherein the variable working condition operation model of the energy conversion equipment comprises the following steps:
Figure BDA0003672419740000071
wherein, P out For outputting energy, P, to energy-converting apparatus in Energy is input to the energy conversion device, eta is the energy conversion efficiency of the energy conversion device, eta R For the energy conversion efficiency of the energy conversion device under rated operating conditions,
Figure BDA0003672419740000072
the efficiency correction coefficient is the efficiency correction coefficient of a cogeneration unit or a gas boiler or an absorption refrigerator or an electric refrigerator; wherein, the efficiency correction coefficients of the cogeneration unit, the gas boiler, the absorption refrigerator and the electric refrigerator are respectively as follows:
efficiency correction coefficient of cogeneration unit:
Figure BDA0003672419740000073
Figure BDA0003672419740000074
wherein the content of the first and second substances,
Figure BDA0003672419740000075
the efficiency correction coefficient of the cogeneration unit; k is a radical of CHP,n The fitting coefficient is the n-order fitting coefficient of the electric efficiency of the cogeneration unit; n is a radical of CHP The electric load rate of the cogeneration unit;
Figure BDA0003672419740000076
the correction coefficient is the heat-electricity ratio of the cogeneration unit; k is a radical of formula α,n Fitting coefficients of an nth order of a thermoelectric ratio of the cogeneration unit;
efficiency correction factor of gas boiler:
Figure BDA0003672419740000077
wherein, the first and the second end of the pipe are connected with each other,
Figure BDA0003672419740000078
the efficiency correction coefficient of the gas boiler; k is a radical of GB,n An n-order fitting coefficient for the gas boiler efficiency; n is a radical of GB Is the load factor of the gas boiler;
efficiency correction coefficient of absorption chiller:
Figure BDA0003672419740000079
wherein, the first and the second end of the pipe are connected with each other,
Figure BDA00036724197400000710
the efficiency correction factor of the absorption refrigerator; k is a radical of AC,n Fitting coefficients of order n for the efficiency of the absorption chiller; n is a radical of AC Is the load factor of the absorption chiller;
efficiency correction coefficient of electric refrigerator:
Figure BDA00036724197400000711
wherein the content of the first and second substances,
Figure BDA00036724197400000712
the efficiency correction factor of the electric refrigerator is obtained; k is a radical of formula EC,n Fitting coefficients of the n orders of the efficiency of the electric refrigerator; n is a radical of EC Is the load factor of the electric refrigerator.
(1.2) establishing an integrated model of the comprehensive energy system as follows:
Figure BDA0003672419740000081
wherein f is 1 ,f 2 ,…,f n Optimizing an objective function for operation of the integrated energy system; g () is a supply and demand balance expression of the comprehensive energy system; g () is a device constraint expression of the comprehensive energy system; i represents the ith type of energy in cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is heat, E is electricity and G is gas; x is the number of i A parameter representing the energy of class i; t is a time scale; xi is an uncertain variable; l is the load demand; p is an output energy value of the energy supply equipment or the energy conversion equipment or the distribution network, namely an output value; h () is a coupling conversion matrix; η is the energy conversion efficiency of the energy conversion device.
2) Constructing a comprehensive cost-energy consumption curve facing the multi-energy consumption requirement of the park; the method comprises the following steps:
(2.1) integrating an objective function of the optimized operation of the comprehensive energy system;
the objective function of the optimization operation of the integrated comprehensive energy system is as follows:
Figure BDA0003672419740000082
f is the comprehensive cost of the optimized operation of the comprehensive energy system after multi-objective integration by using a membership function; f. of 1 ,f 2 ,…,f n Optimizing an objective function for operation of the integrated energy system; u is the energy conversion device type; f u Represents the net cost of the energy conversion device; s i Representing the energy cost of the ith type of energy; l is a radical of an alcohol i Load demand for class i energy; f i The comprehensive cost of the ith type of energy; delta is a repeated calculation part caused by the energy conversion equipment simultaneously generating multiple energies; omega is an energy conversion equipment set; i represents the ith type of energy in the cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is heat, E is electricity and G is gas.
(2.2) constructing a net cost-output curve of the energy conversion equipment;
the net cost-output curve of the energy conversion equipment is a curve drawn according to net cost-output functions of the energy conversion equipment of a cogeneration unit, a gas boiler, an absorption refrigerator and an electric refrigerator; the net cost-out function of the energy conversion device is:
Figure BDA0003672419740000083
wherein, F u Represents the net cost of the energy conversion device;
Figure BDA0003672419740000084
for the output value of the energy conversion device u, the superscript ij represents that the energy conversion device u converts the ith type energy into the jth type energy; s i Representing the energy cost of the ith type of energy; s. the j Representing the energy cost of the j-th energy;
Figure BDA0003672419740000085
the energy conversion efficiency of the energy conversion device u; d u Loss of the energy conversion device u; i and j respectively represent the i and j energy in the cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is hot, E is electricity and G is gas.
(2.3) constructing a comprehensive cost-energy consumption curve facing the multi-element energy consumption requirement of the park;
the comprehensive cost-energy consumption curve for building the diversified energy consumption demand of the park is a curve drawn according to a comprehensive cost-energy consumption function; the overall cost-energy consumption function is:
Figure BDA0003672419740000086
wherein, F i The comprehensive cost of the i-th energy is obtained; f u Net cost for energy conversion equipment;
Figure BDA0003672419740000087
is the output value of the energy conversion device u; s i Energy cost for class i energy; i represents the ith type of energy in cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is heat, E is electricity and G is gas;
Figure BDA0003672419740000091
for the actual energy demand of class i energy in the campus, the numerical values satisfy the following constraints:
Figure BDA0003672419740000092
Figure BDA0003672419740000093
wherein L is i Load demand for class i energy;
Figure BDA0003672419740000094
the energy conversion efficiency of the energy conversion device u;
Figure BDA0003672419740000095
is the output value of the energy supply device v; v is a set of energy supply devices;
Figure BDA0003672419740000096
outputting an energy value upper limit for the distribution network with the ith type of energy;
Figure BDA0003672419740000097
the upper limit of the output value of the energy conversion device u;
Figure BDA0003672419740000098
is the upper limit of the output value of the energy supply device v.
And (2.4) carrying out regional division on a comprehensive cost-energy consumption curve of the diversified energy consumption requirements of the facing park. The method comprises the following steps of dividing an optimized area and a guarantee supply area, wherein the optimized area comprises: a self-energy supply area, an energy purchasing area and an energy conversion area I, wherein the energy supply area is an energy conversion area II, as shown in figure 1; wherein:
(2.4.1) self-energizing zone: the energy consumption of the park is generated by wind and light renewable energy sources in the park, and the unit energy consumption cost is lower than that of energy purchasing;
(2.4.2) energy purchase zone: the energy consumption of the park is met by purchasing energy through an external network;
(2.4.3) energy conversion region I: the energy consumption of the garden is met by energy conversion equipment, and the unit energy consumption cost is lower than that of energy purchasing;
(2.4.4) energy conversion zone II: the energy consumption of the park is met by energy conversion equipment, and the unit energy consumption cost is higher than the energy purchasing cost.
3) Calculating an optimized operation scheme of the comprehensive energy system based on the comprehensive cost-energy consumption curve; comprises that
(3.1) calculating an optimized operation scheme of the comprehensive energy system without the energy storage equipment; the method comprises the following steps:
(3.1.1) considering the time-of-use electricity price, respectively constructing 24 groups of comprehensive cost-energy consumption curves corresponding to 24 hours a day according to the comprehensive cost-energy consumption function in the step (2.3) in the step 2), wherein each group of comprehensive cost-energy consumption curves comprises 4 curves of a cold energy comprehensive cost-energy consumption curve, a heat energy comprehensive cost-energy consumption curve, an electric energy comprehensive cost-energy consumption curve and a gas energy comprehensive cost-energy consumption curve;
(3.1.2) according to the 24 groups of comprehensive cost-energy consumption curves, establishing 24 groups of energy distribution data tables containing output and purchased energy of park energy equipment, wherein each group of energy distribution data tables comprises 4 tables of cold energy distribution, heat energy distribution, electric energy distribution and gas energy distribution;
(3.1.3) according to the comprehensive cost-energy consumption curve of the cold energy and by combining a cold energy distribution data table, obtaining the output conditions of the electric refrigerator and the absorption refrigerator;
(3.1.4) superposing the electric energy demand generated by the electric refrigerator to the total electric energy consumption amount, and obtaining the electricity purchasing quantity, the wind power and photovoltaic power generation quantity and the cogeneration output condition of the park according to the electric energy comprehensive cost-energy consumption curve and in combination with an electric energy distribution data table;
(3.1.5) superposing the heat energy demand generated by the absorption refrigerator to the total heat energy consumption, and combining a heat energy distribution data table according to a heat energy comprehensive cost-energy consumption curve to obtain the heat purchasing quantity of the park, the cogeneration output condition and the gas boiler output condition;
(3.1.6) judging whether the cogeneration output in the step (3.1.4) and the step (3.1.5) is the same, if not, taking a value with large cogeneration output according to a net cost-output curve of cogeneration if the cogeneration output is in a profit region; if the gas boiler is in the loss area and the gas boiler is not fully loaded, taking a value with small cogeneration output under the premise of meeting the equipment constraint of the comprehensive energy system; then, setting the cogeneration output as a fixed value, obtaining the park electricity purchasing quantity, the wind power generation quantity and the photovoltaic power generation quantity again according to the electric energy comprehensive cost-energy consumption curve and the electric energy distribution data table, and obtaining the park heat purchasing quantity and the gas boiler output condition according to the heat energy comprehensive cost-energy consumption curve and the heat energy distribution data table;
(3.1.7) superposing the gas energy requirements generated by cogeneration and a gas boiler to the total gas energy consumption, and combining a gas energy distribution data table according to a gas energy comprehensive cost-energy consumption curve to obtain the gas purchasing quantity of the park;
and (3.1.8) calculating the comprehensive cost of the optimized operation of the comprehensive energy system by combining 24 groups of comprehensive cost-energy consumption curves to obtain the optimized operation scheme of the comprehensive energy system.
(3.2) calculating an optimized operation scheme of the comprehensive energy system comprising the energy storage equipment;
firstly, the energy storage using modes are divided into an energy storage using mode 1 and an energy storage using mode 2, and the meanings are as follows:
energy storage usage mode 1: storing the energy which can meet the energy consumption requirement in the period a and can be supplied by the optimized area to replace the period b;
energy storage use mode 2: and storing the low-cost external network energy purchasing energy after the c-period optimizable area meets the energy consumption requirement, and replacing the high-cost external network energy purchasing energy needed by the d-period optimizable area.
The calculation of the optimized operation scheme of the comprehensive energy system comprising the energy storage device specifically comprises the following steps:
(3.2.1) calculating the residual energy value of each energy optimizing area and the using energy value of the reserve supply area in 24 periods of cold, heat, electricity and gas according to the optimized operation scheme of the comprehensive energy system obtained in the step (3.1), wherein the calculation formula is as follows:
Figure BDA0003672419740000101
Figure BDA0003672419740000102
wherein the content of the first and second substances,
Figure BDA0003672419740000103
optimizing the zone residual energy value for the ith type energy t period;
Figure BDA0003672419740000104
the energy using value of the supply area is guaranteed for the ith type energy t period;
Figure BDA0003672419740000105
outputting an energy value upper limit for the distribution network with the ith type of energy;
Figure BDA0003672419740000106
is the upper limit of the output value of the energy conversion device w; w is an energy conversion equipment set of the energy conversion I area;
Figure BDA0003672419740000107
an upper limit of the output value for the energy supply device v; v is a set of energy supply devices;
Figure BDA0003672419740000108
the actual energy demand of the ith type of energy in the park; i represents the ith type of energy in cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is heat, E is electricity and G is gas;
(3.2.2) calculating an energy storage use scheme under the energy storage use mode 1, wherein the calculation formula of the energy storage use scheme is as follows:
Figure BDA0003672419740000109
wherein, y i Aiming at the optimization target of the ith type energy in the energy storage use mode 1 and replacing the energy provided by the reserve supply area as much as possibleWhile using as little energy storage capacity as possible; i represents the ith energy of cold, heat, electricity and gas of the comprehensive energy system; t is a scheduling period of 24 h;
Figure BDA00036724197400001010
the output energy value of the energy storage device t period of the ith type energy (if the absorbed energy is negative) is obtained;
Figure BDA00036724197400001011
an upper limit of energy storage/release power of the energy storage device for the ith type of energy in unit time;
Figure BDA00036724197400001012
judging the energy storage working mode for the ith type energy t time period, if so
Figure BDA00036724197400001013
Then
Figure BDA00036724197400001014
Otherwise, the reverse is carried out
Figure BDA00036724197400001015
M is a set constant;
Figure BDA00036724197400001016
storing an energy value for the energy storage device for the ith type energy t time period;
Figure BDA0003672419740000111
storing an energy value for the energy storage device in the ith type energy t-1 time period;
Figure BDA0003672419740000112
the self-discharging rate of the energy storage device for the ith type of energy;
Figure BDA0003672419740000113
and with
Figure BDA0003672419740000114
Stored energy value of energy storage device respectively being i-th energyUpper/lower limits;
(3.2.3) superposing the energy storage use scheme obtained in the step (3.2.2) to the total electric energy consumption, the total heat energy consumption, the total gas energy consumption and the total cold energy consumption in the step (3.1) in the step (3), and recalculating the optimized operation scheme of the comprehensive energy system;
(3.2.4) calculating the secondary residual energy value of each energy optimizing area and the secondary using energy value of the supply area in 24 periods of cold, heat, electricity and gas, wherein the calculation formula is as follows:
Figure BDA0003672419740000115
Figure BDA0003672419740000116
wherein, the first and the second end of the pipe are connected with each other,
Figure BDA0003672419740000117
the secondary residual energy value of the optimization area is the ith type energy t period;
Figure BDA0003672419740000118
ensuring the secondary use energy value of the supply area for the ith type energy t period;
(3.2.5) respectively judging whether the sum of the secondary use energy values of 24 time-keeping supply areas of cold, heat, electricity and gas is 0, if so, performing the step (3.2.6); if not, performing the step (3.2.7);
(3.2.6) calculating the energy storage usage scheme in the energy storage usage mode 2 according to the following formula:
Figure BDA0003672419740000119
wherein, Δ y i The optimization target of the ith type energy in the energy storage use mode 2 is to make use of time-of-use energy price to make profit under the condition of ensuring the energy supply of the guaranteed supply area;
Figure BDA00036724197400001110
outputting the correction quantity of the energy value for the ith type energy storage device in the t period (increasing the released energy to be positive, and increasing the absorbed energy to be negative);
Figure BDA00036724197400001111
outputting an energy value for the distribution network in the ith type energy t period;
Figure BDA00036724197400001112
the energy consumption unit cost of the energy storage device for the ith type of energy;
Figure BDA00036724197400001113
energy cost of ith type of energy in t period;
(3.2.7) the energy storage use scheme in the energy storage use mode 1, the energy storage use scheme in the energy storage use mode 2 and the recalculated comprehensive energy system optimized operation scheme jointly form a comprehensive energy system optimized operation scheme comprising energy storage equipment; at the moment, the comprehensive energy cost calculation formula of the comprehensive energy system is as follows:
Figure BDA00036724197400001114
wherein F is the comprehensive cost of the optimized operation of the comprehensive energy system; f i The comprehensive cost of the i-th energy is obtained; Δ is the iterative part of the calculation resulting from the simultaneous generation of multiple energies by the energy conversion device.
Examples are given below:
for example, a structure diagram of a small town with a peace of mind is shown in FIG. 2.4 scenes are designed for simulation and comparative analysis. The scene details are as follows:
scene 1: the variable working condition operation characteristics of the multi-type energy equipment are not considered, and a solver is used for solving a CIES optimization operation scheme;
scene 2: the variable working condition operation characteristics of the multi-type energy equipment are considered, the multi-type energy equipment is subjected to piecewise linearization (divided into 3 sections), and a solver is further utilized to solve the collaborative optimization operation scheme of the park comprehensive energy system;
scene 3: the variable working condition operation characteristics of the multi-type energy equipment are considered, the multi-type energy equipment is subjected to piecewise linearization (divided into 15 sections), and a solver is further utilized to solve the collaborative optimization operation scheme of the park comprehensive energy system;
scene 4: and (4) considering the variable working condition operation characteristics of the multi-type energy equipment, and solving the collaborative optimization operation scheme of the park comprehensive energy system by using the method provided by the invention.
Table 1 shows the comparison of simulation results in different scenarios of the campus integrated energy system without energy storage devices; table 2 shows the comparison of simulation results in different scenarios for the campus integrated energy system including the energy storage device. The total energy deviation in the table refers to the sum of the all-day energy differences between the optimized operating schedule and the actual load demand.
TABLE 1
Figure BDA0003672419740000121
TABLE 2
Figure BDA0003672419740000122
According to the data in table 1 and table 2, the effect of the proposed method can be clearly shown:
comparing scenes 1-3, it can be seen that the total amount of energy deviation can be remarkably reduced by considering the variable working condition operation characteristics of the multi-type energy conversion equipment, and the accuracy of the collaborative optimization operation scheme of the park comprehensive energy system is improved. The more accurate the variable operating characteristic characterization is, the higher the accuracy of the optimized operating scheme is, but at the same time, the optimization calculation time is increased. The deviation sum of various energies is different, the energy deviation of electric energy and heat energy is caused by the variable working condition operation of refrigeration equipment (an electric refrigerator and an absorption refrigerator), and the gas energy deviation is caused by the variable working condition operation of power generation and heating equipment (CHP and a gas boiler). The daily operation cost of the park comprehensive energy system is reduced after the variable working condition operation characteristics of the equipment are considered, mainly because the energy conversion efficiency of part of energy conversion equipment is higher under the non-rated working condition, such as the refrigeration efficiency of an electric refrigerator.
Comparing table 1 with table 2, it can be seen that the energy storage device can effectively reduce the operating cost of the system. But the cost reduction is not significant due to the smaller energy storage capacity in this example. After the energy storage equipment is considered, the optimization calculation time is obviously increased mainly because the energy storage equipment cannot be optimized through a single time section during operation, and all the time sections need to be planned overall, so that the number of the optimized variables is increased by 1 order of magnitude, and the more the optimized variables are, the slower the solving speed is. The energy deviation sum of the gas energy in the table 2 is smaller than that in the table 1, because the electricity energy storage and heat energy storage devices are used, the electricity generation and the heat generation of the CHP and the gas boiler are reduced, and further, the influence of the variable working condition operation characteristics of the two devices on the total energy consumption is reduced.
(3) Comparing the scene 4 with other scenes, it can be seen that the method provided by the invention can effectively overcome the contradiction between the calculation accuracy and the calculation efficiency of the collaborative optimization operation scheme of the park comprehensive energy system, and ensure shorter optimization calculation time while remarkably reducing the total amount of energy deviation. The method provided by the invention mainly considers the variable working condition operating characteristics of the equipment, and the calculation process only adopts logic judgment and data table query (small-scale linear programming is added when the energy storage equipment is considered). The method of the invention results in slightly higher cost (the daily operation cost is about 0.006 percent), because the heat energy required by refrigeration in actual conditions can be provided by a gas boiler on the basis of the energy purchase price of electric energy and heat energy during cold energy distribution, so that the optimal operation scheme is not globally optimal. In general occasions, the daily operation cost of the scheme is closer to the actual optimal scheme, so that the scheme can be directly used; on occasions with special requirements, the operation scheme can provide an optimized operation reference value with high reliability for other optimized operation strategies, so that the optimization accuracy of the other optimized operation strategies is improved, and the optimization time is shortened.

Claims (10)

1. An integrated energy system optimization operation method based on an integrated cost-energy consumption curve is characterized by comprising the following steps:
1) establishing a park comprehensive energy system integrated model considering variable working condition characteristics of energy conversion equipment; comprises that
(1.1) establishing a variable working condition operation model of energy conversion equipment of a combined heat and power generation unit, a gas boiler, an absorption refrigerator and an electric refrigerator, wherein the variable working condition operation model of the energy conversion equipment is as follows:
Figure FDA0003672419730000011
wherein, P out For outputting energy, P, to energy-converting apparatus in Energy is input to the energy conversion device, eta is the energy conversion efficiency of the energy conversion device, eta R For the energy conversion efficiency of the energy conversion device under rated operating conditions,
Figure FDA0003672419730000012
the efficiency correction coefficient is the efficiency correction coefficient of a cogeneration unit or a gas boiler or an absorption refrigerator or an electric refrigerator;
(1.2) establishing an integrated model of the comprehensive energy system;
2) constructing a comprehensive cost-energy consumption curve facing the multi-energy consumption requirement of the park; the method comprises the following steps:
(2.1) integrating an objective function of the optimized operation of the comprehensive energy system;
(2.2) constructing a net cost-output curve of the energy conversion equipment;
(2.3) constructing a comprehensive cost-energy consumption curve facing the multi-energy consumption requirement of the park;
(2.4) carrying out regional division on a comprehensive cost-energy consumption curve of the multi-energy consumption requirement of the facing park;
3) calculating an optimized operation scheme of the comprehensive energy system based on the comprehensive cost-energy consumption curve; comprises that
(3.1) calculating an optimized operation scheme of the comprehensive energy system without the energy storage equipment;
and (3.2) calculating an optimized operation scheme of the integrated energy system comprising the energy storage equipment.
2. The comprehensive energy system optimal operation method based on the comprehensive cost-energy consumption curve according to claim 1, wherein the efficiency correction coefficients of the cogeneration unit, the gas boiler, the absorption chiller and the electric chiller in the step 1) and the step (1.1) are respectively as follows:
efficiency correction coefficient of cogeneration unit:
Figure FDA0003672419730000013
Figure FDA0003672419730000014
wherein the content of the first and second substances,
Figure FDA0003672419730000015
the efficiency correction coefficient of the cogeneration unit; k is a radical of CHP,n An n-order fitting coefficient of the electric efficiency of the cogeneration unit; n is a radical of CHP The electric load rate of the cogeneration unit;
Figure FDA0003672419730000016
the correction coefficient is the heat-electricity ratio of the cogeneration unit; k is a radical of α,n Fitting coefficients of an nth order of a thermoelectric ratio of the cogeneration unit;
efficiency correction factor of gas boiler:
Figure FDA0003672419730000017
wherein the content of the first and second substances,
Figure FDA0003672419730000018
the efficiency correction coefficient of the gas boiler; k is a radical of GB,n An n-order fitting coefficient of the gas boiler efficiency; n is a radical of GB Is the load factor of the gas boiler;
efficiency correction coefficient of absorption chiller:
Figure FDA0003672419730000021
wherein the content of the first and second substances,
Figure FDA0003672419730000022
correcting the coefficient for the efficiency of the absorption chiller; k is a radical of AC,n Is an n-order fitting coefficient of the efficiency of the absorption refrigerator; n is a radical of AC Is the load factor of the absorption chiller;
efficiency correction coefficient of electric refrigerator:
Figure FDA0003672419730000023
wherein the content of the first and second substances,
Figure FDA0003672419730000024
the efficiency correction factor of the electric refrigerator is obtained; k is a radical of EC,n Fitting coefficients of the electric refrigerator efficiency in the order of n; n is a radical of EC Is the load factor of the electric refrigerator.
3. The method for optimizing the operation of the integrated energy system based on the integrated cost-energy consumption curve according to claim 1, wherein the integrated model of the integrated energy system in the step 1) and the step (1.2) is as follows:
Figure FDA0003672419730000025
wherein f is 1 ,f 2 ,…,f n An objective function for optimizing operation of the integrated energy system; g () is a supply and demand balance expression of the comprehensive energy system; g () is a device constraint expression of the comprehensive energy system; i represents the ith energy in the cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is hot, E is electricity and G is gas; x is the number of i A parameter representing the energy of class i; t is a time scale; xi is uncertainDetermining variables; l is the load demand; p is an output energy value of the energy supply equipment or the energy conversion equipment or the distribution network, namely an output value; h () is a coupling conversion matrix; η is the energy conversion efficiency of the energy conversion device.
4. The method for optimizing the operation of the integrated energy system based on the integrated cost-energy consumption curve according to claim 1, wherein the objective function of the optimizing operation of the integrated energy system in the step 2) at the step (2.1) is:
Figure FDA0003672419730000026
f is the comprehensive cost of the optimized operation of the comprehensive energy system after multi-objective integration by using a membership function; f. of 1 ,f 2 ,…,f n An objective function for optimizing operation of the integrated energy system; u is the energy conversion device type; f u Represents the net cost of the energy conversion device; s i Representing the energy cost of the ith type of energy; l is i Load demand for class i energy; f i The comprehensive cost of the i-th energy is obtained; delta is a repeated calculation part caused by the energy conversion equipment simultaneously generating multiple energies; omega is an energy conversion equipment set; i represents the ith type of energy in the comprehensive energy system of cold, heat, electricity and gas, C is cold, H is heat, E is electricity and G is gas.
5. The method according to claim 1, wherein the net cost-output curve of the energy conversion device in step 2) (2.2) is a curve plotted according to a net cost-output function of the energy conversion device for the cogeneration unit, the gas boiler, the absorption chiller, and the electric chiller; the net cost-out function of the energy conversion device is:
Figure FDA0003672419730000031
wherein, F u Represents the net cost of the energy conversion device;
Figure FDA0003672419730000032
for the output value of the energy conversion device u, the superscript ij represents that the energy conversion device u converts the ith type energy into the jth type energy; s i Representing the energy cost of the ith type of energy; s j Representing the energy cost of the j-th energy;
Figure FDA0003672419730000033
the energy conversion efficiency of the energy conversion device u; d u Loss of the energy conversion device u; i and j respectively represent the i and j energy in the cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is hot, E is electricity and G is gas.
6. The integrated energy system optimized operation method based on integrated cost-energy consumption curve according to claim 1, characterized in that the integrated cost-energy consumption curve for building the diversified energy consumption requirements of the park in the step 2) (2.3) is a curve drawn according to the integrated cost-energy consumption function; the overall cost-energy consumption function is:
Figure FDA0003672419730000034
wherein, F i The comprehensive cost of the i-th energy is obtained; f u Net cost for energy conversion equipment;
Figure FDA0003672419730000035
is the output value of the energy conversion device u; s i Energy cost for class i energy; i represents the ith type of energy in cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is heat, E is electricity and G is gas;
Figure FDA0003672419730000036
for class i energy in the parkThe practical energy demand and the numerical value satisfy the following constraints:
Figure FDA0003672419730000037
Figure FDA0003672419730000038
wherein L is i Load demand for class i energy;
Figure FDA0003672419730000039
the energy conversion efficiency of the energy conversion device u;
Figure FDA00036724197300000310
is the output value of the energy supply device v; v is a set of energy supply devices;
Figure FDA00036724197300000311
outputting an energy value upper limit for the distribution network with the ith type of energy;
Figure FDA00036724197300000312
is the upper limit of the output value of the energy conversion device u;
Figure FDA00036724197300000313
is the upper limit of the output value of the energy supply device v.
7. The integrated energy system optimized operation method based on integrated cost-energy consumption curve according to claim 1, characterized in that the integrated cost-energy consumption curve of the multi-energy consumption demand of the facing park in the step 2) in the step (2.4) is divided into regions, including an optimizable region and a reserve region, wherein the optimizable region comprises: the energy supply system comprises a self-energy supply area, an energy purchasing area and an energy conversion area I, wherein a supply area is an energy conversion area II; wherein:
(2.4.1) self-energizing zone: the energy consumption of the park is generated by wind and light renewable energy sources in the park, and the unit energy consumption cost is lower than that of energy purchasing;
(2.4.2) energy purchase zone: energy consumption of the park is met by purchasing energy through an external network;
(2.4.3) energy conversion region I: the energy consumption of the garden is met by energy conversion equipment, and the unit energy consumption cost is lower than that of energy purchasing;
(2.4.4) energy conversion zone II: the energy consumption of the park is met by energy conversion equipment, and the unit energy consumption cost is higher than the energy purchasing cost.
8. The method for optimized operation of an integrated energy system based on integrated cost-energy consumption curve of claim 1, wherein the step 3) of calculating the optimized operation scheme of the integrated energy system without energy storage device in step (3.1) comprises:
(3.1.1) considering the time-of-use electricity price, respectively constructing 24 groups of comprehensive cost-energy consumption curves corresponding to 24 hours a day according to the comprehensive cost-energy consumption function in the step (2.3) in the step 2), wherein each group of comprehensive cost-energy consumption curves comprises 4 curves of a cold energy comprehensive cost-energy consumption curve, a heat energy comprehensive cost-energy consumption curve, an electric energy comprehensive cost-energy consumption curve and a gas energy comprehensive cost-energy consumption curve;
(3.1.2) according to the 24 groups of comprehensive cost-energy consumption curves, establishing 24 groups of energy distribution data tables containing output and purchased energy of park energy equipment, wherein each group of energy distribution data tables comprises 4 tables of cold energy distribution, heat energy distribution, electric energy distribution and gas energy distribution;
(3.1.3) obtaining the output conditions of the electric refrigerator and the absorption refrigerator according to the comprehensive cold energy cost-energy consumption curve and in combination with a cold energy distribution data table;
(3.1.4) superposing the electric energy demand generated by the electric refrigerator to the total electric energy consumption amount, and obtaining the electricity purchasing quantity, the wind power and photovoltaic power generation quantity and the cogeneration output condition of the park according to the electric energy comprehensive cost-energy consumption curve and in combination with an electric energy distribution data table;
(3.1.5) superposing the heat energy demand generated by the absorption refrigerator to the total heat energy consumption, and obtaining the district heat purchase amount, the cogeneration output condition and the gas boiler output condition according to the heat energy comprehensive cost-energy consumption curve and by combining a heat energy distribution data table;
(3.1.6) judging whether the cogeneration output in the step (3.1.4) and the step (3.1.5) is the same, if not, taking a large value of the cogeneration output according to a net cost-output curve of the cogeneration if the cogeneration output is in a profit region; if the gas boiler is in the loss area and the gas boiler is not fully loaded, taking a value with small cogeneration output under the premise of meeting the equipment constraint of the comprehensive energy system; then, setting the cogeneration output as a fixed value, obtaining the park electricity purchasing quantity, the wind power generation quantity and the photovoltaic power generation quantity according to the electric energy comprehensive cost-energy consumption curve and the electric energy distribution data table again, and obtaining the park heat purchasing quantity and the gas boiler output condition according to the heat energy comprehensive cost-energy consumption curve and the heat energy distribution data table;
(3.1.7) superposing the gas energy requirements generated by cogeneration and a gas boiler to the total gas energy consumption, and combining a gas energy distribution data table according to a gas energy comprehensive cost-energy consumption curve to obtain the gas purchasing quantity of the park;
and (3.1.8) calculating the comprehensive cost of the optimized operation of the comprehensive energy system by combining 24 groups of comprehensive cost-energy consumption curves to obtain the optimized operation scheme of the comprehensive energy system.
9. The comprehensive energy system optimized operation method based on the comprehensive cost-energy consumption curve as claimed in claim 1, wherein the step 3) and the step (3.2) firstly divide the energy storage usage modes into two types, namely an energy storage usage mode 1 and an energy storage usage mode 2, and the meanings are as follows:
energy storage usage pattern 1: storing the energy which can meet the energy consumption requirement in the period a and can be supplied by the optimized area to replace the period b;
energy storage use mode 2: and after the c-period optimized area is stored, the low-cost external network energy purchasing energy required by the energy consumption requirement is met, and the high-cost external network energy purchasing energy required by the d-period optimized area is replaced.
10. The integrated energy system optimal operation method based on the integrated cost-energy consumption curve according to claim 9, wherein the step 3) of calculating the integrated energy system optimal operation scheme comprising the energy storage device in the step (3.2) comprises:
(3.2.1) calculating the residual energy value of each energy optimizing area and the using energy value of the reserve supply area in 24 periods of cold, heat, electricity and gas according to the optimized operation scheme of the comprehensive energy system obtained in the step (3.1), wherein the calculation formula is as follows:
Figure FDA0003672419730000041
Figure FDA0003672419730000042
wherein, the first and the second end of the pipe are connected with each other,
Figure FDA0003672419730000051
optimizing the zone residual energy value for the ith type energy t period;
Figure FDA0003672419730000052
the energy using value of the supply area is guaranteed for the ith type energy t period;
Figure FDA0003672419730000053
outputting an energy value upper limit for the distribution network with the ith type of energy;
Figure FDA0003672419730000054
is the upper limit of the output value of the energy conversion device w; w is an energy conversion equipment set of an energy conversion I area;
Figure FDA0003672419730000055
an upper limit of the output value for the energy supply device v; v is a set of energy supply devices;
Figure FDA0003672419730000056
for the actual energy demand of class i energy in the park(ii) a i represents the ith type of energy in cold, heat, electricity and gas of the comprehensive energy system, C is cold, H is heat, E is electricity and G is gas;
(3.2.2) calculating an energy storage use scheme under the energy storage use mode 1, wherein the calculation formula of the energy storage use scheme is as follows:
Figure FDA0003672419730000057
wherein, y i For the optimization target of the ith type of energy in the energy storage use mode 1, i represents the energy generated by various types of energy such as cold, heat, electricity and gas of the comprehensive energy system; t is a scheduling period of 24 h;
Figure FDA0003672419730000058
the output energy value of the energy storage device t time period of the ith type of energy;
Figure FDA0003672419730000059
the upper limit of the energy storage/release power of the energy storage device for the ith type of energy in unit time;
Figure FDA00036724197300000510
judging the energy storage working mode for the ith type energy t time period, if so
Figure FDA00036724197300000511
Then
Figure FDA00036724197300000512
Otherwise, the reverse is carried out
Figure FDA00036724197300000513
M is a set constant;
Figure FDA00036724197300000514
storing an energy value for the energy storage device for the ith type energy t time period;
Figure FDA00036724197300000515
storing an energy value for the energy storage device in the ith type energy t-1 time period;
Figure FDA00036724197300000516
the self-discharging rate of the energy storage device for the ith type of energy;
Figure FDA00036724197300000517
and
Figure FDA00036724197300000518
the upper limit and the lower limit of the stored energy value of the energy storage device for the ith type of energy are respectively set;
(3.2.3) superposing the energy storage use scheme obtained in the step (3.2.2) to the total electric energy consumption amount, the total heat energy consumption amount, the total gas energy consumption amount and the total cold energy consumption amount in the step (3.1) in the step (3), and recalculating the optimized operation scheme of the comprehensive energy system;
(3.2.4) calculating the secondary residual energy value of each energy optimizing area and the secondary using energy value of the supply area in 24 periods of cold, heat, electricity and gas, wherein the calculation formula is as follows:
Figure FDA00036724197300000519
Figure FDA00036724197300000520
wherein the content of the first and second substances,
Figure FDA00036724197300000521
the secondary residual energy value of the optimization area is the ith type energy t period;
Figure FDA00036724197300000522
ensuring the secondary use energy value of the supply area for the ith type energy t period;
(3.2.5) respectively judging whether the sum of the secondary use energy values of 24 time-keeping supply areas of cold, heat, electricity and gas is 0, if so, performing the step (3.2.6); if not, performing the step (3.2.7);
(3.2.6) calculating the energy storage usage scheme in the energy storage usage mode 2 according to the following formula:
Figure FDA0003672419730000061
wherein, Δ y i An optimization target of the ith type of energy in the energy storage use mode 2 is obtained;
Figure FDA0003672419730000062
the correction quantity of the energy value is output for the ith type energy storage device in the t period;
Figure FDA0003672419730000063
outputting an energy value for the distribution network in the ith type energy t period;
Figure FDA0003672419730000064
the energy consumption unit cost of the energy storage device for the ith type of energy;
Figure FDA0003672419730000065
energy cost of ith type of energy in t period;
(3.2.7) the energy storage use scheme in the energy storage use mode 1, the energy storage use scheme in the energy storage use mode 2 and the recalculated comprehensive energy system optimized operation scheme jointly form an optimized operation scheme of the comprehensive energy system comprising the energy storage equipment; at the moment, the comprehensive energy cost calculation formula of the comprehensive energy system is as follows:
Figure FDA0003672419730000066
wherein F is the comprehensive cost of the optimized operation of the comprehensive energy system; f i The comprehensive cost of the i-th energy is obtained; delta is energy conversion equipmentA plurality of energy-induced iterative computation portions are generated.
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