Electricity-hydrogen coordinated system planning method and device considering ancillary service market benefits

Abstract

The present application provides a method and device for planning an electric-hydrogen synergistic system that considers the revenue of the ancillary service market. The method of the present application includes: obtaining the basic parameters of the ancillary service market; constructing an optimization planning model for the electric-hydrogen synergistic system that considers the revenue of the ancillary service market; constructing the objective function and constraints of the optimization planning model for the electric-hydrogen synergistic system that considers the revenue of the ancillary service market with the goal of maximizing the annualized net revenue during the planning period; solving the objective function of the optimization planning model for the electric-hydrogen synergistic system that considers the revenue of the ancillary service market according to the constraints, and obtaining the capacity configuration of each element in the electric-hydrogen synergistic system; planning the electric-hydrogen synergistic system according to the capacity configuration of each element in the electric-hydrogen synergistic system. The technical solution provided by the present application can tap the flexible adjustment potential of hydrogen production from electricity, as a flexible resource for the power system, and help the consumption of new energy. At the same time, it can obtain revenue in the ancillary service market and promote the development of green hydrogen.

Description

Technical Field

[0001] This document relates to the technical field of electric-hydrogen synergistic system planning, and in particular to a method and device for planning an electric-hydrogen synergistic system taking into account the benefits of the ancillary service market. Background Art

[0002] At present, hydrogen energy, especially green hydrogen industry, is developing rapidly. Green hydrogen is hydrogen produced by green electricity. Therefore, the coupling relationship between hydrogen and electricity will become closer. In particular, in the process of preparing green hydrogen, the electric hydrogen production device allows the use of flexible and fluctuating operation mode to track the fluctuation of new energy, and can participate in the peak load regulation, standby and other auxiliary services of the power system. By converting the flexible adjustment value into economic value in the auxiliary service market, it can be used as the income of the electric-hydrogen synergistic system. At present, the coordinated development of electric and hydrogen is mostly at the conceptual level. The invention patent CN116579115B discloses a system planning method and device for the coordinated interaction of electricity and hydrogen to solve the problem of the lack of electric-hydrogen coordinated planning method.

[0003] However, current methods for planning electric-hydrogen synergy are mostly considered from the perspective of the overall cost of the electric-hydrogen system, that is, the optimization model for planning is to pursue the lowest overall system cost of electricity and hydrogen coupling synergy, and fails to consider the participation of electric-hydrogen synergy elements in auxiliary services such as peak regulation and standby of the power system. The former pursues the overall optimality of the electric-hydrogen coupling system and is more idealistic, which is suitable for national or regional macro-level planning; but the latter is more in line with the specific operating logic of actually stimulating electric-hydrogen synergy, and is closer to the actual strategic selection of the electric-hydrogen synergy system, and is suitable for carrying out capacity planning and configuration of various elements at the specific system project level.

[0004] Therefore, this application proposes a method and device for planning an electric-hydrogen synergistic system that takes into account the benefits of the ancillary service market, so as to solve the problem of the lack of a current electric-hydrogen synergistic system planning method that takes into account the benefits of participating in the ancillary service market and is oriented towards stimulating the flexible adjustment value of the electric-hydrogen synergistic system. Summary of the invention

[0005] The present invention provides a method and device for planning an electric-hydrogen collaborative system taking into account the revenue of the ancillary service market, aiming to solve the above-mentioned problems.

[0006] An embodiment of the present invention provides a method for planning an electric-hydrogen coordinated system taking into account the revenue of ancillary service market, including:

[0007] S1. Obtain basic parameters of the ancillary services market;

[0008] S2. Constructing an optimization planning model for the electric-hydrogen synergistic system taking into account the revenue of the ancillary service market according to the basic parameters of the ancillary service market;

[0009] S3. Construct the objective function of the optimization planning model of the electric-hydrogen synergistic system considering the ancillary service market revenue with the goal of maximizing the annualized net revenue during the planning period;

[0010] S4. Construct the constraints of the optimization planning model of the electric-hydrogen synergistic system considering the ancillary service market benefits;

[0011] S5. Solve the objective function of the optimization planning model of the electric-hydrogen synergistic system considering the ancillary service market revenue according to the constraint conditions to obtain the capacity configuration of each element in the electric-hydrogen synergistic system;

[0012] S6. Plan the electric-hydrogen synergistic system according to the capacity configuration of each element in the electric-hydrogen synergistic system.

[0013] An electronic device according to an embodiment of the present invention includes:

[0014] processor; and,

[0015] A memory arranged to store computer executable instructions, which, when executed, cause the processor to perform the steps of the above-mentioned method for planning an electric-hydrogen coordinated system considering the revenue of the ancillary service market.

[0016] An embodiment of the present invention provides a storage medium for storing computer-executable instructions, which, when executed, implement the steps of the above-mentioned method for planning an electric-hydrogen collaborative system taking into account the benefits of the ancillary service market.

[0017] By adopting the embodiment of the present invention, the electricity-hydrogen synergy planning is considered from the perspective of the participation of the electricity-hydrogen synergy elements in auxiliary services such as peak-shaving and standby of the power system. By obtaining revenue in the auxiliary service market, the flexible adjustment value of the electricity-hydrogen synergy system can be converted into economic value, thereby promoting the development of green hydrogen. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] In order to more clearly illustrate one or more embodiments of this specification or the technical solutions in the prior art, the drawings required for use in the embodiments or the description of the prior art will be briefly introduced below. Obviously, the drawings described below are only some embodiments recorded in this specification. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying creative labor.

[0019] Figure 1 This is a flow chart of a method for planning an electric-hydrogen cooperative system taking into account ancillary service market revenue according to an embodiment of the present invention. DETAILED DESCRIPTION

[0020] In order to enable those skilled in the art to better understand the technical solutions in one or more embodiments of this specification, the technical solutions in one or more embodiments of this specification will be clearly and completely described below in conjunction with the drawings in one or more embodiments of this specification. Obviously, the described embodiments are only part of the embodiments of this specification, not all of them. Based on one or more embodiments of this specification, all other embodiments obtained by ordinary technicians in this field without creative work should fall within the scope of protection of this document.

[0021] Method Embodiment

[0022] According to an embodiment of the present invention, a method for planning an electric-hydrogen coordinated system taking into account the revenue of ancillary service market is provided. Figure 1 This is a flow chart of a method for planning an electric-hydrogen coordinated system considering the ancillary service market revenue according to an embodiment of the present invention. Figure 1 As shown, the electric-hydrogen coordinated system planning method considering the ancillary service market revenue of the embodiment of the present invention specifically includes:

[0023] S1. Obtain the basic parameters of the ancillary services market; S1 specifically includes:

[0024] Get the parameters related to the upward peak load (valley filling) of the ancillary service market:

[0025] Refer to the operation of the auxiliary service market in the previous year to obtain the annual expected number of times the electric-hydrogen collaborative system participates in upward peak regulation (valley filling) N ur , the average revenue per unit capacity of the electric-hydrogen synergy system participating in upward peak regulation (valley filling) R ur , the potential coefficient of the electrolyzer participating in upward peak regulation (valley filling) , the potential coefficient of hydrogen-fired units participating in upward peak regulation (valley filling) .

[0026] Get the parameters related to downward peak regulation (peak shaving) in the ancillary service market:

[0027] Refer to the operation of the ancillary service market in the previous year to obtain the annual expected number of times the electric-hydrogen collaborative system will participate in downward peak regulation (peak shaving) N dr , the average revenue per unit capacity of the electric-hydrogen synergy system participating in downward peak regulation (peak shaving) R dr , the potential coefficient of the electrolyzer participating in downward peak regulation (peak shaving) , the potential coefficient of hydrogen-fired units participating in downward peak regulation (peak shaving) .

[0028] Get frequency modulation related parameters of the ancillary service market:

[0029] Refer to the operation of the ancillary service market in the previous year to obtain the annual expected number of times the electric-hydrogen collaborative system will participate in frequency regulation N fr , the average revenue per unit capacity of the electric-hydrogen synergistic system participating in frequency regulation R fr , the potential coefficient of the electrolyzer participating in frequency regulation , the potential coefficient of hydrogen-fired units participating in frequency regulation .

[0030] Get the backup related parameters of the ancillary service market:

[0031] Refer to the operation of the auxiliary service market in the previous year to obtain the annual expected number of times the electric-hydrogen collaborative system will participate in the reserve N sr , the average revenue per unit capacity of the electric-hydrogen synergy system participating in the reserve R sr , the potential coefficient of electrolytic cell participation in standby , potential coefficient of hydrogen-fired units participating in standby .

[0032] S2. Constructing an optimization planning model for the electric-hydrogen synergistic system taking into account the benefits of the ancillary service market based on the basic parameters of the ancillary service market; S2 specifically includes:

[0033] 1) Constructing a revenue model for the electric-hydrogen synergy system to participate in upward peak load regulation (valley filling):

[0034] ;

[0035] in, E ur The benefits of the electric-hydrogen synergy system participating in upward peak load regulation (valley filling) are N ur is the expected annual number of times the electric-hydrogen coordinated system participates in upward peak regulation (valley filling), R ur The average revenue per unit capacity of the electric-hydrogen synergistic system participating in upward peak load regulation (valley filling) is is the potential coefficient of the electrolyzer participating in upward peak regulation (valley filling), C ec For the planned construction capacity of the electrolyzer, is the potential coefficient of hydrogen-fired units participating in upward peak regulation (valley filling), C ht The planned construction capacity for hydrogen-fired units.

[0036] 2) Constructing a revenue model for the electric-hydrogen synergy system to participate in downward peak regulation (peak shaving):

[0037] ;

[0038] in, E dr The benefits of the electric-hydrogen synergy system participating in downward peak load regulation (peak shaving) are N dr is the expected number of times the electric-hydrogen coordinated system participates in downward peak regulation (peak shaving) in a year, R dr The average revenue per unit capacity of the electric-hydrogen synergistic system participating in downward peak load regulation (peak shaving) is: is the potential coefficient of the electrolyzer participating in downward peak regulation (peak shaving), C ec For the planned construction capacity of the electrolyzer, is the potential coefficient of hydrogen-fired units participating in downward peak regulation (peak shaving), C ht The planned construction capacity for hydrogen-fired units.

[0039] 3) Constructing a revenue model for the electric-hydrogen synergy system to participate in frequency regulation:

[0040] ;

[0041] in, E fr The benefits of the electric-hydrogen synergy system participating in frequency regulation, N fr is the expected annual number of times the electric-hydrogen cooperative system participates in frequency regulation, R fr is the average revenue per unit capacity of the electric-hydrogen synergistic system participating in frequency regulation, is the potential coefficient of the electrolytic cell participating in frequency regulation, C ec For the planned construction capacity of the electrolyzer, is the potential coefficient of hydrogen-fired units participating in frequency regulation, C ht The planned construction capacity for hydrogen-fired units.

[0042] 4) Constructing a revenue model for the electric-hydrogen synergy system to participate in reserve:

[0043] ;

[0044] in, E sr The benefits of participating in the reserve of the electric-hydrogen coordinated system, N sr is the expected annual number of times the electric-hydrogen coordinated system participates in the reserve function. R sr is the average revenue per unit capacity of the electric-hydrogen synergistic system participating in the reserve, is the potential coefficient of the electrolytic cell participating in the standby, Cec For the planned construction capacity of the electrolyzer, is the potential coefficient of hydrogen-fired units participating in standby, C ht The planned construction capacity for hydrogen-fired units.

[0045] 5) Construct an optimization planning model for the electric-hydrogen synergistic system considering the benefits of the ancillary service market:

[0046] ;

[0047] S3. To maximize the annualized net income during the planning period, the objective function of the optimization planning model of the electric-hydrogen synergistic system considering the ancillary service market income is constructed; S3 specifically includes:

[0048] The goal is to maximize the annualized net income during the planning period, as shown below:

[0049] ;

[0050] in, N ur is the expected annual number of times the electric-hydrogen coordinated system participates in upward peak regulation (valley filling), R ur The average revenue per unit capacity of the electric-hydrogen synergistic system participating in upward peak load regulation (valley filling) is is the potential coefficient of the electrolyzer participating in upward peak regulation (valley filling), C ec For the planned construction capacity of the electrolyzer, is the potential coefficient of hydrogen-fired units participating in upward peak regulation (valley filling), C ht For the planned construction capacity of hydrogen-fired units, N dr is the expected number of times the electric-hydrogen coordinated system participates in downward peak regulation (peak shaving) in a year, R dr The average revenue per unit capacity of the electric-hydrogen synergistic system participating in downward peak load regulation (peak shaving) is: is the potential coefficient of the electrolyzer participating in downward peak regulation (peak shaving), is the potential coefficient of hydrogen-fired units participating in downward peak regulation (peak shaving), E fr The benefits of the electric-hydrogen synergy system participating in frequency regulation, N fr is the expected annual number of times the electric-hydrogen cooperative system participates in frequency regulation, R fr is the average revenue per unit capacity of the electric-hydrogen synergistic system participating in frequency regulation, is the potential coefficient of the electrolytic cell participating in frequency regulation, is the potential coefficient of hydrogen-fired units participating in frequency regulation,E sr The benefits of participating in the reserve of the electric-hydrogen coordinated system, N sr is the expected annual number of times the electric-hydrogen coordinated system participates in the reserve function. R sr is the average revenue per unit capacity of the electric-hydrogen synergistic system participating in the reserve, is the potential coefficient of the electrolytic cell participating in the standby, is the potential coefficient of hydrogen-fired units participating in standby, Q h is the expected annual hydrogen production of the electricity-hydrogen synergy system, R h is the unit hydrogen price, Q o is the expected annual oxygen production of the electric-hydrogen synergy system, R o is the unit oxygen price, Q e is the expected annual power consumption of the electric-hydrogen synergy system, R e is the average unit electricity price, Q w is the expected annual water consumption of the electricity-hydrogen synergy system, R w is the average unit water price, M Other annual operation and maintenance costs of the electric-hydrogen synergy system, b ec , b ht , b hs , b wp , b sp , b es They are the unit capacity construction costs of electrolyzer, hydrogen-fired unit, hydrogen storage tank, wind turbine, photovoltaic generator, and electric energy storage. C ec , C ht , C hs , C wp , C sp , C es They are the planned construction capacity of electrolyzers, hydrogen-fired units, hydrogen storage tanks, wind turbines, photovoltaic generators, and electric energy storage. T ec , T ht , T hs ,T wp , T sp , T es They are the life span of electrolyzer, hydrogen-fired unit, hydrogen storage tank, wind turbine, photovoltaic generator and electric energy storage.

[0051] S4. Constraints for constructing an optimization planning model for the electric-hydrogen synergistic system considering the benefits of the ancillary service market; S4 specifically includes:

[0052] 1) Power balance constraints to ensure the balance of power supply and demand in the electric-hydrogen coordinated system at all times;

[0053] ;

[0054] in, P wp,t , P sp,t , P ht,t They are wind turbines, photovoltaic generators, and hydrogen-fired generators in the t The power generation output at all times, P es,t For electric energy storage t The net discharge power at the moment, P g,t For the t The power received by the electric-hydrogen cooperative system from the large power grid at any given moment. P ec,t For the t The power consumption of the electrolyzer at any moment, P oe,t For the t The power consumption of other electrical equipment at all times.

[0055] 2) Hydrogen balance constraints to ensure the balance of hydrogen supply and demand in the electricity-hydrogen synergy system at all times;

[0056] ;

[0057] in, H ec,t For the electrolytic cell t The hydrogen production at the time, H hs,t For hydrogen storage tank t The net amount of hydrogen released at the time, H ht,t For hydrogen-fired units t Hydrogen consumption at each moment, H hp,t For the t The amount of hydrogen exported by the electric-hydrogen coordinated system at each moment.

[0058] 3) Output constraints for various types of equipment, that is, the output at each moment does not exceed the planned capacity;

[0059] ;

[0060] ;

[0061] ;

[0062] ;

[0063] ;

[0064] ;

[0065] in, P wp,t , P sp,t , P ht,t They are wind turbines, photovoltaic generators, and hydrogen-fired generators in the t The power generation output at all times, P es,t For electric energy storage t The net discharge power at the moment, H ec,t For the electrolytic cell t The hydrogen production at the time, H hs,t For hydrogen storage tank t The net amount of hydrogen released at the time, C ec , C ht , C hs , C wp , C sp , C es They are the planned construction capacities of electrolyzers, hydrogen-fired units, hydrogen storage tanks, wind turbines, photovoltaic generators, and electric energy storage.

[0066] 4) Wind power and photovoltaic power generation resource condition constraints, that is, the wind power and photovoltaic power generation output at each moment does not exceed the output limit determined by the weather resource conditions at that time;

[0067] ;

[0068] ;

[0069] in, P wp,t ,P sp,t They are wind turbines and photovoltaic generators in the t The power generation output at all times, W wp,t , W sp,t Respectively t The upper limit of the output of wind turbines and photovoltaic generators is determined by the weather resource conditions at that moment.

[0070] 5) Electricity-hydrogen energy conversion constraints, i.e., the electricity-hydrogen input-output conversion relationship of electricity-hydrogen energy conversion devices such as electrolyzers and hydrogen-fired units;

[0071] ;

[0072] ;

[0073] in, H ec,t For the electrolytic cell t The hydrogen production at the time, u ec , u ht are the energy conversion efficiency of the electrolyzer and the hydrogen-fired unit, v is the calorific value conversion coefficient between electric energy and hydrogen energy, P ec,t For the t The power consumption of the electrolyzer at any moment, P ht,t For hydrogen-fired units t The power generation output at all times, H ht,t For hydrogen-fired units t Hydrogen consumption at each moment.

[0074] 6) Energy storage balance constraint, that is, the energy storage input and output are balanced;

[0075] ;

[0076] in, P es,t For electric energy storage t The net discharge power at the moment, J es The duration of the balancing cycle for energy storage scheduling.

[0077] 7) Hydrogen storage tank balance constraint, that is, the input and output of the hydrogen storage tank are kept balanced;

[0078] ;

[0079] in, Hhs,t For hydrogen storage tank t The net amount of hydrogen released at the time, J hs Schedule the balancing cycle duration for the hydrogen storage tank.

[0080] 8) The power grid is subject to power input constraints, that is, the power input from the external power grid by the electric-hydrogen cooperative system at each moment does not exceed the power range of the access grid;

[0081] ;

[0082] in, P g,t For the t The power received by the electric-hydrogen cooperative system from the large power grid at any given moment. G The maximum exchange power of the electric-hydrogen cooperative system connected to the external power grid.

[0083] 9) Hydrogen production constraints;

[0084] ;

[0085] in, Q h is the expected annual hydrogen production of the electricity-hydrogen synergy system, Y is the number of scheduling times in a year, H ec,t For the electrolytic cell t Hydrogen production at the time.

[0086] 10) Oxygen production constraints;

[0087] ;

[0088] in, Q o is the expected annual oxygen production of the electric-hydrogen synergy system, o is the by-product oxygen coefficient per unit hydrogen production, Q h The expected annual hydrogen production of the electricity-hydrogen synergy system.

[0089] 11) Power consumption constraint, which describes the power consumption index in the objective function;

[0090] ;

[0091] in, Q e is the expected annual power consumption of the electric-hydrogen synergy system, Y is the number of scheduling times in a year, P ec,t For the t The power consumption of the electrolyzer at any moment, Poe,t For the t The power consumption of other electrical equipment at all times.

[0092] 12) Water consumption constraint, which describes the water consumption index in the objective function;

[0093] ;

[0094] in, Q w is the expected annual water consumption of the electricity-hydrogen synergy system, z is the unit hydrogen production water consumption coefficient, Q h The expected annual hydrogen production of the electricity-hydrogen synergy system.

[0095] 13) Equipment planning and construction scale constraints, which are used to consider factors such as raw material supply, resource endowment and construction speed, so that the planning and construction scale of various types of equipment does not exceed its maximum construction capacity;

[0096] ;

[0097] ;

[0098] ;

[0099] ;

[0100] ;

[0101] ;

[0102] C ec , C ht , C hs , C wp , C sp , C es They are the planned construction capacity of electrolyzers, hydrogen-fired units, hydrogen storage tanks, wind turbines, photovoltaic generators, and electric energy storage. X ec , X ht , X hs , X wp , X sp , X esThey are the maximum construction capacities of electrolyzers, hydrogen-fired units, hydrogen storage tanks, wind turbines, photovoltaic generators, and electric energy storage during the planning period.

[0103] S5. Solve the objective function of the optimization planning model of the electric-hydrogen synergistic system considering the ancillary service market revenue according to the constraint conditions to obtain the capacity configuration of each element in the electric-hydrogen synergistic system; S5 specifically includes:

[0104] Based on the above model, a set of solutions that meet various constraints and optimize the objective function are solved, that is, the capacity configuration of each element in the electric-hydrogen synergistic system, such as the electrolyzer, hydrogen-fired unit, hydrogen storage tank, wind turbine, photovoltaic generator, and electric energy storage, is obtained.

[0105] S6. Plan the electric-hydrogen synergistic system according to the capacity configuration of each element in the electric-hydrogen synergistic system.

[0106] By adopting the embodiments of the present invention, the following beneficial effects are achieved:

[0107] The present invention proposes an optimization planning method for the electric-hydrogen synergistic system that takes into account the revenue of the ancillary service market. It can help tap the flexible regulation potential of electric hydrogen production, serve as a flexible resource for the power system, and help the consumption of new energy. At the same time, it can obtain revenue in the ancillary service market, and can also realize the conversion of the flexible regulation value of electric hydrogen production into economic value, thus promoting the development of green hydrogen.

[0108] Device Example 1

[0109] According to an embodiment of the present invention, there is provided an electronic device, including:

[0110] processor; and,

[0111] A memory arranged to store computer executable instructions, which, when executed, cause the processor to perform the steps as described in the above method embodiment.

[0112] Device Example 2

[0113] A storage medium is used to store computer executable instructions, and the computer executable instructions, when executed, implement the steps described in the above method embodiment.

[0114] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit it. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the aforementioned embodiments, or replace some or all of the technical features therein with equivalents. However, these modifications or replacements do not cause the essence of the corresponding technical solutions to deviate from the scope of the technical solutions of the embodiments of the present invention.

Claims

1. A planning method for an electric-hydrogen synergistic system considering the revenue of ancillary service market, characterized in that include: S1. Obtain basic parameters of the ancillary services market; S2. Constructing an optimization planning model for the electric-hydrogen synergistic system taking into account the benefits of the ancillary service market based on the basic parameters of the ancillary service market; S3. Construct the objective function of the optimization planning model of the electric-hydrogen synergistic system considering the ancillary service market revenue with the goal of maximizing the annualized net revenue during the planning period; S4. Construct the constraints of the optimization planning model of the electric-hydrogen synergistic system considering the ancillary service market benefits; S5. Solve the objective function of the optimization planning model of the electric-hydrogen synergistic system considering the ancillary service market revenue according to the constraint conditions to obtain the capacity configuration of each element in the electric-hydrogen synergistic system; S6. Planning the electric-hydrogen synergistic system according to the capacity configuration of each element in the electric-hydrogen synergistic system; The S2 specifically includes: Construct a profit model for the electric-hydrogen synergy system to participate in upward peak regulation; Construct a profit model for the electric-hydrogen synergy system to participate in downward peak regulation; Construct a revenue model for the electric-hydrogen synergistic system to participate in frequency regulation; Construct a profit model for the electric-hydrogen synergistic system to participate in reserve; Construct an optimization planning model for the electric-hydrogen synergistic system considering the benefits of the ancillary service market; The profit model of building an electric-hydrogen synergistic system to participate in upward peak regulation is obtained by formula 1: Formula 1; in, E ur The benefits of the electric-hydrogen synergy system participating in upward peak load regulation, N ur is the expected annual number of times the electric-hydrogen coordinated system participates in upward peak regulation, R ur The average revenue per unit capacity of the electric-hydrogen synergistic system participating in upward peak regulation is: is the potential coefficient of the electrolyzer participating in upward peak regulation, C ec For the planned construction capacity of the electrolyzer, is the potential coefficient of hydrogen-fired units participating in upward peak regulation, C ht Planned construction capacity for hydrogen-fired units; The profit model of building an electric-hydrogen synergistic system to participate in downward peak regulation is obtained by formula 2: Formula 2; in, E dr The benefits of the electric-hydrogen synergy system participating in downward peak load regulation are: N dr is the expected annual number of times the electric-hydrogen coordinated system participates in downward peak regulation, R dr The average revenue per unit capacity of the electric-hydrogen synergy system participating in downward peak regulation, is the potential coefficient of the electrolyzer participating in downward peak regulation, C ec For the planned construction capacity of the electrolyzer, is the potential coefficient of hydrogen-fired units participating in downward peak regulation, C ht Planned construction capacity for hydrogen-fired units; The profit model of building an electric-hydrogen coordinated system to participate in frequency regulation is obtained by formula 3: Formula 3: in, E fr The benefits of the electric-hydrogen synergy system participating in frequency regulation, N fr is the expected annual number of times the electric-hydrogen cooperative system participates in frequency regulation, R fr is the average revenue per unit capacity of the electric-hydrogen cooperative system participating in frequency regulation, is the potential coefficient of the electrolytic cell participating in frequency regulation, C ec For the planned construction capacity of the electrolyzer, is the potential coefficient of hydrogen-fired units participating in frequency regulation, C ht Planned construction capacity for hydrogen-fired units; The profit model of building an electric-hydrogen coordinated system to participate in reserve is obtained by formula 4: Formula 4: in, E sr The benefits of participating in the reserve of the electric-hydrogen coordinated system, N sr is the expected annual number of times the electric-hydrogen coordinated system participates in the reserve function, R sr is the average revenue per unit capacity of the electric-hydrogen synergistic system participating in the reserve, is the potential coefficient of the electrolytic cell participating in the standby, C ec For the planned construction capacity of the electrolyzer, is the potential coefficient of hydrogen-fired units participating in standby, C ht Planned construction capacity for hydrogen-fired units; The optimization planning model for the electric-hydrogen synergistic system considering the ancillary service market revenue is obtained by formula 5: Formula 5: The S3 specifically includes: The objective function of the optimization planning model of the electric-hydrogen synergistic system considering the ancillary service market revenue is constructed by formula 6: Formula 6: in, N ur is the expected annual number of times the electric-hydrogen coordinated system participates in upward peak regulation, R ur The average revenue per unit capacity of the electric-hydrogen synergistic system participating in upward peak regulation is: is the potential coefficient of the electrolyzer participating in upward peak regulation, C ec For the planned construction capacity of the electrolyzer, is the potential coefficient of hydrogen-fired units participating in upward peak regulation, C ht For the planned construction capacity of hydrogen-fired units, N dr is the expected annual number of times the electric-hydrogen coordinated system participates in downward peak regulation, R dr The average revenue per unit capacity of the electric-hydrogen synergy system participating in downward peak regulation, is the potential coefficient of the electrolyzer participating in downward peak regulation, is the potential coefficient of hydrogen-fired units participating in downward peak regulation, E fr The benefits of the electric-hydrogen synergy system participating in frequency regulation, N fr is the expected annual number of times the electric-hydrogen cooperative system participates in frequency regulation, R fr is the average revenue per unit capacity of the electric-hydrogen cooperative system participating in frequency regulation, is the potential coefficient of the electrolytic cell participating in frequency regulation, is the potential coefficient of hydrogen-fired units participating in frequency regulation, E sr The benefits of participating in the reserve of the electric-hydrogen synergy system, N sr is the expected annual number of times the electric-hydrogen coordinated system participates in the reserve function, R sr is the average revenue per unit capacity of the electric-hydrogen synergistic system participating in the reserve, is the potential coefficient of the electrolytic cell participating in the standby, is the potential coefficient of hydrogen-fired units participating in standby, Q h is the expected annual hydrogen production of the electricity-hydrogen synergy system, R h is the unit hydrogen price, Q o is the expected annual oxygen production of the electric-hydrogen synergy system, R o is the unit oxygen price, Q e is the expected annual power consumption of the electric-hydrogen synergy system, R e is the average unit electricity price, Q w is the expected annual water consumption of the electricity-hydrogen synergy system, R w is the average unit water price, M Other annual operation and maintenance costs of the electric-hydrogen synergy system, b ec , b ht , b hs , b wp , b sp , b es They are the unit capacity construction costs of electrolyzer, hydrogen-fired unit, hydrogen storage tank, wind turbine, photovoltaic generator, and electric energy storage. C ec , C ht , C hs , C wp , C sp , C es They are the planned construction capacity of electrolyzers, hydrogen-fired units, hydrogen storage tanks, wind turbines, photovoltaic generators, and electric energy storage. T ec , T ht , T hs , T wp , T sp , T es They are the lifespan of electrolyzer, hydrogen-fired unit, hydrogen storage tank, wind turbine, photovoltaic generator, and electric energy storage; The S4 specifically includes: Set power balance constraints, hydrogen balance constraints, various equipment output constraints, wind power and photovoltaic power generation resource condition constraints, electric-hydrogen energy conversion constraints, electric energy storage balance constraints, hydrogen storage tank balance constraints, grid power input constraints, hydrogen production constraints, oxygen production constraints, power consumption constraints, water consumption constraints, and equipment planning and construction scale constraints; The power balance constraint is obtained by the following formula: Formula 7: in, P wp,t , P sp,t , P ht,t They are wind turbines, photovoltaic generators, and hydrogen-fired generators in the t The power generation output at all times, P es,t For electric energy storage t The net discharge power at the moment, P g,t For the t The power received by the electric-hydrogen cooperative system from the large power grid at any given moment. P ec,t For the t The power consumption of the electrolyzer at any moment, P oe,t For the t The power consumption of other electrical equipment at all times; The hydrogen balance constraint is obtained by the following formula: Formula 8: in, H ec,t For the electrolytic cell t The hydrogen production at the time, H hs,t For the hydrogen storage tank t The net amount of hydrogen released at the time, H ht,t For hydrogen-fired units t Hydrogen consumption at each moment, H hp,t For the t The amount of hydrogen exported by the electricity-hydrogen collaborative system at each moment; The output constraints of various types of equipment are obtained through the following formula: Formula 9: Formula 10: Formula 11: Formula 12: Formula 13: Formula 14: in, P wp,t , P sp,t , P ht,t They are wind turbines, photovoltaic generators, and hydrogen-fired generators in the t The power generation output at all times, P es,t For electric energy storage t The net discharge power at the moment, H ec,t For the electrolytic cell t The hydrogen production at the time, H hs,t For the hydrogen storage tank t The net amount of hydrogen released at the time, C ec , C ht , C hs , C wp , C sp , C es They are the planned construction capacity of electrolyzers, hydrogen-fired units, hydrogen storage tanks, wind turbines, photovoltaic generators, and electric energy storage; The wind power and photovoltaic power generation resource constraints are obtained through the following formula: Formula 15: Formula 16: in, P wp,t , P sp,t They are wind turbines and photovoltaic generators in the t The power generation output at all times, W wp,t , W sp,t Respectively t The upper limit of the output of wind turbines and photovoltaic generators determined by weather resource conditions at any given moment; The electric-hydrogen energy conversion constraint is obtained by the following formula: Formula 17: Formula 18: in, H ec,t For the electrolytic cell t The hydrogen production at the time, u ec , u ht are the energy conversion efficiency of the electrolyzer and the hydrogen-fired unit, v is the calorific value conversion coefficient between electric energy and hydrogen energy, P ec,t For the t The power consumption of the electrolyzer at any moment, P ht,t For hydrogen-fired units t The power generation output at all times, H ht,t For hydrogen-fired units t Hydrogen consumption at each time; The electric energy storage balance constraint is obtained by the following formula: Formula 19: in, P es,t For electric energy storage t The net discharge power at the moment, J es The duration of the balancing cycle for energy storage scheduling; The hydrogen storage tank balance constraint is obtained by the following formula: Formula 20: in, H hs,t For the hydrogen storage tank t The net amount of hydrogen released at the time, J hs Schedule the balancing cycle duration for the hydrogen storage tank; The grid is subject to the power input constraint through the following formula: Formula 21; in, P g,t For the t The power received by the electric-hydrogen cooperative system from the large power grid at any given moment. G The maximum exchange power for the electric-hydrogen synergy system to access the external power grid; The hydrogen production constraint is obtained by the following formula: Formula 22; in, Q h is the expected annual hydrogen production of the electricity-hydrogen synergy system, Y is the number of scheduling times in a year, H ec,t For the electrolytic cell t Hydrogen production at the time; The oxygen production constraint is obtained by the following formula: Formula 23: in, Q o is the expected annual oxygen production of the electric-hydrogen synergy system, o is the by-product oxygen coefficient per unit hydrogen production, Q h The expected annual hydrogen production of the electricity-hydrogen synergy system; The power consumption constraint is obtained by the following formula: Formula 24; Among them, Q e is the expected annual power consumption of the electric-hydrogen cooperative system, Y is the number of dispatching times in a year, and P ec,t is the power consumption of the electrolytic cell at time t, P oe,t is the power consumption of other electrical equipment at time t; The water consumption constraint is obtained by the following formula: Formula 25; in, Q w is the expected annual water consumption of the electricity-hydrogen synergy system, z is the unit hydrogen production water consumption coefficient, Q h The expected annual hydrogen production of the electricity-hydrogen synergy system; The equipment planning and construction scale constraint is obtained by the following formula: Formula 26 ； Formula 27 ； Formula 28 ； Formula 29 ； Formula 30 ； Formula 31 ； C ec , C ht , C hs , C wp , C sp , C es They are the planned construction capacity of electrolyzers, hydrogen-fired units, hydrogen storage tanks, wind turbines, photovoltaic generators, and electric energy storage. X ec , X ht , X hs , X wp , X sp , X es They are the maximum construction capacities of electrolyzers, hydrogen-fired units, hydrogen storage tanks, wind turbines, photovoltaic generators, and electric energy storage during the planning period.

2. The method according to claim 1, characterized in that: The S1 specifically includes: Obtain the upward peak-shaving related parameters of the ancillary service market, the downward peak-shaving related parameters of the ancillary service market, the frequency regulation related parameters of the ancillary service market, and the standby related parameters of the ancillary service market.

3. The method according to claim 2, characterized in that The parameters related to the upward peak load regulation of the ancillary service market include: the annual expected number of times the electric-hydrogen synergy system participates in the upward peak load regulation N ur , the average revenue per unit capacity of the electric-hydrogen synergy system participating in upward peak regulation R ur , the potential coefficient of electrolyzer participating in upward peak regulation , the potential coefficient of hydrogen-fired units participating in upward peak regulation ; The parameters related to downward peak regulation in the ancillary service market include: the expected number of times the electric-hydrogen synergy system participates in downward peak regulation per year N dr , the average revenue per unit capacity of the electric-hydrogen synergy system participating in downward peak regulation R dr , the potential coefficient of electrolyzer participating in downward peak regulation , the potential coefficient of hydrogen-fired units participating in downward peak regulation ; The frequency regulation related parameters of the ancillary service market include: the annual expected number of times the electric-hydrogen cooperative system participates in frequency regulation N fr , the average revenue per unit capacity of the electric-hydrogen synergistic system participating in frequency regulation R fr , the potential coefficient of the electrolyzer participating in frequency regulation , the potential coefficient of hydrogen-fired units participating in frequency regulation ; The reserve-related parameters of the ancillary service market include: the annual expected number of times the electric-hydrogen collaborative system participates in reserve N sr , the average revenue per unit capacity of the electric-hydrogen synergy system participating in the reserve R sr , the potential coefficient of electrolytic cell participation in standby , potential coefficient of hydrogen-fired units participating in standby .

4. An electronic device comprising: processor; as well as, A memory arranged to store computer executable instructions, which, when executed, cause the processor to perform the steps of the method for planning an electric-hydrogen coordinated system taking into account the benefits of ancillary service markets as described in any one of claims 1 to 3.

5. A storage medium for storing computer executable instructions, which, when executed, implement the steps of the electric-hydrogen collaborative system planning method taking into account the ancillary service market benefits as described in any one of claims 1-3.

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