CN112163780A - Wind-solar complementary system-hydrogen storage capacity planning method and system - Google Patents

Wind-solar complementary system-hydrogen storage capacity planning method and system Download PDF

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CN112163780A
CN112163780A CN202011096239.5A CN202011096239A CN112163780A CN 112163780 A CN112163780 A CN 112163780A CN 202011096239 A CN202011096239 A CN 202011096239A CN 112163780 A CN112163780 A CN 112163780A
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hydrogen
cost
power
wind
hydrogen production
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方彤
蒋东方
袁铁江
孙传帅
杨彪
许晓艳
鲁强
贾跃龙
滕越
徐斌
陈国宏
赵骞
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Dalian University of Technology
Electric Power Research Institute of State Grid Anhui Electric Power Co Ltd
State Grid Energy Research Institute Co Ltd
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Dalian University of Technology
Electric Power Research Institute of State Grid Anhui Electric Power Co Ltd
State Grid Energy Research Institute Co Ltd
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    • 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
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    • G06Q10/0637Strategic management or analysis, e.g. setting a goal or target of an organisation; Planning actions based on goals; Analysis or evaluation of effectiveness of goals
    • 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
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Abstract

The invention discloses a wind-solar hybrid system-hydrogen storage capacity planning method and a system. The method comprises the following steps: calculating the cost and the benefit of the hydrogen production-storage system; calculating the net benefit of the hydrogen production-storage system according to the cost and the benefit of the hydrogen production-storage system; acquiring a constraint condition; determining the maximum value of the net gain of the system according to the constraint condition; and determining the capacity of the hydrogen production-storage system when the net benefit of the system is maximum. The invention can reasonably distribute renewable energy sources for integration and development of a power grid, and the hydrogen production-storage system obtains system benefits to the maximum extent under the condition of meeting regional hydrogen energy demand, and obtains the optimal hydrogen production system scale under different hydrogen production modes by considering the punishment cost of wind abandonment and light abandonment and hydrogen energy supply shortage and the environmental benefit of the system.

Description

Wind-solar complementary system-hydrogen storage capacity planning method and system
Technical Field
The invention relates to the field of hydrogen storage capacity planning, in particular to a wind-solar hybrid system-hydrogen storage capacity planning method and system.
Background
The development of conventional energy power generation technology is restricted by the pollution problem and the energy exhaustion problem of conventional energy, and new energy power generation grid-connected operation is more and more attracted by people with the development of new energy power generation technology in recent years. Wind energy and solar energy power generation are two of new energy power generation which have development prospects.
However, the new energy power generation has the characteristics of randomness and volatility, and the uncertainty of the effective capacity and the output power of the new energy brings many challenges to the power and electric quantity balance calculation. The complexity and uncertainty problems of medium-and long-term power and electric quantity balance after large-scale grid connection are obviously increased. Adversely affecting the stable operation of the system.
Scholars at home and abroad make a lot of researches on the problem of power and electricity balance of new energy grid connection, and most researches are to solve the problem of consumption of new energy grid connection through adjustment of conventional units under the condition that the power generation proportion of new energy is not high
Disclosure of Invention
The invention aims to provide a wind-solar hybrid hydrogen production-hydrogen storage capacity planning method and system, which can reasonably distribute renewable energy sources for integration and development of a power grid and obtain the optimal hydrogen production system scale under different hydrogen production modes.
In order to achieve the purpose, the invention provides the following scheme:
a wind-solar hybrid system-hydrogen storage capacity planning method comprises the following steps:
calculating the cost and the benefit of the hydrogen production-storage system;
calculating the net benefit of the hydrogen production-storage system according to the cost and the benefit of the hydrogen production-storage system;
acquiring a constraint condition;
determining the maximum value of the net gain of the system according to the constraint condition;
and determining the capacity of the hydrogen production-storage system when the net benefit of the system is maximum.
Alternatively, the cost and benefits of the system for producing-storing hydrogen include: investment cost, system annual operation maintenance cost, system electricity purchasing cost from a power grid, wind and light abandoning punishment cost, hydrogen shortage punishment cost, market-oriented hydrogen selling and receiving of the system, power supply income of the system to the power grid, environmental income of reducing pollution discharge of a coal-fired unit by the system power on the grid and environmental income of wind, light and electricity hydrogen production.
Optionally, the constraint condition includes: the method comprises the following steps of power balance constraint, system operation equivalent power balance constraint, grid-connected power constraint, hydrogen storage tank capacity limitation and system hydrogen supply reliability limitation.
Alternatively, the cost of the hydrogen production-storage system is calculated as follows:
M=Ch+Ce+Cen1+Cen2-CC-COM-CS-Cwp.cut-Cph
wherein, CCTo investment costs, COMFor annual operating maintenance costs of the system, CSCost of electricity purchase from the grid for the system, Cwp.cutPenalizing costs for wind and light rejection, CphPenalizing the cost for hydrogen deficiency, ChFor the system market-oriented hydrogen sales revenue, CeRevenue of power supply of the system to the grid, Cen1Environmental benefits of reducing coal-fired unit pollution discharge for system on-line electricity quantity, Cen2The environmental benefit for the wind, light and electricity hydrogen production is gained.
Optionally, the investment cost CCThe calculation formula of (a) is as follows:
Figure BDA0002723839680000021
wherein: n is a radical ofiSpecific capacity, N, of each unit of equipment for making a hydrogen storage system1、N2、N3And N4Unit capacity, C, of the electrolyzer, hydrogen storage tank, fuel cell and electricity transmission project, respectivelyiUnit price per unit capacity of each equipment for making hydrogen storage system, C1、C2、C3And C4Unit price per unit capacity of electrolytic cell, hydrogen storage tank and fuel cell power transmission project, r is depreciation rate, LiThe engineering age is the engineering age.
Optionally, the system annual operating maintenance cost COMAnd the system purchases electricity cost C from the power gridSThe calculation formula of (a) is as follows:
Figure BDA0002723839680000022
Figure BDA0002723839680000023
wherein liThe operation and maintenance cost of each equipment for manufacturing the hydrogen storage system is in proportion to the initial investment, Ps(t) Power purchase to the grid in real time, ζS(t) isAnd (5) real-time electricity price for purchasing electricity to the power grid.
Optionally, the wind curtailment and light curtailment penalty cost Cwp.cutAnd hydrogen deficiency punished as CphThe calculation formula of (a) is as follows:
Figure BDA0002723839680000031
Figure BDA0002723839680000032
in the formula: lambda [ alpha ]wt、Pwt.curt(t) and ζwp(t) punishment cost coefficients of wind abandoning and light abandoning, wind abandoning and light abandoning power and wind-solar power generation internet access electricity price are respectively; lambda [ alpha ]phPenalty cost factor for hydrogen energy shortage, ζph(t) real-time hydrogen price on the market, Ddm(t) real-time demand for Hydrogen energy, Dsh(T) the real-time available amount of hydrogen energy, T being the number of points in the selected sampling interval.
Alternatively, the system is directed to a market Hydrogen sales revenue ChAnd the power supply income C of the system to the power grideThe calculation formula of (a) is as follows:
Figure BDA0002723839680000033
Figure BDA0002723839680000034
wherein, Pgs(t) is wind power on-line power, PfcAnd (t) is the real-time working power of the fuel cell.
Optionally, the system is used for reducing the environmental benefit C of coal-fired unit pollution dischargeen1Environmental benefits of wind-solar-photovoltaic hydrogen production Cen2The calculation formula is as follows:
Figure BDA0002723839680000035
Figure BDA0002723839680000036
wherein N is the pollutant type quantity, tau, discharged by the traditional coal-fired unitpIs the charging standard of unit pollution equivalent value of thermal power generation, taukIs the charging standard of the unit pollution equivalent value of hydrogen production from coal, nkAnd mukRespectively the unit emission and the pollution equivalent value of the pollutant k, P, caused by the coal-fired unitel(t) is the real-time operating power of the electrolyzer, eelEnergy consumption for electrolytic hydrogen production ecomEnergy consumption for compressing hydrogen.
The invention also provides a wind-solar hybrid system-hydrogen storage capacity planning system, which comprises:
the cost and income calculation module is used for calculating the cost and income of the hydrogen production-storage system;
a net gain calculation module for calculating net gains of the hydrogen production-storage system according to the cost and gains of the hydrogen production-storage system;
the constraint condition acquisition module is used for acquiring constraint conditions;
the benefit maximum value determining module is used for determining the maximum value of the net benefit of the system according to the constraint condition;
and the capacity determining module is used for determining the capacity of the hydrogen production-storage system when the net income of the system is maximum.
According to the specific embodiment provided by the invention, the invention discloses the following technical effects:
the invention discloses a wind-light complementary hydrogen production-storage capacity planning method and system under the condition of large-scale renewable energy grid connection, which reasonably distributes renewable energy for integration and development of a power grid, and a hydrogen production-storage system obtains system benefits to the maximum extent under the condition of meeting regional hydrogen energy requirements, considers the punishment cost of wind light abandonment and hydrogen energy supply shortage and the environmental benefits of the system, and obtains the optimal hydrogen production system scale under different hydrogen production modes.
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In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings needed to be used in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art to obtain other drawings without inventive exercise.
FIG. 1 is a flow chart of a wind-solar hybrid generation-hydrogen storage capacity planning method according to an embodiment of the invention;
fig. 2 is a block diagram of a wind-solar hybrid system-hydrogen storage capacity planning system according to an embodiment of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
The invention aims to provide a wind-solar hybrid hydrogen production-hydrogen storage capacity planning method and system, which can reasonably distribute renewable energy sources for integration and development of a power grid and obtain the optimal hydrogen production system scale under different hydrogen production modes.
In order to make the aforementioned objects, features and advantages of the present invention comprehensible, embodiments accompanied with figures are described in further detail below.
As shown in fig. 1, a method for planning wind-solar hybrid system-hydrogen storage capacity includes:
step 101: and calculating the cost and the benefit of the hydrogen production-storage system.
The system cost is as follows:
annual investment costs of electrolyzer, compressor, hydrogen storage tank, fuel cell CC
Figure BDA0002723839680000051
In the formula: n is a radical ofiSpecific capacity, N, of each unit of equipment for making a hydrogen storage system1、N2、N3And N4Unit capacity, C, of the electrolyzer, hydrogen storage tank, fuel cell and electricity transmission project, respectivelyiUnit price per unit capacity of each equipment for making hydrogen storage system, C1、C2、C3And C4Unit prices per unit capacity of an electrolytic cell, a hydrogen storage tank and a fuel cell in a power transmission project, r is a depreciation rate and LiAnd (5) engineering age limit.
Annual operating maintenance cost of the system COMThe system purchases electricity from the power grid at a cost CS
Figure BDA0002723839680000052
Figure BDA0002723839680000053
Pwp(t)=Pwt(t)+Ppv(t)
In the formula: liThe operation and maintenance cost of each equipment for manufacturing the hydrogen storage system is in proportion to the initial investment, Ps(t) Power purchase to the grid in real time, ζS(t) real-time electricity prices for purchasing electricity from the grid, Ppv(t) represents the real-time generated power of the photovoltaic power plant, Pwt(t) represents the real-time generated power of the wind farm.
Wind and light abandon penalty cost Cwp.cutPenalty cost for hydrogen deficiency Cph
Figure BDA0002723839680000054
Figure BDA0002723839680000061
In the formula: lambda [ alpha ]wt、Pwt.curt(t) and ζwp(t) punishment cost coefficients of wind abandoning and light abandoning, wind abandoning and light abandoning power and wind-solar power generation internet access electricity price are respectively; lambda [ alpha ]phPenalty cost factor for hydrogen energy shortage, ζph(t) real-time hydrogen price on the market, Ddm(t) real-time hydrogen energy demand, Dsh(T) the real-time available amount of hydrogen energy, T being the number of points in the selected sampling interval.
And (4) system yield:
system market-oriented hydrogen sales revenue Ch(ii) a System power supply income C to power gride
Figure BDA0002723839680000062
Figure BDA0002723839680000063
Wherein, Pgs(t) is wind power on-line power, PfcAnd (t) is the real-time working power of the fuel cell.
Environmental benefit C of reducing coal-fired unit pollution discharge for system power on-line electric quantityen1
Figure BDA0002723839680000064
In the formula: n is the number of the types of pollutants discharged by the traditional coal-fired unit, taupIs a charging standard of unit pollution equivalent value of thermal power generation, nkAnd mukThe unit emission amount and the pollution equivalent value of the pollutant k caused by the coal-fired unit are respectively.
Wind-solar-electricity hydrogen production environmental benefit Cen2
Figure BDA0002723839680000065
Pel(t) is the real-time operating power of the electrolyzer, eelEnergy consumption for electrolytic hydrogen production, ecomEnergy consumption for compressing hydrogen, τkIs the charging standard of the unit pollution equivalent value of the hydrogen produced by coal.
The net profit M of the system is:
M=Ch+Ce+Cen1+Cen2-CC-COM-CS-Cwp.cut-Cph
step 102: and calculating the net benefit of the hydrogen production-storage system according to the cost and the benefit of the hydrogen production-storage system.
Step 103: and acquiring constraint conditions.
(1) And (3) real-time working power constraint of the electrolytic cell: the optimal working interval of the electrolytic cell is 50% -100% of rated power, and the simplified model is as follows:
Pel.min≤Pel(t)≤Pel.max
Pel.min=0.5·Pel.max
in the formula, Pel(t) is the real-time working power of the electrolyzer, Pel.min、Pel.maxRespectively the minimum operating power and the maximum power of the electrolytic cell.
(2) And (3) real-time working power constraint of the fuel cell: the fuel cell operating power is 10% -100% of rated power, and the simplified model is as follows:
Pfc(t)=Hfc(t)×ηfc×HLHV
Pfc.min≤Pfc(t)≤Pfc.max
Pfc.min=10%·Pfc.max
Pfc(t) real-time operating power of the fuel cell, Hfc(t) is the real-time hydrogen consumption of the fuel cell in kg; etafcFor the operating efficiency of the cell, HLHVIs a low calorific value of hydrogen of 120MJ/kg (33.3 kWh/kg); pfc.maxIs the maximum operating power, also the rated power, P, of the fuel cellfc.minIs the minimum operating power of the fuel cell.
(3) And power balance constraint:
Pgs(t)+Pwp.curt(t)+Pel(t)=Pwp(t)
in the formula: pwp(t) wind and photovoltaic output, Pwp.curt(t) is the power of abandoned wind and abandoned light, Pgs(t) wind power grid power, Pel(t) inputting power to the electrolytic cell.
(4) And (3) system operation equivalent power balance constraint:
the hydrogen produced by the electrolyzer, after being compressed by the compressor, can be sold directly or stored in a hydrogen storage facility, which can be designated as follows.
Figure BDA0002723839680000071
Qin(t) the amount of hydrogen produced by the electrolyzer at time t and compressed by the compressor into the hydrogen storage tank, Pel(t) is the power input to the cell. Energy consumption e of hydrogen production by electrolysisel(HLHVelkWh/kg) and energy consumption e for compressing hydrogencom(kWh/kg)。
The amount of hydrogen stored in the high-pressure hydrogen storage apparatus at each moment may be expressed as:
Qtan(t)=Qtan(t-1)+Qin(t)-Qsh(t)-Qfc(t)
Dsh(t)=Qsh(t)·
in the formula: qtan(t-1) and Qtan(t) the amounts of hydrogen gas stored in the hydrogen storage tank at times t-1 and t, respectively; qsh(t) the amount of hydrogen sold at time t, QfcAnd (t) is the amount of hydrogen consumed by the fuel cell at time t, and is the mass volume fraction of hydrogen at high pressure, kg/L.
(5) And (3) grid-connected power constraint:
0≤Pgs(t)+Pfc(t)≤Pbw
Pbwrepresenting the upper limit of power incorporation into the grid.
(6) Capacity limitation of the hydrogen storage tank:
0.1·Qtan≤Qtan(t)≤0.9·Qtan
(7) and (3) limiting the reliability of hydrogen supply of the system:
because the invention considers the capability of a large-scale hydrogen production-storage system for providing load hydrogen demand, the hydrogen supply reliability of the system is represented by the hydrogen deficiency rate (HSSP), which is defined as:
Figure BDA0002723839680000081
t is the total duration, T represents the time, and obviously, the smaller the HSSP, the higher the hydrogen supply reliability.
Step 104: and determining the maximum value of the net gain of the system according to the constraint condition.
Step 105: and determining the capacity of the hydrogen production-storage system when the net benefit of the system is maximum.
As shown in fig. 2, the present invention further provides a wind-solar hybrid system-hydrogen storage capacity planning system, which includes:
and a cost and profit calculation module 201 for calculating the cost and profit of the hydrogen production-storage system.
A net benefit calculation module 202 for calculating net benefits of the hydrogen production-storage system based on the costs and benefits of the hydrogen production-storage system.
And a constraint condition obtaining module 203, configured to obtain a constraint condition.
And a benefit maximum determination module 204, configured to determine a maximum value of the net benefit of the system according to the constraint condition.
A capacity determination module 205 for determining a capacity of the hydrogen storage system at which the net gain of the system is maximized.
The embodiments in the present description are described in a progressive manner, each embodiment focuses on differences from other embodiments, and the same and similar parts among the embodiments are referred to each other. For the system disclosed by the embodiment, the description is relatively simple because the system corresponds to the method disclosed by the embodiment, and the relevant points can be referred to the method part for description.
The principles and embodiments of the present invention have been described herein using specific examples, which are provided only to help understand the method and the core concept of the present invention; meanwhile, for a person skilled in the art, according to the idea of the present invention, the specific embodiments and the application range may be changed. In view of the above, the present disclosure should not be construed as limiting the invention.

Claims (10)

1. A wind-solar hybrid system-hydrogen storage capacity planning method is characterized by comprising the following steps:
calculating the cost and the benefit of the hydrogen production-storage system;
calculating the net benefit of the hydrogen production-storage system according to the cost and the benefit of the hydrogen production-storage system;
acquiring a constraint condition;
determining the maximum value of the net gain of the system according to the constraint condition;
and determining the capacity of the hydrogen production-storage system when the net benefit of the system is maximum.
2. The method of claim 1, wherein the cost and benefits of the system for hydrogen generation and storage comprise: investment cost, system annual operation maintenance cost, system electricity purchasing cost from a power grid, wind and light abandoning punishment cost, hydrogen shortage punishment cost, market-oriented hydrogen selling and receiving of the system, power supply income of the system to the power grid, environmental income of reducing pollution discharge of a coal-fired unit by the system power on the grid and environmental income of wind, light and electricity hydrogen production.
3. The method of claim 1, wherein the constraints comprise: the method comprises the following steps of electrolyzer real-time working power constraint, fuel cell real-time working power constraint, power balance constraint, system operation equivalent power balance constraint, grid-connected power constraint, hydrogen storage tank capacity limitation and system hydrogen supply reliability limitation.
4. The method for planning the wind-solar hybrid hydrogen production-storage capacity according to claim 2, wherein the cost of the hydrogen production-storage system is calculated according to the following formula:
M=Ch+Ce+Cen1+Cen2-CC-COM-CS-Cwp.cut-Cph
wherein, CCTo investment costs, COMFor annual operating maintenance costs of the system, CSCost of electricity purchase from the grid for the system, Cwp.cutPenalizing costs for wind and light rejection, CphPenalizing the cost for hydrogen deficiency, ChFor the system market-oriented hydrogen sales revenue, CeRevenue of power supply of the system to the grid, Cen1Environmental benefits of reducing coal-fired unit pollution discharge for system on-line electricity quantity, Cen2The environmental benefit for the wind, light and electricity hydrogen production is gained.
5. The method of claim 4, wherein the investment cost C isCThe calculation formula of (a) is as follows:
Figure FDA0002723839670000011
wherein: n is a radical ofiSpecific capacity, N, of each unit of equipment for making a hydrogen storage system1、N2、N3And N4Unit capacity, C, of the electrolyzer, hydrogen storage tank, fuel cell and electricity transmission project, respectivelyiUnit price per unit capacity of each equipment for making hydrogen storage system, C1、C2、C3And C4Unit price per unit capacity of electrolytic cell, hydrogen storage tank and fuel cell power transmission project, r is depreciation rate, LiThe engineering age is the engineering age.
6. The method of claim 5, wherein the system annual operating maintenance cost COMAnd the system purchases electricity cost C from the power gridSThe calculation formula of (a) is as follows:
Figure FDA0002723839670000021
Figure FDA0002723839670000022
wherein liThe operation and maintenance cost of each equipment for manufacturing the hydrogen storage system is in proportion to the initial investment, Ps(t) Power purchase to the grid in real time, ζSAnd (t) the real-time electricity price for purchasing electricity to the power grid.
7. The wind-solar hybrid hydrogen storage capacity planning method according to claim 5, wherein the wind curtailment and light curtailment penalty cost Cwp.cutAnd hydrogen deficiency punished as CphThe calculation formula of (a) is as follows:
Figure FDA0002723839670000023
Figure FDA0002723839670000024
in the formula: lambda [ alpha ]wt、Pwt.curt(t) and ζwp(t) punishment cost coefficients of wind abandoning and light abandoning, wind abandoning and light abandoning power and wind-solar power generation internet access electricity price are respectively; lambda [ alpha ]phPenalty cost factor for hydrogen energy shortage, ζph(t) real-time hydrogen price on the market, Ddm(t) real-time hydrogen energy demand, Dsh(T) the real-time available amount of hydrogen energy, T being the number of points in the selected sampling interval.
8. The method of claim 7, wherein the system provides a market oriented hydrogen sales revenue ChAnd the power supply income C of the system to the power grideThe calculation formula of (a) is as follows:
Figure FDA0002723839670000025
Figure FDA0002723839670000031
wherein, Pgs(t) is wind power on-line power, PfcAnd (t) is the real-time working power of the fuel cell.
9. The method of claim 8, wherein the environmental benefit C of reducing coal-fired unit pollution discharge is reduced by the amount of electricity on the griden1Environmental benefits of wind-solar-photovoltaic hydrogen production Cen2The calculation formula is as follows:
Figure FDA0002723839670000032
Figure FDA0002723839670000033
wherein N is the pollutant type quantity, tau, discharged by the traditional coal-fired unitpIs the charging standard of unit pollution equivalent value of thermal power generation, taukIs the charging standard of the unit pollution equivalent value of hydrogen production from coal, nkAnd mukRespectively the unit emission and the pollution equivalent value of the pollutant k, P, caused by the coal-fired unitel(t) is the real-time operating power of the electrolyzer, eelEnergy consumption for electrolytic hydrogen production ecomEnergy consumption for compressing hydrogen.
10. A wind-solar hybrid system-hydrogen storage capacity planning system is characterized by comprising:
the cost and income calculation module is used for calculating the cost and income of the hydrogen production-storage system;
a net gain calculation module for calculating net gains of the hydrogen production-storage system according to the cost and gains of the hydrogen production-storage system;
the constraint condition acquisition module is used for acquiring constraint conditions;
the benefit maximum value determining module is used for determining the maximum value of the net benefit of the system according to the constraint condition;
and the capacity determining module is used for determining the capacity of the hydrogen production-storage system when the net income of the system is maximum.
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