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CN115115087A - Virtual power plant coordinated scheduling method considering hydrogen fuel automobile and hydrogen energy storage - Google Patents

Virtual power plant coordinated scheduling method considering hydrogen fuel automobile and hydrogen energy storage Download PDF

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CN115115087A
CN115115087A CN202210533501.0A CN202210533501A CN115115087A CN 115115087 A CN115115087 A CN 115115087A CN 202210533501 A CN202210533501 A CN 202210533501A CN 115115087 A CN115115087 A CN 115115087A
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张海波
王兆霖
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Abstract

The invention discloses a virtual power plant coordinated scheduling method considering hydrogen fuel automobiles and hydrogen energy storage, which comprises the following steps: calculating the hydrogenation time and the required fuel quantity of the hydrogen energy automobile based on the historical data of the road; constructing a hydrogen energy storage system electrolytic cell, a fuel cell and a hydrogen storage tank model; scene generation is carried out on wind and light output by adopting an autoregressive moving average based model, clustering is carried out by adopting a K-means clustering algorithm, and a plurality of typical scenes are generated; and constructing an objective function of the virtual power plant scheduling model with the aim of maximizing the expected economic benefit. Analyzing the influence of whether hydrogen energy storage participates in the scheduling of the virtual power plant and whether the virtual power plant participates in the rotary standby market, the peak shaving market and the carbon emission right trade on the income and the scheduling result; generating a scene set by typical solar wind light output in summer and winter, substituting the scene set into the model for optimal scheduling, and analyzing the scheduling optimization condition of the virtual power plant.

Description

一种考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法A coordinated scheduling method for virtual power plants considering hydrogen fuel vehicles and hydrogen energy storage

技术领域technical field

本发明涉及虚拟电厂应用技术领域,尤其涉及一种考虑氢燃料汽车与氢储 能的虚拟电厂协调调度方法。The invention relates to the technical field of virtual power plant applications, and in particular to a virtual power plant coordination scheduling method considering hydrogen fuel vehicles and hydrogen energy storage.

背景技术:Background technique:

氢燃料汽车(hydrogen vehicle,HV)因其清洁和节能的特点,与传统的内燃 机汽车相比有望显著降低温室气体的排放,同时,在低温环境下的性能更优于 电动汽车,因此被认为是在未来交通领域的替代技术之一。Compared with traditional internal combustion engine vehicles, hydrogen vehicles (HV) are expected to significantly reduce greenhouse gas emissions due to their cleanliness and energy-saving features. At the same time, their performance in low temperature environments is better than that of electric vehicles. One of the alternative technologies in the field of future transportation.

然而由于目前氢燃料供给体系建设不完善,导致HV存在燃料成本过高、加 氢站网点少等问题,制约了HV的推广应用。利用分布式新能源发电电解水制氢 在利用新能源消纳的同时还保证了氢燃料的供给,是解决此问题的一个有效手 段。氢能利于存储,在各种储能方式中,氢储能在储能密度和储能时间等方面 具有优势,此外氢储能还具有资源广泛、清洁无污染等优点。制备的氢气可作 为氢燃料供给HV,也可实现向电能、热能的转化,成为支撑多能源互补、构建 统一能源体系的纽带。However, due to the imperfect construction of the current hydrogen fuel supply system, HV has problems such as high fuel cost and few hydrogen refueling stations, which restricts the popularization and application of HV. Using distributed new energy to generate electricity and electrolyze water to produce hydrogen can ensure the supply of hydrogen fuel while using new energy to consume, which is an effective means to solve this problem. Hydrogen energy is beneficial to storage. Among various energy storage methods, hydrogen energy storage has advantages in terms of energy storage density and energy storage time. In addition, hydrogen energy storage also has the advantages of extensive resources, cleanliness and no pollution. The prepared hydrogen can be used as hydrogen fuel to supply HV, and can also be converted into electric energy and heat energy, becoming a link to support multi-energy complementarity and build a unified energy system.

综上,本文在虚拟电厂的技术框架下,基于HV商用车的运行特点,对HV 的用氢量进行负荷预测,采用场景法考虑新能源出力的不确定性,结合氢储能 的特点,同时考虑电、热、氢等负荷的协调调度,令虚拟电厂同时参与能量市 场(energy market,EM)、旋转备用市场(spinning reserve market,SRM)、调 峰市场(peak regulation market,PRM)和碳排放权交易市场,以VPP期望收益 最大化为目标,构建了协调优化调度模型,以求获得电解水制氢VPP的最大收 益,探索电解水制氢的商业可行性。To sum up, under the technical framework of virtual power plant, based on the operational characteristics of HV commercial vehicles, this paper forecasts the hydrogen consumption of HVs. The scenario method is used to consider the uncertainty of new energy output, combined with the characteristics of hydrogen energy storage. Considering the coordinated scheduling of electricity, heat, hydrogen and other loads, the virtual power plant can participate in the energy market (EM), spinning reserve market (SRM), peak regulation market (PRM) and carbon emissions at the same time With the goal of maximizing the expected revenue of VPP, a coordinated optimization scheduling model is constructed to obtain the maximum revenue of VPP from electrolyzed water for hydrogen production, and to explore the commercial feasibility of electrolyzed water to produce hydrogen.

发明目的Purpose of invention

本发明的目的在于,提供一种考虑氢燃料汽车与氢储能的虚拟电厂协调调 度方法,比较是否考虑氢储能对虚拟电厂优化调度的经济性的影响,考虑新能 源出力的不确定性对虚拟电厂调度的影响,并分析虚拟电厂参与能量市场、旋 转备用市场、调峰市场和碳排放权交易对收益和调度结果的影响,保证了调度 方案的全面性和最优性。The purpose of the present invention is to provide a virtual power plant coordination scheduling method considering hydrogen fuel vehicles and hydrogen energy storage, comparing whether to consider the influence of hydrogen energy storage on the economy of optimal scheduling of virtual power plants, and considering the uncertainty of new energy output. The impact of virtual power plant scheduling is analyzed, and the impact of virtual power plants' participation in energy market, rotating reserve market, peak shaving market and carbon emission trading on revenue and scheduling results is analyzed to ensure the comprehensiveness and optimality of the scheduling plan.

发明内容SUMMARY OF THE INVENTION

本发明提供了一种考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法,所 述虚拟电厂包括风电机组、光伏电站、CHP机组、氢储能系统、热储能单元, 所述氢储能系统包括电解槽、HFC和储氢罐,其中,风电机组、光伏电站、CHP 机组和外接电网共同为氢储能系统提供电解水制氢的电能和向外界支持电负荷 IL,外部的天然气市场为CHP机组提供燃料,氢储能系统向外支持氢负荷;HFC、 CHP机组和热储能单元共同支持热负荷;所述调度方法包括以下步骤:The present invention provides a method for coordinating and dispatching a virtual power plant considering hydrogen fuel vehicles and hydrogen energy storage. The system includes electrolyzers, HFCs and hydrogen storage tanks. Among them, wind turbines, photovoltaic power stations, CHP units and external power grids jointly provide the hydrogen energy storage system with electricity for electrolysis of water to produce hydrogen and support the electrical load IL to the outside world. The external natural gas market is The CHP unit provides fuel, and the hydrogen energy storage system supports the hydrogen load outward; the HFC, the CHP unit and the thermal energy storage unit jointly support the heat load; the dispatch method includes the following steps:

步骤1、构建考虑与路网耦合的氢燃料汽车所需氢负荷的预测模型,所述氢 燃料汽车的形式线路是从加氢站到其他多个地点的行驶路线;根据氢燃料汽车 到达加氢站时间和剩余燃料量得到燃料需求量;Step 1. Construct a prediction model considering the hydrogen load required by the hydrogen fuel vehicle coupled with the road network. The form route of the hydrogen fuel vehicle is the driving route from the hydrogen refueling station to other multiple locations; according to the hydrogen fuel vehicle arriving at hydrogen refueling Station time and remaining fuel amount to get fuel demand;

步骤2、构建包含电解槽、储氢罐和氢燃料电池的氢储能系统模型,包括电 解槽、储氢罐和燃料电池设备的模型以及系统整体的模型;Step 2. Build a hydrogen energy storage system model including electrolyzer, hydrogen storage tank and hydrogen fuel cell, including models of electrolyzer, hydrogen storage tank and fuel cell equipment as well as the model of the whole system;

步骤3、采用自回归滑动平均模型和k-means聚类方法生成风光典型出力场 景集;Step 3, adopt the autoregressive moving average model and the k-means clustering method to generate the scenery typical output scene set;

步骤4、以期望经济效益最大化为目标,构建虚拟电厂调度模型的目标函数, 如式(1)所示:Step 4. With the goal of maximizing the expected economic benefits, construct the objective function of the virtual power plant dispatching model, as shown in formula (1):

Figure BDA0003646925140000021
Figure BDA0003646925140000021

式(1)中,Is,i(X0)、Cs,i(X0)分别为场景s下各项运行收益和成本指标函数,X0为优化变量;所述目标函数采用系统运行集约束,包括虚拟电厂整体运行约 束和设备运行约束;In formula (1), Is ,i (X 0 ) and C s,i (X 0 ) are the respective operating income and cost index functions under the scenario s, and X 0 is the optimization variable; the objective function adopts the system operation Set constraints, including the overall operation constraints of the virtual power plant and equipment operation constraints;

步骤5、以夏季和冬季典型日的风、光出力生成场景集,代入虚拟电厂模型 进行优化调度。Step 5. Generate a scene set based on the wind and light output of typical days in summer and winter, and substitute it into the virtual power plant model for optimal scheduling.

优选地,步骤1进一步包括以下子步骤:Preferably, step 1 further includes the following sub-steps:

步骤S11、计算氢燃料汽车到达加氢地点的时间:Step S11, calculate the time when the hydrogen fuel vehicle arrives at the hydrogenation location:

假设HV由聚合器控制,加氢站位于HV线路起始站点,当车辆n跑完第k次 循环返回起始站点,由聚合器获取其到达时间

Figure BDA0003646925140000031
和剩余燃料量
Figure BDA0003646925140000032
则根据式(2) -(4)所示计算方法进行计算:Assuming that the HV is controlled by the aggregator, and the hydrogen refueling station is located at the starting station of the HV line, when the vehicle n returns to the starting station after the kth cycle, the aggregator obtains its arrival time
Figure BDA0003646925140000031
and remaining fuel
Figure BDA0003646925140000032
Then calculate according to the calculation method shown in formulas (2)-(4):

Figure BDA0003646925140000033
Figure BDA0003646925140000033

Figure BDA0003646925140000034
Figure BDA0003646925140000034

Figure BDA0003646925140000035
Figure BDA0003646925140000035

其中,vt为t时段道路i的汽车平均行驶速度,与道路等级、时间及道路车流 量等因素密切相关;α1、α2、α3和β为回归参数与修正系数,随道路等级变化; v0为各等级道路的设计车速;Ft为t时段道路的车流量;F0为为道路的设计通行 车流量;D为车辆行驶过程中途径公交站点数量;

Figure BDA0003646925140000036
为车辆初始时间;Di,d为 途中第(d-1)个站点至第d个站点的道路距离;△td-1为在第(d-1)个站点停车等待 的时间;
Figure BDA0003646925140000037
为车辆n初始燃料量,采用蒙特卡洛模拟进行仿真,生成初始燃料 随机数;l为车辆路线的距离;△m为HV每公里氢耗量;η为汽车非正常行驶状 态下的能耗系数,包括启动加速以及刹车期间发动机所需的负荷功导致的能量 损失;Among them, v t is the average speed of vehicles on road i in period t, which is closely related to factors such as road grade, time, and road traffic flow; α 1 , α 2 , α 3 and β are regression parameters and correction coefficients, which change with the road grade ; v 0 is the design speed of each grade of road; F t is the traffic flow of the road in the t period; F 0 is the design traffic flow of the road; D is the number of bus stops in the process of vehicle driving;
Figure BDA0003646925140000036
is the initial time of the vehicle; D i,d is the road distance from the (d-1)th station to the dth station on the way; △t d-1 is the waiting time at the (d-1)th station;
Figure BDA0003646925140000037
is the initial fuel quantity of vehicle n, which is simulated by Monte Carlo simulation to generate initial fuel random numbers; l is the distance of the vehicle route; △m is the hydrogen consumption per kilometer of the HV; η is the energy consumption coefficient of the vehicle in abnormal driving state , including the energy loss due to the load work required by the engine during start-up acceleration and braking;

步骤S12、计算氢燃料汽车氢负荷需求总量:Step S12, calculate the total amount of hydrogen load demand for hydrogen fuel vehicles:

当剩余燃料小于一定值时,则在到达加氢站后进行加氢,HV加氢状态判断 如式(5)、(6)所示:When the remaining fuel is less than a certain value, hydrogenation is carried out after arriving at the hydrogenation station, and the judgment of the HV hydrogenation state is shown in formulas (5) and (6):

Figure BDA0003646925140000041
Figure BDA0003646925140000041

Figure BDA0003646925140000042
Figure BDA0003646925140000042

其中,mset为HV的燃料阈值;

Figure BDA0003646925140000043
表示第n辆HV在第k次循环结束的t时段 需要加氢;
Figure BDA0003646925140000044
为t时段氢燃料汽车的燃料需求总量;N为氢燃料汽车的数量;
Figure BDA0003646925140000045
为氢燃料汽车的储氢瓶含量。Among them, mset is the fuel threshold of HV;
Figure BDA0003646925140000043
Indicates that the nth HV needs to be hydrogenated in the period t at the end of the kth cycle;
Figure BDA0003646925140000044
is the total fuel demand of hydrogen fuel vehicles in period t; N is the number of hydrogen fuel vehicles;
Figure BDA0003646925140000045
The content of hydrogen storage tanks for hydrogen fuel vehicles.

优选地,步骤2进一步包括以下子步骤:Preferably, step 2 further includes the following sub-steps:

步骤S21、构建电解槽模型:Step S21, build an electrolytic cell model:

设定电解槽单位电量产氢率为ηPtH,则电解槽t时段的产氢气量

Figure BDA0003646925140000046
被表示为 产氢率ηPtH和输入电功率
Figure BDA0003646925140000047
的乘积,如式(7)所示:Set the hydrogen production rate per unit of electricity of the electrolytic cell η PtH , then the hydrogen production amount of the electrolytic cell in the period t
Figure BDA0003646925140000046
is expressed as hydrogen production rate η PtH and input electric power
Figure BDA0003646925140000047
The product of , as shown in formula (7):

Figure BDA0003646925140000048
Figure BDA0003646925140000048

步骤S22、构建氢燃料电池模型:Step S22, build a hydrogen fuel cell model:

氢燃料电池的发电和产热功率分别由消耗氢气量

Figure BDA0003646925140000049
和氢燃料电池温度THFC决定,将氢燃料电池的模型表示为如式(8)所示:The power generation and heat generation power of hydrogen fuel cells are determined by the consumption of hydrogen, respectively.
Figure BDA0003646925140000049
and the hydrogen fuel cell temperature T HFC , the model of the hydrogen fuel cell is expressed as formula (8):

Figure BDA00036469251400000410
Figure BDA00036469251400000410

其中,Ener为能斯特电压;ηact、ηohm、ηcon分别为活化极化、欧姆和浓差损耗; F、MH2分别为法拉第常数和氢气摩尔质量;K、S为热交换系数和交换面积;ηHFCh为氢燃料电池的产热效率;

Figure BDA00036469251400000411
为总功率;Among them, E ner is the Nernst voltage; η act , η ohm , and η con are activation polarization, ohmic and concentration loss, respectively; F, M H2 are Faraday's constant and hydrogen molar mass, respectively; K, S are heat exchange coefficients and exchange area; η HFCh is the heat production efficiency of the hydrogen fuel cell;
Figure BDA00036469251400000411
is the total power;

步骤S23、构建储氢罐模型:Step S23, build a hydrogen storage tank model:

储氢罐储存电解槽生成的氢气,为氢燃料电池提供氢气,给氢燃料汽车补 充燃料并向市场出售氢气获得利润,将储氢罐中的氢气质量表示为如式(9)所 示:The hydrogen storage tank stores the hydrogen generated by the electrolyzer, provides hydrogen for the hydrogen fuel cell, refuels the hydrogen fuel vehicle and sells the hydrogen to the market for profit. The quality of the hydrogen in the hydrogen storage tank is expressed as formula (9):

Figure BDA0003646925140000051
Figure BDA0003646925140000051

式(9)中,

Figure BDA0003646925140000052
为t时段储氢罐中氢气的质量;
Figure BDA0003646925140000053
为t时段电解槽的产氢量;
Figure BDA0003646925140000054
为t时段氢燃料电池的耗氢量;
Figure BDA0003646925140000055
为t时段HV的氢气需求量;In formula (9),
Figure BDA0003646925140000052
is the mass of hydrogen in the hydrogen storage tank at time t;
Figure BDA0003646925140000053
is the hydrogen production of the electrolyzer in period t;
Figure BDA0003646925140000054
is the hydrogen consumption of the hydrogen fuel cell in period t;
Figure BDA0003646925140000055
is the hydrogen demand of HV in period t;

步骤S24、构建氢储能系统模型:Step S24, build a hydrogen energy storage system model:

将氢储能系统整体的模型表示为如式(10)所示:The overall model of the hydrogen energy storage system is expressed as equation (10):

Figure BDA0003646925140000056
Figure BDA0003646925140000056

Figure BDA0003646925140000057
Figure BDA0003646925140000057

Figure BDA0003646925140000058
Figure BDA0003646925140000058

式中,

Figure BDA0003646925140000059
为氢储能系统整体的输出功率;布尔变量
Figure BDA00036469251400000510
分别表示t时段 氢储能电解槽和氢燃料电池工作状态。In the formula,
Figure BDA0003646925140000059
is the overall output power of the hydrogen energy storage system; Boolean variable
Figure BDA00036469251400000510
respectively represent the working states of the hydrogen energy storage electrolyzer and the hydrogen fuel cell in the t period.

优选地,步骤3进一步包括以下子步骤:Preferably, step 3 further includes the following sub-steps:

步骤S31、确定基于均值和标准差的白噪声,即滑动回归平均参数;Step S31, determining the white noise based on the mean and standard deviation, that is, the sliding regression mean parameter;

步骤S32、基于基准预测数据,本着残差方差最小原则,生成负荷风电出力 各1000个场景数据;Step S32, based on the reference prediction data, and in line with the principle of minimum residual variance, generate 1,000 scenario data for each load wind power output;

步骤S33、基于改进k-means聚类算法,对风光出力进行聚类,生成若干个 典型运行场景,具体包括:基于局部密度均值聚类算法寻找初始的数据聚类中 心;基于初始聚类中心,采用k-means聚类算法生成典型运行场景。Step S33, based on the improved k-means clustering algorithm, cluster the wind and solar output, and generate several typical operating scenarios, which specifically include: finding the initial data clustering center based on the local density mean clustering algorithm; based on the initial clustering center, The k-means clustering algorithm is used to generate typical running scenarios.

优选地,步骤4进一步包括以下子步骤:Preferably, step 4 further includes the following sub-steps:

步骤S41、建立虚拟电厂协调调度优化目标模型,目标函数表示为如式(13) 所示:Step S41, establishing a virtual power plant coordination scheduling optimization objective model, and the objective function is expressed as shown in formula (13):

Figure BDA0003646925140000061
Figure BDA0003646925140000061

其中,Is,i(X0)、Cs,i(X0)分别为场景s下各项运行收益和成本指标函数,X0为 优化变量;所述各项的含义分别如下:Among them, I s,i (X 0 ) and C s,i (X 0 ) are the respective operating benefit and cost index functions under the scenario s, and X 0 is the optimization variable; the meanings of the items are as follows:

(1)场景s下虚拟电厂参与日前能量市场、旋转备用和调峰市场的售电总收 益表示为如式(14)所示:(1) Under scenario s, the total revenue of electricity sales of virtual power plants participating in the day-ahead energy market, rotating reserve and peak shaving market is expressed as formula (14):

Figure BDA0003646925140000062
Figure BDA0003646925140000062

其中,

Figure BDA0003646925140000063
表示t时段的日前电能量市场电价;
Figure BDA0003646925140000064
表示t时段的备用容量市 场电价;
Figure BDA0003646925140000065
Figure BDA0003646925140000066
分别表示t时段的向上调峰和向下调峰电价;
Figure BDA0003646925140000067
Figure BDA0003646925140000068
分别表示场景s下t时段虚拟电厂的日前电能量出力、备用出力和向上向下调 峰;
Figure BDA0003646925140000069
表示场景s下t时段虚拟电厂的热出力。
Figure BDA00036469251400000610
分别表示t时 段的EM、SRM、向上调峰和向下调峰电价;
Figure BDA00036469251400000611
分别为场景s下t时段风、 光、电解槽实际出力;
Figure BDA00036469251400000612
分别为CHP机组和HFC参与EM、SRM和向上、向下调峰市场的出力;in,
Figure BDA0003646925140000063
Indicates the day-ahead electricity market electricity price in period t;
Figure BDA0003646925140000064
represents the market electricity price of reserve capacity in period t;
Figure BDA0003646925140000065
and
Figure BDA0003646925140000066
Respectively represent the up-peak and down-peak electricity prices in the t period;
Figure BDA0003646925140000067
and
Figure BDA0003646925140000068
Respectively represent the day-ahead power output, standby output and peak-down peaking of the virtual power plant in the period t under the scenario s;
Figure BDA0003646925140000069
Indicates the heat output of the virtual power plant in the t period under the scenario s.
Figure BDA00036469251400000610
Respectively represent the EM, SRM, peak-up and down-peak electricity prices in t period;
Figure BDA00036469251400000611
are the actual output of wind, light, and electrolytic cell in time period t under scene s, respectively;
Figure BDA00036469251400000612
The output of CHP unit and HFC participating in EM, SRM and up and down peak markets respectively;

(2)场景s下虚拟电厂供热的收益表示为如式(15)所示:(2) The revenue of virtual power plant heating under scenario s is expressed as formula (15):

Figure BDA00036469251400000613
Figure BDA00036469251400000613

其中,

Figure BDA00036469251400000614
分别为CHP机组、HFC和热储能储、放的热 功率;in,
Figure BDA00036469251400000614
are the thermal power of CHP unit, HFC and thermal energy storage and discharge respectively;

(3)场景s下虚拟电厂出售氢气的收益表示为如式(16)所示:(3) In the scenario s, the revenue from the sale of hydrogen by the virtual power plant is expressed as formula (16):

Figure BDA00036469251400000615
Figure BDA00036469251400000615

其中,

Figure BDA0003646925140000071
表示氢气价格;in,
Figure BDA0003646925140000071
represents the hydrogen price;

(4)碳交易收益表示为如式(17)所示:(4) The carbon trading income is expressed as formula (17):

Figure BDA0003646925140000072
Figure BDA0003646925140000072

其中,CCM为碳交易价格;

Figure BDA0003646925140000073
为场景s下t时段虚拟电厂的碳排放配额;γe、 γh分别为CHP机组的供电基准值和供热基准值;Fr为机组供热量修正系数;Among them, C CM is the carbon trading price;
Figure BDA0003646925140000073
is the carbon emission quota of the virtual power plant in the t period under the scenario s; γ e and γ h are the reference value of power supply and the reference value of heat supply of the CHP unit, respectively; F r is the correction coefficient of heat supply of the unit;

(5)场景s下风光发电的运行维护成本表示为如式(18)所示:(5) The operation and maintenance cost of wind and solar power generation in scenario s is expressed as formula (18):

Figure BDA0003646925140000074
Figure BDA0003646925140000074

其中,kW、kPV分别为风光发电的单位运行维护成本;

Figure BDA0003646925140000075
分别为场景s 下t时段风、光实际出力;Among them, k W and k PV are the unit operation and maintenance costs of wind and solar power generation respectively;
Figure BDA0003646925140000075
are the actual output of wind and light in time period t under scene s, respectively;

(6)场景s下虚拟电厂与调度指令偏差的惩罚成本表示为如式(19)所示:(6) In the scenario s, the penalty cost of the deviation between the virtual power plant and the dispatch instruction is expressed as formula (19):

Figure BDA0003646925140000076
Figure BDA0003646925140000076

其中,

Figure BDA0003646925140000077
表示场景s下t时段EM、向上向下调峰的偏差量;γem、γru、γrd分别为EM、向上向下调峰的惩罚系数;in,
Figure BDA0003646925140000077
Represents the deviation amount of EM, upward and downward peak reduction in the t period of scene s; γ em , γ ru , and γ rd are the penalty coefficients of EM and upward and downward peak reduction, respectively;

(7)场景s下CHP机组的成本表示为如式(20)所示:(7) The cost of CHP unit under scenario s is expressed as formula (20):

Figure BDA0003646925140000078
Figure BDA0003646925140000078

其中,α0、α1、α2、α3、α4、α5为CHP机组能耗系数;

Figure BDA0003646925140000079
表示CHP机组 的电出力;Among them, α 0 , α 1 , α 2 , α 3 , α 4 , α 5 are the energy consumption coefficients of CHP units;
Figure BDA0003646925140000079
Indicates the electrical output of the CHP unit;

(8)氢储能的成本包括电解槽、燃料电池和储氢罐的平均投资成本和运维成 本,被表示为如式(21)所示:(8) The cost of hydrogen energy storage includes the average investment cost and operation and maintenance cost of electrolyzers, fuel cells and hydrogen storage tanks, which are expressed as equation (21):

Figure BDA0003646925140000081
Figure BDA0003646925140000081

其中,

Figure BDA0003646925140000082
表示场景s下t时段电解槽、HFC、储氢罐的运行维护 成本;λPtH、λHFC、λHS分别为电解槽、HFC和储氢罐的单位运行维护成本;
Figure BDA0003646925140000083
为 场景s下t时段储氢罐储氢质量。in,
Figure BDA0003646925140000082
represents the operation and maintenance costs of the electrolyzer, HFC, and hydrogen storage tank in the t period of the scenario s; λ PtH , λ HFC , and λ HS are the unit operation and maintenance costs of the electrolyzer, HFC and hydrogen storage tank, respectively;
Figure BDA0003646925140000083
is the hydrogen storage quality of the hydrogen storage tank in the t period of the scenario s.

进一步优选地,所述目标函数采用系统运行集约束,包括虚拟电厂整体运 行约束和设备运行约束,其中,所述虚拟电厂整体运行约束包括:日前电能量 市场功率平衡约束、备用容量约束、向上调峰功率约束、向下调峰功率约束和 热功率平衡约束,分别表达为如下所示:Further preferably, the objective function adopts system operation set constraints, including the overall operation constraints of the virtual power plant and the equipment operation constraints, wherein the overall operation constraints of the virtual power plant include: day-ahead power market power balance constraints, reserve capacity constraints, upward adjustment The peak power constraint, the downward peak power constraint and the thermal power balance constraint are expressed as follows:

(1)日前电能量市场功率平衡约束被表示为如式(22)所示:(1) The power balance constraint of the day-ahead electric energy market is expressed as formula (22):

Figure BDA0003646925140000084
Figure BDA0003646925140000084

式中,

Figure BDA0003646925140000085
为上级电网下发的t时段EM电量指令;
Figure BDA0003646925140000086
分别为场景 s下t时段CHP机组和HFC电能量市场的功率;In the formula,
Figure BDA0003646925140000085
The EM power command issued by the upper-level power grid in the t period;
Figure BDA0003646925140000086
are the power of the CHP unit and the HFC power market in the t period of the scenario s, respectively;

(2)备用容量约束被表示为如式(23)所示:(2) The reserve capacity constraint is expressed as Eq. (23):

Figure BDA0003646925140000087
Figure BDA0003646925140000087

式中,

Figure BDA0003646925140000088
分别为场景s下t时段CHP机组和HFC在备用容量市场 的备用容量;In the formula,
Figure BDA0003646925140000088
are the spare capacity of CHP units and HFC in the spare capacity market in the period t under scenario s, respectively;

(3)向上、下调峰功率约束被表示为如式(24)所示:(3) The up and down peak power constraints are expressed as equation (24):

Figure BDA0003646925140000089
Figure BDA0003646925140000089

式中,

Figure BDA00036469251400000810
分别为上级电网下发的t时段向上向下调峰的指令功率;
Figure BDA00036469251400000811
分别为场景s下t时段CHP机组和HFC在灵活调峰 市场向上向下调峰的功率;In the formula,
Figure BDA00036469251400000810
are the command power for peaking up and down in t period issued by the upper-level power grid, respectively;
Figure BDA00036469251400000811
are the powers of CHP units and HFC in the flexible peak shaving market up and down in the t period under scenario s, respectively;

(5)热功率平衡约束被表示为如式(25)所示:(5) The thermal power balance constraint is expressed as Eq. (25):

Figure BDA0003646925140000091
Figure BDA0003646925140000091

式中,Ht为t时段虚拟电厂热负荷需求;

Figure BDA0003646925140000092
为场景s下t时段CHP机组的热 功率;
Figure BDA0003646925140000093
分别为场景s下t时段热储能的充、放热功率;In the formula, H t is the heat load demand of the virtual power plant in period t;
Figure BDA0003646925140000092
is the thermal power of the CHP unit in the t period under the scenario s;
Figure BDA0003646925140000093
are the charging and discharging powers of the thermal energy storage in the t period of the scene s, respectively;

所述设备运行约束包括CHP机组出力约束、电解槽出力及爬坡约束、燃料 电池运行及爬坡约束和储氢罐和热储能约束,分别表示为:The equipment operation constraints include CHP unit output constraints, electrolyzer output and ramp constraints, fuel cell operation and ramp constraints, and hydrogen storage tanks and thermal energy storage constraints, which are respectively expressed as:

(6))CHP机组出力约束(6)) Output constraints of CHP units

将CHP机组的运行区间限定为四边形ABCD的范围内,边界AD、AB、BC、CD 分别代表蒸汽喷射的最小极限、最大热率、燃料喷射的最大极限、输出电功率 的最大极限,定义转角点,即边界交点的电功率、热功率为(xk,yk);CHP机组的 电功率、热功率与边界交点坐标的关系被表示为如式(26)所示:The operating interval of the CHP unit is limited to the range of the quadrilateral ABCD, and the boundaries AD, AB, BC, and CD represent the minimum limit of steam injection, the maximum heat rate, the maximum limit of fuel injection, and the maximum limit of output electric power, respectively. Define the corner point, That is, the electrical power and thermal power of the boundary intersection point are (x k , y k ); the relationship between the electrical power and thermal power of the CHP unit and the coordinates of the boundary intersection point is expressed as formula (26):

Figure BDA0003646925140000094
Figure BDA0003646925140000094

式中,Mi为CHP机组的边界交点总数,组合系数满足如式(27)所示约束 方程:In the formula, M i is the total number of boundary intersection points of the CHP unit, and the combination coefficient satisfies the constraint equation shown in Eq. (27):

Figure BDA0003646925140000095
Figure BDA0003646925140000095

(7)电解槽出力及爬坡约束被表示为如式(28)、(29)所示:(7) The output of the electrolytic cell and the constraints of climbing are expressed as formulas (28) and (29):

Figure BDA0003646925140000096
Figure BDA0003646925140000096

Figure BDA0003646925140000097
Figure BDA0003646925140000097

式中,

Figure BDA0003646925140000098
分别为电解槽出力上、下限;RPtH为电解槽出力爬坡速率约 束;In the formula,
Figure BDA0003646925140000098
are the upper and lower limits of the output of the electrolytic cell, respectively; R PtH is the limit of the ramp rate of the output of the electrolytic cell;

(8)燃料电池运行及爬坡约束被表示为如式(30)、(31)、(32)所示:(8) The fuel cell operation and climbing constraints are expressed as equations (30), (31), (32):

Figure BDA0003646925140000101
Figure BDA0003646925140000101

Figure BDA0003646925140000102
Figure BDA0003646925140000102

Figure BDA0003646925140000103
Figure BDA0003646925140000103

式中,

Figure BDA0003646925140000104
分别为燃料电池出力上、下限;RHFC为燃料电池出力爬坡 速率约束;In the formula,
Figure BDA0003646925140000104
are the upper and lower limits of fuel cell output, respectively; R HFC is the fuel cell output ramp rate constraint;

(9)储氢罐和热储能约束被表示为如式(33)-(39)所示:(9) The hydrogen storage tank and thermal energy storage constraints are expressed as equations (33)-(39):

Figure BDA0003646925140000105
Figure BDA0003646925140000105

Figure BDA0003646925140000106
Figure BDA0003646925140000106

Figure BDA0003646925140000107
Figure BDA0003646925140000107

Figure BDA0003646925140000108
Figure BDA0003646925140000108

Figure BDA0003646925140000109
Figure BDA0003646925140000109

Figure BDA00036469251400001010
Figure BDA00036469251400001010

Figure BDA00036469251400001011
Figure BDA00036469251400001011

式中,

Figure BDA00036469251400001012
分别为储氢的上、下限;
Figure BDA00036469251400001013
分别为储氢量在一天的 始、末值。
Figure BDA00036469251400001014
分别为储、放热功率的最大值;布尔变量
Figure BDA00036469251400001015
分别 表示场景s下t时段储热装置是否储放热,是则置1,否则置0;
Figure BDA00036469251400001016
分别 为储热容量的上、下限;
Figure BDA00036469251400001017
分别为储热容量在一天的始、末值。In the formula,
Figure BDA00036469251400001012
are the upper and lower limits of hydrogen storage, respectively;
Figure BDA00036469251400001013
are the hydrogen storage capacity at the beginning and end of the day, respectively.
Figure BDA00036469251400001014
are the maximum values of storage and heat release power, respectively; Boolean variable
Figure BDA00036469251400001015
Respectively indicate whether the heat storage device stores and releases heat in the t period of the scene s, if it is, it is set to 1, otherwise it is set to 0;
Figure BDA00036469251400001016
are the upper and lower limits of the heat storage capacity, respectively;
Figure BDA00036469251400001017
are the beginning and end values of the heat storage capacity in a day, respectively.

优选地,所述虚拟电厂由1台CHP机组、1个风电场、1个光伏电站、1台 电解制氢装置,1台燃料电池,1个储氢罐和1个储热装置组成;所述电解制氢 装置的最大功率为5MW,爬坡率为1MW;所述燃料电池的最大功率为5MW,爬坡 率为2MW;所述储氢罐的最大容量为1000kg,最小容量为100kg,初始容量为500kg;所述储热装置的最大容量为10MW·h,最小容量为1MW·h,初始容量为 5MW·h,储放热效率为0.88。Preferably, the virtual power plant is composed of 1 CHP unit, 1 wind farm, 1 photovoltaic power station, 1 electrolysis hydrogen production device, 1 fuel cell, 1 hydrogen storage tank and 1 heat storage device; the The maximum power of the electrolytic hydrogen production device is 5MW, and the ramp rate is 1MW; the maximum power of the fuel cell is 5MW, and the ramp rate is 2MW; the maximum capacity of the hydrogen storage tank is 1000kg, the minimum capacity is 100kg, and the initial capacity is 1000kg. The maximum capacity of the heat storage device is 10MW·h, the minimum capacity is 1MW·h, the initial capacity is 5MW·h, and the heat storage and release efficiency is 0.88.

附图说明Description of drawings

为了更清楚地说明本发明的技术方案,下面将对实施方式中所需要使用的 附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施 方式,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以 根据这些附图获得其他的附图。In order to illustrate the technical solutions of the present invention more clearly, the following will briefly introduce the accompanying drawings used in the embodiments. Obviously, the drawings in the following description are only some embodiments of the present invention, which are common in the art. As far as technical personnel are concerned, other drawings can also be obtained based on these drawings without any creative effort.

图1是本发明提供的虚拟电厂系统构成图;Fig. 1 is a virtual power plant system composition diagram provided by the present invention;

图2是本发明提供的氢燃料汽车运行路线图;Fig. 2 is the hydrogen fuel vehicle operation route map provided by the present invention;

图3是本发明提供的CHP机组运行区间图;Fig. 3 is the operation interval diagram of CHP unit provided by the present invention;

图4是本发明提供的HV的氢负荷预测情况图;Fig. 4 is the hydrogen load prediction situation diagram of HV provided by the present invention;

图5本发明提供的夏季典型日能量市场、旋转备用市场和调峰市场电价值;Fig. 5 typical summer day energy market, rotating reserve market and peak shaving market electricity value provided by the present invention;

图6本发明提供的冬季典型日能量市场、旋转备用市场和调峰市场电价值;Fig. 6 typical daily energy market, rotating reserve market and peak shaving market electricity value provided by the present invention;

图7本发明提供的风电与光伏预测功率图;Fig. 7 wind power and photovoltaic forecast power diagram provided by the present invention;

图8本发明提供的调度指令、热负荷图;Fig. 8 scheduling instruction and heat load diagram provided by the present invention;

图9本发明提供的夏季典型日虚拟电厂优化情况图;Fig. 9 is a typical summer day virtual power plant optimization situation diagram provided by the present invention;

图10发明提供的冬季典型日虚拟电厂优化情况图;Figure 10 is a diagram of the optimization situation of a virtual power plant on a typical day in winter provided by the invention;

具体实施方式:Detailed ways:

下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清 楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是 全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造 性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

本领域技术人员应当理解,文中所使用的步骤编号仅是为了方便描述,不 对作为对步骤执行先后顺序的限定。在本发明说明书中所使用的术语仅仅是出 于描述特定实施例的目的而并不意在限制本发明。如在本发明说明书和所附权 利要求书中所使用的那样,除非上下文清楚地指明其它情况,否则单数形式的 “一”、“一个”及“该”意在包括复数形式。术语“包括”和“包含”指示所 描述特征、整体、步骤、操作、元素和/或组件的存在,但并不排除一个或多个 其它特征、整体、步骤、操作、元素、组件和/或其集合的存在或添加。术语“和 /或”是指相关联列出的项中的一个或多个的任何组合以及所有可能组合,并且 包括这些组合。It should be understood by those skilled in the art that the step numbers used in the text are only for the convenience of description, and are not intended to limit the order of execution of the steps. The terms used in the present specification are for the purpose of describing particular embodiments only and are not intended to limit the present invention. As used in this specification and the appended claims, the singular forms "a," "an," and "the" are intended to include the plural unless the context clearly dictates otherwise. The terms "comprising" and "comprising" indicate the presence of the described features, integers, steps, operations, elements and/or components, but do not exclude one or more other features, integers, steps, operations, elements, components and/or the existence or addition of its collection. The term "and/or" refers to and including any and all possible combinations of one or more of the associated listed items.

本发明提供了一种考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法,具 体包括以下步骤:The present invention provides a virtual power plant coordination scheduling method considering hydrogen fuel vehicles and hydrogen energy storage, which specifically includes the following steps:

S101构建考虑路网的氢能源汽车负荷预测模型,具体包括:S101 Build a hydrogen energy vehicle load prediction model considering the road network, including:

(1)计算氢燃料汽车到达加氢地点的时间:(1) Calculate the time for the hydrogen fuel vehicle to arrive at the hydrogenation site:

对于HV,假设它们由聚合器控制。加氢站位于HV线路起始站点,当车辆n 跑完第k次循环返回起始站点,聚合器获取其到达时间

Figure BDA0003646925140000121
和剩余燃料量
Figure BDA0003646925140000122
其 计算方法为:For HVs, they are assumed to be controlled by the aggregator. The hydrogen refueling station is located at the starting station of the HV line. When the vehicle n returns to the starting station after the k-th cycle, the aggregator obtains its arrival time
Figure BDA0003646925140000121
and remaining fuel
Figure BDA0003646925140000122
Its calculation method is:

Figure BDA0003646925140000123
Figure BDA0003646925140000123

Figure BDA0003646925140000124
Figure BDA0003646925140000124

Figure BDA0003646925140000125
Figure BDA0003646925140000125

其中,vt为t时段道路i的汽车平均行驶速度,与道路等级、时间及道路车流 量等因素密切相关;α1、α2、α3和β为回归参数与修正系数,随道路等级变化; v0为各等级道路的设计车速;Ft为t时段道路的车流量;F0为为道路的设计通行 车流量;D为车辆行驶过程中途径公交站点数量;

Figure BDA0003646925140000126
为车辆初始时间;Di,d为 途中第(d-1)个站点至第d个站点的道路距离;△td-1为在第(d-1)个站点停车等待 的时间;
Figure BDA0003646925140000127
为车辆n初始燃料量,采用蒙特卡洛模拟进行仿真,生成初始燃料 随机数;l为车辆路线的距离;△m为HV每公里氢耗量;η为汽车非正常行驶状 态下的能耗系数,包括启动加速以及刹车期间发动机所需的负荷功导致的能量 损失。Among them, v t is the average speed of vehicles on road i in period t, which is closely related to factors such as road grade, time, and road traffic flow; α 1 , α 2 , α 3 and β are regression parameters and correction coefficients, which change with the road grade ; v 0 is the design speed of each grade of road; F t is the traffic flow of the road in the t period; F 0 is the design traffic flow of the road; D is the number of bus stops in the process of vehicle driving;
Figure BDA0003646925140000126
is the initial time of the vehicle; D i,d is the road distance from the (d-1)th station to the dth station on the way; △t d-1 is the waiting time at the (d-1)th station;
Figure BDA0003646925140000127
is the initial fuel quantity of vehicle n, which is simulated by Monte Carlo simulation to generate initial fuel random numbers; l is the distance of the vehicle route; △m is the hydrogen consumption per kilometer of the HV; η is the energy consumption coefficient of the vehicle in abnormal driving state , including the energy loss due to the load work required by the engine during start-up acceleration and braking.

(2)计算氢燃料汽车氢负荷需求总量:(2) Calculate the total demand for hydrogen load of hydrogen fuel vehicles:

当剩余燃料小于一定值时,则在到达加氢站后进行加氢,HV加氢状态判断 如下式所示:When the remaining fuel is less than a certain value, hydrogenation is carried out after arriving at the hydrogenation station, and the judgment of the HV hydrogenation state is shown in the following formula:

Figure BDA0003646925140000131
Figure BDA0003646925140000131

Figure BDA0003646925140000132
Figure BDA0003646925140000132

其中,mset为HV的燃料阈值;

Figure BDA0003646925140000133
表示第n辆HV在第k次循环结束的t时段 需要加氢;
Figure BDA0003646925140000134
为t时段氢燃料汽车的燃料需求总量;N为氢燃料汽车的数量;
Figure BDA0003646925140000135
为氢燃料汽车的储氢瓶含量。Among them, mset is the fuel threshold of HV;
Figure BDA0003646925140000133
Indicates that the nth HV needs to be hydrogenated in the period t at the end of the kth cycle;
Figure BDA0003646925140000134
is the total fuel demand of hydrogen fuel vehicles in period t; N is the number of hydrogen fuel vehicles;
Figure BDA0003646925140000135
The content of hydrogen storage tanks for hydrogen fuel vehicles.

S102构建氢储能系统模型,具体内容包括:S102 Build a hydrogen energy storage system model, the specific contents include:

(1)电解槽模型(1) Electrolyzer Model

电解槽的产氢气速率和电解槽的耗电功率近似成线性关系,设定电解槽单 位电量产氢率为ηPtH,则电解槽t时段的产氢气量

Figure BDA0003646925140000136
可表示为产氢率ηPtH和输入 电功率
Figure BDA0003646925140000137
的乘积:The hydrogen production rate of the electrolytic cell and the power consumption of the electrolytic cell are approximately in a linear relationship. If the hydrogen production rate per unit of electricity of the electrolytic cell is η PtH , the hydrogen production rate of the electrolytic cell in the period t is
Figure BDA0003646925140000136
It can be expressed as hydrogen production rate η PtH and input electric power
Figure BDA0003646925140000137
The product of :

Figure BDA0003646925140000138
Figure BDA0003646925140000138

(2)氢燃料电池模型(2) Hydrogen fuel cell model

在外界因素已知时,氢燃料电池的发电和产热功率分别受消耗氢气量

Figure BDA0003646925140000139
和 氢燃料电池温度THFC决定。则氢燃料电池的模型为:When the external factors are known, the power generation and heat generation power of the hydrogen fuel cell are respectively affected by the consumption of hydrogen
Figure BDA0003646925140000139
and the hydrogen fuel cell temperature T HFC is determined. Then the model of the hydrogen fuel cell is:

Figure BDA00036469251400001310
Figure BDA00036469251400001310

其中,Ener为能斯特电压;ηact、ηohm、ηcon分别为活化极化、欧姆和浓差损耗; F、MH2分别为法拉第常数和氢气摩尔质量;ηHFCh为氢燃料电池的产热效率;

Figure BDA0003646925140000141
为总功率。Among them, E ner is the Nernst voltage; η act , η ohm , and η con are activation polarization, ohmic and concentration loss, respectively; F, M H2 are the Faraday constant and hydrogen molar mass, respectively; η HFCh is the hydrogen fuel cell heat production efficiency;
Figure BDA0003646925140000141
is the total power.

(3)储氢罐模型(3) Hydrogen storage tank model

储氢罐储存电解槽生成的氢气,可为氢燃料电池提供氢气、给氢燃料汽车 补充燃料并向市场出售氢气获得利润。储氢罐中的氢气质量为:The hydrogen storage tank stores the hydrogen generated by the electrolyzer, which can provide hydrogen for hydrogen fuel cells, refuel hydrogen vehicles, and sell hydrogen to the market for profit. The mass of hydrogen in the hydrogen storage tank is:

Figure BDA0003646925140000142
Figure BDA0003646925140000142

其中,

Figure BDA0003646925140000143
为t时段储氢罐中氢气的质量;
Figure BDA0003646925140000144
为t时段电解槽的产氢量;
Figure BDA0003646925140000145
为t时段氢燃料电池的耗氢量;
Figure BDA0003646925140000146
为t时段HV的氢气需求量。in,
Figure BDA0003646925140000143
is the mass of hydrogen in the hydrogen storage tank at time t;
Figure BDA0003646925140000144
is the hydrogen production of the electrolyzer in period t;
Figure BDA0003646925140000145
is the hydrogen consumption of the hydrogen fuel cell in period t;
Figure BDA0003646925140000146
is the hydrogen demand of HV in period t.

(4)氢储能系统模型(4) Hydrogen energy storage system model

氢储能系统整体的模型为:The overall model of the hydrogen energy storage system is:

Figure BDA0003646925140000147
Figure BDA0003646925140000147

Figure BDA0003646925140000148
Figure BDA0003646925140000148

Figure BDA0003646925140000149
Figure BDA0003646925140000149

式中:

Figure BDA00036469251400001410
为氢储能系统整体的输出功率;布尔变量
Figure BDA00036469251400001411
分别表示t时段 氢储能电解槽和氢燃料电池工作状态。where:
Figure BDA00036469251400001410
is the overall output power of the hydrogen energy storage system; Boolean variable
Figure BDA00036469251400001411
respectively represent the working states of the hydrogen energy storage electrolyzer and the hydrogen fuel cell in the t period.

S103基于场景法对电网内风光出力的不确定性进行处理,包括场景生成和 场景削减两部分。S103 processes the uncertainty of wind and solar output in the power grid based on the scene method, including scene generation and scene reduction.

基于自回归滑动平均模型进行场景生成,构建包含风光出力的大量预测场 景,描述风光出力不确定性,具体内容包括:Based on the autoregressive moving average model, the scene is generated, and a large number of forecasting scenarios including the wind and light output are constructed to describe the uncertainty of the wind and light output. The specific contents include:

确定基于均值和标准差的白噪声,即滑动回归平均参数;Determine the white noise based on the mean and standard deviation, that is, the sliding regression mean parameter;

基于基准预测数据,本着残差方差最小原则,生成负荷风电出力各1000个 场景数据;Based on the benchmark forecast data, and in line with the principle of minimum residual variance, generate 1,000 scenario data for each load wind power output;

进一步地,基于改进k-means聚类算法,对风光出力进行聚类,生成若干 个典型运行场景,具体内容包括:Further, based on the improved k-means clustering algorithm, the wind and solar output is clustered to generate several typical operating scenarios, the specific contents include:

基于局部密度均值聚类算法寻找初始的数据聚类中心;Find the initial data cluster center based on the local density mean clustering algorithm;

基于初始聚类中心,采用k-means聚类算法生成典型运行场景。Based on the initial cluster centers, k-means clustering algorithm is used to generate typical operating scenarios.

S104建立优化调度模型的目标函数和约束条件。S104 establishes the objective function and constraints of the optimal scheduling model.

具体的,建立虚拟电厂协调调度优化目标模型:Specifically, establish a virtual power plant coordination scheduling optimization objective model:

Figure BDA0003646925140000151
Figure BDA0003646925140000151

其中,Is,i(X0)、Cs,i(X0)分别为场景s下各项运行收益和成本指标函数,X0为 优化变量。各项含义如下:Among them, Is ,i (X 0 ) and C s,i (X 0 ) are the index functions of various operating benefits and costs under the scenario s, respectively, and X 0 is the optimization variable. The meanings of each are as follows:

(1)场景s下虚拟电厂参与日前能量市场、旋转备用和调峰市场的售电总收 益:(1) Under scenario s, the total revenue from electricity sales of virtual power plants participating in the day-ahead energy market, rotating reserve and peak shaving market:

Figure BDA0003646925140000152
Figure BDA0003646925140000152

其中,

Figure BDA0003646925140000153
表示t时段的日前电能量市场电价;
Figure BDA0003646925140000154
表示t时段的备用容量市 场电价;
Figure BDA0003646925140000155
Figure BDA0003646925140000156
分别表示t时段的向上调峰和向下调峰电价;
Figure BDA0003646925140000157
Figure BDA0003646925140000158
分别表示场景s下t时段虚拟电厂的日前电能量出力、备用出力和向上向下调 峰;
Figure BDA0003646925140000159
表示场景s下t时段虚拟电厂的热出力。
Figure BDA00036469251400001510
分别表示t时 段的EM、SRM、向上调峰和向下调峰电价;
Figure BDA00036469251400001511
分别为场景s下t时段风、 光、电解槽实际出力;
Figure BDA00036469251400001512
分别为CHP机组和HFC参与EM、SRM和向上、向下调峰市场的出力。in,
Figure BDA0003646925140000153
Indicates the day-ahead electricity market electricity price in period t;
Figure BDA0003646925140000154
represents the market electricity price of reserve capacity in period t;
Figure BDA0003646925140000155
and
Figure BDA0003646925140000156
Respectively represent the up-peak and down-peak electricity prices in the t period;
Figure BDA0003646925140000157
and
Figure BDA0003646925140000158
Respectively represent the day-ahead power output, standby output and peak-down peaking of the virtual power plant in the period t under the scenario s;
Figure BDA0003646925140000159
Indicates the heat output of the virtual power plant in the t period under the scenario s.
Figure BDA00036469251400001510
Respectively represent the EM, SRM, peak-up and down-peak electricity prices in t period;
Figure BDA00036469251400001511
are the actual output of wind, light, and electrolytic cell in time period t under scene s, respectively;
Figure BDA00036469251400001512
It is the output of CHP unit and HFC participating in EM, SRM and up and down peaking market respectively.

(2)场景s下虚拟电厂供热的收益:(2) The benefits of virtual power plant heating under scenario s:

Figure BDA00036469251400001513
Figure BDA00036469251400001513

其中,

Figure BDA00036469251400001514
分别为CHP机组、HFC和热储能储、放的热 功率。in,
Figure BDA00036469251400001514
are the thermal power of CHP unit, HFC and thermal energy storage and discharge, respectively.

(3)场景s下虚拟电厂出售氢气的收益:(3) Revenue from the sale of hydrogen by the virtual power plant in scenario s:

Figure BDA0003646925140000161
Figure BDA0003646925140000161

其中,

Figure BDA0003646925140000162
表示氢气价格。in,
Figure BDA0003646925140000162
Indicates the hydrogen price.

(4)虚拟电厂可通过出售未达到碳排放配额的排放额度取得收益。反之,当 净排放量超过碳排放配额时,需支付碳交易费用于购买排放配额。碳交易收益 表达如下:(4) Virtual power plants can make profits by selling the emission credits that do not meet the carbon emission quotas. Conversely, when net emissions exceed carbon emission allowances, carbon transaction fees are required to purchase emission allowances. The carbon trading income is expressed as follows:

Figure BDA0003646925140000163
Figure BDA0003646925140000163

其中,CCM为碳交易价格;

Figure BDA0003646925140000164
为场景s下t时段虚拟电厂的碳排放配额;γe、 γh分别为CHP机组的供电基准值和供热基准值;Fr为机组供热量修正系数。Among them, C CM is the carbon trading price;
Figure BDA0003646925140000164
is the carbon emission quota of the virtual power plant in the t period under the scenario s; γ e and γ h are the reference value of power supply and the reference value of heat supply of the CHP unit, respectively; F r is the correction coefficient of heat supply of the unit.

(5)场景s下风光发电的运行维护成本为:(5) The operation and maintenance cost of wind and solar power generation in scenario s is:

Figure BDA0003646925140000165
Figure BDA0003646925140000165

其中,kW、kPV分别为风光发电的单位运行维护成本;

Figure BDA0003646925140000166
分别为场景s 下t时段风、光实际出力。Among them, k W and k PV are the unit operation and maintenance costs of wind and solar power generation respectively;
Figure BDA0003646925140000166
are the actual output of wind and light in time period t under scene s, respectively.

(6)场景s下虚拟电厂与调度指令偏差的惩罚成本::(6) The penalty cost of the deviation between the virtual power plant and the dispatch instruction in the scenario s:

Figure BDA0003646925140000167
Figure BDA0003646925140000167

其中,

Figure BDA0003646925140000168
表示场景s下t时段EM、向上向下调峰的偏差量;γem、γru、γrd分别为EM、向上向下调峰的惩罚系数。in,
Figure BDA0003646925140000168
Represents the deviation of EM, up and down peaks in the t period of scene s; γ em , γ ru , and γ rd are the penalty coefficients of EM, up and down peaks, respectively.

(7)场景s下CHP机组的成本,主要是天然气的燃料成本。其成本表达式如 下:(7) The cost of CHP units in scenario s is mainly the fuel cost of natural gas. Its cost expression is as follows:

Figure BDA0003646925140000169
Figure BDA0003646925140000169

其中,α0、α1、α2、α3、α4、α5为CHP机组能耗系数;

Figure BDA0003646925140000171
表示CHP机组 的电出力。Among them, α 0 , α 1 , α 2 , α 3 , α 4 , α 5 are the energy consumption coefficients of CHP units;
Figure BDA0003646925140000171
Indicates the electrical output of the CHP unit.

(8)氢储能的成本包括电解槽、燃料电池和储氢罐的平均投资成本和运维成 本,其成本表达式如下:(8) The cost of hydrogen energy storage includes the average investment cost and operation and maintenance cost of electrolyzers, fuel cells and hydrogen storage tanks. The cost expression is as follows:

Figure BDA0003646925140000172
Figure BDA0003646925140000172

其中,

Figure BDA0003646925140000173
表示场景s下t时段电解槽、HFC、储氢罐的运行维护 成本;λPtH、λHFC、λHS分别为电解槽、HFC和储氢罐的单位运行维护成本;
Figure BDA0003646925140000174
为 场景s下t时段储氢罐储氢质量。in,
Figure BDA0003646925140000173
represents the operation and maintenance costs of the electrolyzer, HFC, and hydrogen storage tank in the t period of the scenario s; λ PtH , λ HFC , and λ HS are the unit operation and maintenance costs of the electrolyzer, HFC and hydrogen storage tank, respectively;
Figure BDA0003646925140000174
is the hydrogen storage quality of the hydrogen storage tank in the t period of the scenario s.

所述目标函数采用系统运行集约束,包括虚拟电厂整体运行约束和设备运 行约束。The objective function adopts system operation set constraints, including the overall operation constraints of the virtual power plant and equipment operation constraints.

系统运行集约束包括虚拟电厂整体运行约束和设备运行约束。虚拟电厂整 体运行约束包括:日前电能量市场功率平衡约束、备用容量约束、向上调峰功 率约束、向下调峰功率约束、热功率平衡约束。The system operating set constraints include the overall virtual power plant operating constraints and equipment operating constraints. The overall operation constraints of the virtual power plant include: day-ahead power market power balance constraints, reserve capacity constraints, up-peak power constraints, down-peak power constraints, and thermal power balance constraints.

(1)日前电能量市场功率平衡约束(1) The power balance constraint of the day-ahead electric energy market

Figure BDA0003646925140000175
Figure BDA0003646925140000175

式中,

Figure BDA0003646925140000176
为上级电网下发的t时段EM电量指令;
Figure BDA0003646925140000177
分别为场景 s下t时段CHP机组和HFC电能量市场的功率。In the formula,
Figure BDA0003646925140000176
The EM power command issued by the upper-level power grid in the t period;
Figure BDA0003646925140000177
are the power of the CHP unit and the HFC power market in the t period under the scenario s, respectively.

(2)备用容量约束(2) Reserve capacity constraints

Figure BDA0003646925140000178
Figure BDA0003646925140000178

式中,

Figure BDA0003646925140000179
分别为场景s下t时段CHP机组和HFC在备用容量市场 的备用容量。In the formula,
Figure BDA0003646925140000179
are the spare capacity of CHP units and HFC in the spare capacity market in the t period under scenario s, respectively.

(3)向上、下调峰功率约束(3) Up and down peak power constraints

Figure BDA0003646925140000181
Figure BDA0003646925140000181

式中,

Figure BDA0003646925140000182
分别为上级电网下发的t时段向上向下调峰的指令功率;
Figure BDA0003646925140000183
分别为场景s下t时段CHP机组和HFC在灵活调峰 市场向上向下调峰的功率。In the formula,
Figure BDA0003646925140000182
are the command power for peaking up and down in t period issued by the upper-level power grid, respectively;
Figure BDA0003646925140000183
are the peaking power of CHP units and HFC in the flexible peaking market during t period under scenario s, respectively.

(5)热功率平衡约束(5) Thermal power balance constraints

Figure BDA0003646925140000184
Figure BDA0003646925140000184

式中,Ht为t时段虚拟电厂热负荷需求;

Figure BDA0003646925140000185
为场景s下t时段CHP机组的热 功率;
Figure BDA0003646925140000186
分别为场景s下t时段热储能的充、放热功率。In the formula, H t is the heat load demand of the virtual power plant in period t;
Figure BDA0003646925140000185
is the thermal power of the CHP unit in the t period under the scenario s;
Figure BDA0003646925140000186
are the charging and discharging powers of the thermal energy storage in the t period under the scenario s, respectively.

设备运行约束为:The device operating constraints are:

(6)CHP机组出力约束(6) Output constraints of CHP units

CHP机组的运行区间如图3示。边界AD、AB、BC、CD分别代表蒸汽喷射的 最小极限、最大热率、燃料喷射的最大极限、输出电功率的最大极限。定义转 角点(边界交点)的电功率、热功率为(xk,yk)。The operating range of the CHP unit is shown in Figure 3. The boundaries AD, AB, BC, and CD represent the minimum limit of steam injection, the maximum heat rate, the maximum limit of fuel injection, and the maximum limit of output electric power, respectively. Define the electric power and thermal power of the corner point (boundary intersection) as (x k , y k ).

CHP机组的热、电耦合,这些参数必须保持在可行的运行区间内。由于区域 内任意点都可以用边界交点的凸组合表示,因此,电功率、热功率与边界交点 坐标的关系表示为:Thermal and electrical coupling of CHP units, these parameters must be maintained within the feasible operating range. Since any point in the region can be represented by a convex combination of boundary intersections, the relationship between electrical power, thermal power and the coordinates of boundary intersections is expressed as:

Figure BDA0003646925140000187
Figure BDA0003646925140000187

式中,Mi为CHP机组的边界交点总数,组合系数满足如下方程:In the formula, M i is the total number of boundary intersection points of CHP units, and the combination coefficient satisfies the following equation:

Figure BDA0003646925140000188
Figure BDA0003646925140000188

(7)电解槽出力及爬坡约束(7) The output of the electrolytic cell and the restriction of climbing

Figure BDA0003646925140000191
Figure BDA0003646925140000191

Figure BDA0003646925140000192
Figure BDA0003646925140000192

式中,

Figure BDA0003646925140000193
分别为电解槽出力上、下限;RPtH为电解槽出力爬坡速率约 束。In the formula,
Figure BDA0003646925140000193
are the upper and lower limits of the output of the electrolytic cell, respectively; R PtH is the limit of the ramp rate of the output of the electrolytic cell.

(8)燃料电池运行及爬坡约束(8) Fuel cell operation and climbing constraints

Figure BDA0003646925140000194
Figure BDA0003646925140000194

Figure BDA0003646925140000195
Figure BDA0003646925140000195

Figure BDA0003646925140000196
Figure BDA0003646925140000196

式中,

Figure BDA0003646925140000197
分别为燃料电池出力上、下限;RHFC为燃料电池出力爬坡 速率约束。In the formula,
Figure BDA0003646925140000197
are the upper and lower limits of the fuel cell output, respectively; R HFC is the fuel cell output ramp rate constraint.

(9)储氢罐和热储能约束(9) Hydrogen storage tank and thermal energy storage constraints

Figure BDA0003646925140000198
Figure BDA0003646925140000198

Figure BDA0003646925140000199
Figure BDA0003646925140000199

Figure BDA00036469251400001910
Figure BDA00036469251400001910

Figure BDA00036469251400001911
Figure BDA00036469251400001911

Figure BDA00036469251400001912
Figure BDA00036469251400001912

Figure BDA00036469251400001913
Figure BDA00036469251400001913

Figure BDA00036469251400001914
Figure BDA00036469251400001914

式中,

Figure BDA00036469251400001915
分别为储氢的上、下限;
Figure BDA00036469251400001916
分别为储氢量在一天的 始、末值。
Figure BDA00036469251400001917
分别为储、放热功率的最大值;布尔变量
Figure BDA00036469251400001918
分别 表示场景s下t时段储热装置是否储放热,是则置1,否则置0;
Figure BDA00036469251400001919
分别 为储热容量的上、下限;
Figure BDA00036469251400001920
分别为储热容量在一天的始、末值。In the formula,
Figure BDA00036469251400001915
are the upper and lower limits of hydrogen storage, respectively;
Figure BDA00036469251400001916
are the hydrogen storage capacity at the beginning and end of the day, respectively.
Figure BDA00036469251400001917
are the maximum values of storage and heat release power, respectively; Boolean variable
Figure BDA00036469251400001918
Respectively indicate whether the heat storage device stores and releases heat in the t period of the scene s, if it is, it is set to 1, otherwise it is set to 0;
Figure BDA00036469251400001919
are the upper and lower limits of the heat storage capacity, respectively;
Figure BDA00036469251400001920
are the beginning and end values of the heat storage capacity in a day, respectively.

S105、加氢站为50辆HV提供加氢服务,其所需氢气由氢储能提供。路线 的参数见表1所示;HV所需的氢燃料预测见图4。S105. The hydrogen refueling station provides hydrogen refueling services for 50 HVs, and the required hydrogen is provided by hydrogen energy storage. The parameters of the route are shown in Table 1; the predicted hydrogen fuel required by HV is shown in Figure 4.

表1 HV和路线的参数Table 1 Parameters of HV and route

Figure BDA0003646925140000201
Figure BDA0003646925140000201

虚拟电厂由1台CHP机组,1个风电场,1个光伏电站,1台电解制氢装置, 1台燃料电池,1个储氢罐和1个储热装置组成。电解制氢装置的最大功率为5MW, 爬坡率为1MW;燃料电池的最大功率为5MW,爬坡率为2MW;储氢罐的最大容量 为1000kg,最小容量为100kg,初始容量为500kg;储热装置的最大容量为10MW·h, 最小容量为1MW·h,初始容量为5MW·h,储放热效率为0.88;热价为90元/MW·h; 氢气价格为50元/kg;夏季和冬季典型日能量市场、旋转备用市场和调峰市场 电价预测值见图5和图6;风电与光伏预测功率见图7;上级调度指令和虚拟电 厂热需求见图8;把一天按小时为单位划分,T=24。相关计算均在英特尔酷睿 i5-7400处理器3.00GHz,8GB内存计算机上完成,采用MATLAB对算例进行编程 求解。The virtual power plant consists of 1 CHP unit, 1 wind farm, 1 photovoltaic power station, 1 electrolysis hydrogen production device, 1 fuel cell, 1 hydrogen storage tank and 1 heat storage device. The maximum power of the electrolysis hydrogen production device is 5MW, and the ramp rate is 1MW; the maximum power of the fuel cell is 5MW, and the ramp rate is 2MW; the maximum capacity of the hydrogen storage tank is 1000kg, the minimum capacity is 100kg, and the initial capacity is 500kg; The maximum capacity of the thermal device is 10MW·h, the minimum capacity is 1MW·h, the initial capacity is 5MW·h, and the heat storage and release efficiency is 0.88; the heat price is 90 yuan/MW·h; the hydrogen price is 50 yuan/kg; Typical daily energy market, rotating reserve market and peak shaving market electricity price forecast values in winter are shown in Figure 5 and Figure 6; wind power and photovoltaic forecast power is shown in Figure 7; superior dispatch instructions and virtual power plant heat demand are shown in Figure 8; Divide, T=24. All relevant calculations were completed on an Intel Core i5-7400 processor 3.00GHz, 8GB memory computer, and MATLAB was used to program and solve the calculation example.

为对比分析本发明实施例所引入评估方法模型的有效性与正确性,对比方 案如表2所示:For comparative analysis of the validity and correctness of the evaluation method model introduced in the embodiment of the present invention, the comparative scheme is as shown in Table 2:

表2 3种对比方案Table 2 Three comparison schemes

Figure BDA0003646925140000202
Figure BDA0003646925140000202

采用上述3种方案构建夏季和冬季典型日VPP调度优化模型,所得收益和成本 情况对比和调度情况结果对比的结果分别如表3、表4所示。The above three schemes are used to build the VPP scheduling optimization model for typical days in summer and winter.

表3 3种方案收益和成本结果对比Table 3 Comparison of benefits and cost results of the three schemes

Figure BDA0003646925140000211
Figure BDA0003646925140000211

表4 3种方案调度结果对比Table 4 Comparison of scheduling results of three schemes

Figure BDA0003646925140000212
Figure BDA0003646925140000212

相比于未考虑氢储能和未参与调峰市场的方案1和2,方案3不仅可利用氢 储能设备制备氢气,在负荷高峰时段发电、供热给用户从而减少与调度指令的 偏差,减少指令偏差惩罚,通过向HV供给燃料来提高收益,还通过参与调峰市 场增加调峰收益。Compared with Schemes 1 and 2, which do not consider hydrogen energy storage and do not participate in the peak shaving market, Scheme 3 can not only use hydrogen energy storage equipment to prepare hydrogen, generate electricity and supply heat to users during peak load hours, thereby reducing the deviation from dispatching instructions. Reduce command deviation penalties, increase revenue by supplying fuel to HVs, and increase peak shaving revenue by participating in the peak shaving market.

(1)夏季典型日虚拟电厂调度优化情况(1) Scheduling optimization of virtual power plants on typical days in summer

以夏季典型日的风光出力生成场景集,代入模型进行优化调度。夏季典型日 虚拟电厂的调度优化情况如图9所示。A scene set is generated based on the scenery output of a typical day in summer, and is substituted into the model for optimal scheduling. The scheduling optimization of virtual power plants on typical days in summer is shown in Figure 9.

采用夏季典型日的风光出力预测值生成场景集,VPP的优化调度结果如图9 所示。在1-7时段,由于调度指令量较低,此时电解槽运行并制备氢气;在8-13 时段,随着调度指令量的增加,此时电解槽停止运行,HFC从9时开始出力供电, 同时VPP在10时开始出现调度指令的偏差量;在14-18时段,随着调度指令量 降低,此时HFC停止工作,启动电解槽;在19-21时段,晚高峰导致调度指令 量增加,HFC在19-20时段工作,此时电解槽停止运行以满足负荷需求;在22-24 时段,调度指令减少,HFC停止工作,电解槽启动。The scenario set is generated by using the forecast value of wind and solar output on a typical day in summer. The optimal scheduling result of VPP is shown in Figure 9. In the period 1-7, due to the low amount of dispatching instructions, the electrolyzer runs and produces hydrogen; in the period 8-13, with the increase in the amount of dispatching instructions, the electrolyzer stops running at this time, and the HFC starts to supply power from 9:00 , At the same time, VPP began to show the deviation of scheduling instructions at 10:00; in the period of 14-18, as the amount of scheduling instructions decreased, the HFC stopped working at this time and started the electrolyzer; in the period of 19-21, the evening peak led to an increase in the amount of scheduling instructions , HFC works in the period of 19-20, at this time, the electrolytic cell stops running to meet the load demand; in the period of 22-24, the dispatching instruction decreases, the HFC stops working, and the electrolytic cell starts.

(2)冬季典型日虚拟电厂调度优化情况(2) Scheduling optimization of virtual power plants on typical days in winter

冬季典型日虚拟电厂的调度优化情况如图10所示。The scheduling optimization of the virtual power plant on a typical day in winter is shown in Figure 10.

冬季典型日VPP的优化调度结果如图10所示。由于冬季典型日市场电价和 调度指令与夏季典型日场景差异较大,因此优化结果也相差很大,其中冬季典 型日VPP热负荷大幅增加,因此CHP机组热出力大幅增加。由于电网调度指令 减少,HFC供电量相比于夏季典型日有所降低,在10-13时段出力供电,电解槽 在1-7时段、15-18时段和21-24时段运行,此外,冬季典型日不存在指令偏差。 本发明考虑氢燃料汽车与氢储能联合运行,并将其引入到虚拟电厂中进行协调 调度,从而建立考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法,并对各项 收益和成本指标建立数学计算模型,通过场景法生成风光典型出力场景集来考 虑风光出力不确定性,以虚拟电厂次日实际运行时的期望经济效益最大化为目 标函数,决策变量包括CHP机组电功率和热功率、电解槽功率、燃料电池电功 率和热功率、热储能储放热功率和储氢罐储放氢气质量等。并对是否加入氢储 能设备和是否参与调峰市场进行对比分析,保证了方案的可靠性和最优性。The optimal scheduling results of VPP on typical days in winter are shown in Figure 10. Since the market electricity price and dispatching instructions on a typical day in winter are quite different from those in a typical day in summer, the optimization results are also quite different. Among them, the VPP heat load on a typical day in winter increases significantly, so the heat output of the CHP unit increases significantly. Due to the reduction of power grid dispatch instructions, the power supply of HFC is lower than that of typical days in summer. The power supply is supplied during the period of 10-13, and the electrolyzer operates in the period of 1-7, 15-18 and 21-24. There is no command deviation on the day. The invention considers the joint operation of hydrogen fuel vehicles and hydrogen energy storage, and introduces them into virtual power plants for coordinated scheduling, so as to establish a virtual power plant coordination scheduling method considering hydrogen fuel vehicles and hydrogen energy storage, and provides various benefits and cost indicators. A mathematical calculation model is established, and a typical wind and solar output scene set is generated by the scenario method to consider the uncertainty of wind and solar output. The objective function is to maximize the expected economic benefits of the virtual power plant in the actual operation of the next day. The decision variables include the electrical power and thermal power of the CHP unit, Electrolyzer power, fuel cell electrical power and thermal power, thermal energy storage and release heat power, and hydrogen storage tank quality, etc. A comparative analysis of whether to add hydrogen energy storage equipment and whether to participate in the peak shaving market ensures the reliability and optimality of the plan.

以上所述是本发明的优选实施方式,应当指出,对于本技术领域的普通技 术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这 些改进和润饰也视为本发明的保护范围。The above are the preferred embodiments of the present invention. It should be pointed out that for those skilled in the art, without departing from the principles of the present invention, several improvements and modifications can be made, and these improvements and modifications may also be regarded as It is the protection scope of the present invention.

Claims (7)

1.一种考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法,所述虚拟电厂包括风电机组、光伏电站、CHP机组、氢储能系统、热储能单元,所述氢储能系统包括电解槽、HFC和储氢罐,其中,风电机组、光伏电站、CHP机组和外接电网共同为氢储能系统提供电解水制氢的电能和向外界支持电负荷IL,外部的天然气市场为CHP机组提供燃料,氢储能系统向外支持氢负荷;HFC、CHP机组和热储能单元共同支持热负荷;其特征在于,所述调度方法包括以下步骤:1. A virtual power plant coordination scheduling method considering hydrogen fuel vehicles and hydrogen energy storage, the virtual power plant comprises a wind turbine, a photovoltaic power station, a CHP unit, a hydrogen energy storage system, and a thermal energy storage unit, and the hydrogen energy storage system includes Electrolyzers, HFCs and hydrogen storage tanks, among which wind turbines, photovoltaic power stations, CHP units and external power grids jointly provide the hydrogen energy storage system with electricity for electrolysis of water to produce hydrogen and support electrical load IL to the outside world, and the external natural gas market is CHP units Provide fuel, and the hydrogen energy storage system supports the hydrogen load externally; the HFC, CHP unit and the thermal energy storage unit jointly support the thermal load; it is characterized in that, the scheduling method includes the following steps: 步骤1、构建考虑与路网耦合的氢燃料汽车所需氢负荷的预测模型,所述氢燃料汽车的形式线路是从加氢站到其他多个地点的行驶路线;根据氢燃料汽车到达加氢站时间和剩余燃料量得到燃料需求量;Step 1. Construct a prediction model considering the hydrogen load required by the hydrogen fuel vehicle coupled with the road network. The form route of the hydrogen fuel vehicle is the driving route from the hydrogen refueling station to other multiple locations; according to the hydrogen fuel vehicle arriving at hydrogen refueling Station time and remaining fuel amount to get fuel demand; 步骤2、构建包含电解槽、储氢罐和氢燃料电池的氢储能系统模型,包括电解槽、储氢罐和燃料电池设备的模型以及系统整体的模型;Step 2. Build a hydrogen energy storage system model including electrolyzers, hydrogen storage tanks and hydrogen fuel cells, including models of electrolyzers, hydrogen storage tanks, and fuel cell equipment, as well as models of the overall system; 步骤3、采用自回归滑动平均模型和k-means聚类方法生成风光典型出力场景集;Step 3. Use the autoregressive moving average model and the k-means clustering method to generate a set of typical scenery output scenes; 步骤4、以期望经济效益最大化为目标,构建虚拟电厂调度模型的目标函数,如式(1)所示:Step 4. With the goal of maximizing the expected economic benefits, construct the objective function of the virtual power plant dispatching model, as shown in formula (1):
Figure RE-FDA0003810563930000011
Figure RE-FDA0003810563930000011
式(1)中,Is,i(X0)、Cs,i(X0)分别为场景s下各项运行收益和成本指标函数,X0为优化变量;所述目标函数采用系统运行集约束,包括虚拟电厂整体运行约束和设备运行约束;In formula (1), Is ,i (X 0 ) and C s,i (X 0 ) are the respective operating income and cost index functions under the scenario s, and X 0 is the optimization variable; the objective function adopts the system operation Set constraints, including the overall operation constraints of the virtual power plant and equipment operation constraints; 步骤5、以夏季和冬季典型日的风、光出力生成场景集,代入虚拟电厂模型进行优化调度。Step 5. Generate a scene set based on the wind and light output of typical days in summer and winter, and substitute it into the virtual power plant model for optimal scheduling.
2.根据权利要求1所述的一种考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法,其特征在于,步骤1进一步包括以下子步骤:2. a kind of virtual power plant coordination scheduling method considering hydrogen fuel vehicle and hydrogen energy storage according to claim 1, is characterized in that, step 1 further comprises the following sub-steps: 步骤S11、计算氢燃料汽车到达加氢地点的时间:Step S11, calculate the time when the hydrogen fuel vehicle arrives at the hydrogenation location: 假设HV由聚合器控制,加氢站位于HV线路起始站点,当车辆n跑完第k次循环返回起始站点,由聚合器获取其到达时间
Figure RE-FDA0003810563930000021
和剩余燃料量
Figure RE-FDA0003810563930000022
则根据式(2)-(4)所示计算方法进行计算:
Assuming that the HV is controlled by the aggregator, and the hydrogen refueling station is located at the starting station of the HV line, when the vehicle n returns to the starting station after the kth cycle, the aggregator obtains its arrival time
Figure RE-FDA0003810563930000021
and remaining fuel
Figure RE-FDA0003810563930000022
Then calculate according to the calculation method shown in formulas (2)-(4):
Figure RE-FDA0003810563930000023
Figure RE-FDA0003810563930000023
Figure RE-FDA0003810563930000024
Figure RE-FDA0003810563930000024
Figure RE-FDA0003810563930000025
Figure RE-FDA0003810563930000025
其中,vt为t时段道路i的汽车平均行驶速度,与道路等级、时间及道路车流量等因素密切相关;α1、α2、α3和β为回归参数与修正系数,随道路等级变化;v0为各等级道路的设计车速;Ft为t时段道路的车流量;F0为为道路的设计通行车流量;D为车辆行驶过程中途径公交站点数量;
Figure RE-FDA0003810563930000031
为车辆初始时间;Di,d为途中第(d-1)个站点至第d个站点的道路距离;Δtd-1为在第(d-1)个站点停车等待的时间;
Figure RE-FDA0003810563930000032
为车辆n初始燃料量,采用蒙特卡洛模拟进行仿真,生成初始燃料随机数;l为车辆路线的距离;Δm为HV每公里氢耗量;η为汽车非正常行驶状态下的能耗系数,包括启动加速以及刹车期间发动机所需的负荷功导致的能量损失;
Among them, v t is the average speed of vehicles on road i in period t, which is closely related to factors such as road grade, time, and road traffic flow; α 1 , α 2 , α 3 and β are regression parameters and correction coefficients, which change with the road grade ; v 0 is the design speed of each grade of road; F t is the traffic flow of the road in the t period; F 0 is the design traffic flow of the road; D is the number of bus stops in the process of vehicle driving;
Figure RE-FDA0003810563930000031
is the initial time of the vehicle; D i,d is the road distance from the (d-1)th station to the dth station on the way; Δt d-1 is the waiting time at the (d-1)th station;
Figure RE-FDA0003810563930000032
is the initial fuel quantity of the vehicle n, which is simulated by Monte Carlo simulation to generate the initial fuel random number; l is the distance of the vehicle route; Δm is the hydrogen consumption per kilometer of the HV; η is the energy consumption coefficient under the abnormal driving state of the vehicle, Including the energy loss caused by the load work required by the engine during start-up acceleration and braking;
步骤S12、计算氢燃料汽车氢负荷需求总量:Step S12, calculate the total amount of hydrogen load demand for hydrogen fuel vehicles: 当剩余燃料小于一定值时,则在到达加氢站后进行加氢,HV加氢状态判断如式(5)、(6)所示:When the remaining fuel is less than a certain value, hydrogenation is carried out after arriving at the hydrogenation station. The judgment of the HV hydrogenation state is shown in formulas (5) and (6):
Figure RE-FDA0003810563930000033
Figure RE-FDA0003810563930000033
Figure RE-FDA0003810563930000034
Figure RE-FDA0003810563930000034
其中,mset为HV的燃料阈值;
Figure RE-FDA0003810563930000035
表示第n辆HV在第k次循环结束的t时段需要加氢;
Figure RE-FDA0003810563930000036
为t时段氢燃料汽车的燃料需求总量;N为氢燃料汽车的数量;
Figure RE-FDA0003810563930000037
为氢燃料汽车的储氢瓶含量。
Among them, mset is the fuel threshold of HV;
Figure RE-FDA0003810563930000035
Indicates that the nth HV needs to be hydrogenated in the period t at the end of the kth cycle;
Figure RE-FDA0003810563930000036
is the total fuel demand of hydrogen fuel vehicles in period t; N is the number of hydrogen fuel vehicles;
Figure RE-FDA0003810563930000037
The content of hydrogen storage tanks for hydrogen fuel vehicles.
3.根据权利要求2所述的一种考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法,其特征在于,步骤2进一步包括以下子步骤:3. a kind of virtual power plant coordination scheduling method considering hydrogen fuel vehicle and hydrogen energy storage according to claim 2, is characterized in that, step 2 further comprises the following sub-steps: 步骤S21、构建电解槽模型:Step S21, build an electrolytic cell model: 设定电解槽单位电量产氢率为ηPtH,则电解槽t时段的产氢气量
Figure RE-FDA0003810563930000041
被表示为产氢率ηPtH和输入电功率
Figure RE-FDA0003810563930000042
的乘积,如式(7)所示:
Set the hydrogen production rate per unit of electricity of the electrolytic cell η PtH , then the hydrogen production amount of the electrolytic cell in the period t
Figure RE-FDA0003810563930000041
is expressed as hydrogen production rate η PtH and input electric power
Figure RE-FDA0003810563930000042
The product of , as shown in formula (7):
Figure RE-FDA0003810563930000043
Figure RE-FDA0003810563930000043
步骤S22、构建氢燃料电池模型:Step S22, build a hydrogen fuel cell model: 氢燃料电池的发电和产热功率分别由消耗氢气量
Figure RE-FDA0003810563930000044
和氢燃料电池温度THFC决定,将氢燃料电池的模型表示为如式(8)所示:
The power generation and heat generation power of hydrogen fuel cells are determined by the consumption of hydrogen, respectively.
Figure RE-FDA0003810563930000044
and the hydrogen fuel cell temperature T HFC , the model of the hydrogen fuel cell is expressed as formula (8):
Figure RE-FDA0003810563930000045
Figure RE-FDA0003810563930000045
其中,Ener为能斯特电压;ηact、ηohm、ηcon分别为活化极化、欧姆和浓差损耗;F、MH2分别为法拉第常数和氢气摩尔质量;ηHFCh为氢燃料电池的产热效率;
Figure RE-FDA0003810563930000046
为总功率;
Among them, E ner is the Nernst voltage; η act , η ohm , and η con are activation polarization, ohmic and concentration loss, respectively; F and M H2 are the Faraday constant and hydrogen molar mass, respectively; η HFCh is the hydrogen fuel cell heat production efficiency;
Figure RE-FDA0003810563930000046
is the total power;
步骤S23、构建储氢罐模型:Step S23, build a hydrogen storage tank model: 储氢罐储存电解槽生成的氢气,为氢燃料电池提供氢气,给氢燃料汽车补充燃料获得利润,将储氢罐中的氢气质量表示为如式(9)所示:The hydrogen storage tank stores the hydrogen generated by the electrolyzer, provides hydrogen for the hydrogen fuel cell, and supplements the fuel for the hydrogen fuel vehicle to obtain profits. The hydrogen quality in the hydrogen storage tank is expressed as formula (9):
Figure RE-FDA0003810563930000047
Figure RE-FDA0003810563930000047
式(9)中,
Figure RE-FDA0003810563930000048
为t时段储氢罐中氢气的质量;
Figure RE-FDA0003810563930000049
为t时段电解槽的产氢量;
Figure RE-FDA00038105639300000410
为t时段氢燃料电池的耗氢量;
Figure RE-FDA00038105639300000411
为t时段HV的氢气需求量;
In formula (9),
Figure RE-FDA0003810563930000048
is the mass of hydrogen in the hydrogen storage tank at time t;
Figure RE-FDA0003810563930000049
is the hydrogen production of the electrolyzer in period t;
Figure RE-FDA00038105639300000410
is the hydrogen consumption of the hydrogen fuel cell in period t;
Figure RE-FDA00038105639300000411
is the hydrogen demand of HV in period t;
步骤S24、构建氢储能系统模型:Step S24, build a hydrogen energy storage system model: 将氢储能系统整体的模型表示为如式(10)所示:The overall model of the hydrogen energy storage system is expressed as equation (10):
Figure RE-FDA0003810563930000051
Figure RE-FDA0003810563930000051
Figure RE-FDA0003810563930000052
Figure RE-FDA0003810563930000052
Figure RE-FDA0003810563930000053
Figure RE-FDA0003810563930000053
式中,
Figure RE-FDA0003810563930000054
为氢储能系统整体的输出功率;布尔变量
Figure RE-FDA0003810563930000055
分别表示t时段氢储能电解槽和氢燃料电池工作状态。
In the formula,
Figure RE-FDA0003810563930000054
is the overall output power of the hydrogen energy storage system; Boolean variable
Figure RE-FDA0003810563930000055
respectively represent the working states of the hydrogen energy storage electrolyzer and the hydrogen fuel cell in the t period.
4.根据权利要求3所述的一种考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法,其特征在于,步骤3进一步包括以下子步骤:4. a kind of virtual power plant coordination scheduling method considering hydrogen fuel vehicle and hydrogen energy storage according to claim 3, is characterized in that, step 3 further comprises the following sub-steps: 步骤S31、确定基于均值和标准差的白噪声,即滑动回归平均参数;Step S31, determining the white noise based on the mean and standard deviation, that is, the sliding regression mean parameter; 步骤S32、基于基准预测数据,本着残差方差最小原则,生成负荷风电出力各1000个场景数据;Step S32 , generating 1000 scene data of each load wind power output based on the reference prediction data and the principle of minimum residual variance; 步骤S33、基于改进k-means聚类算法,对风光出力进行聚类,生成若干个典型运行场景,具体包括:基于局部密度均值聚类算法寻找初始的数据聚类中心;基于初始聚类中心,采用k-means聚类算法生成典型运行场景。Step S33, based on the improved k-means clustering algorithm, cluster the wind and solar output, and generate several typical operating scenarios, which specifically include: finding the initial data clustering center based on the local density mean clustering algorithm; based on the initial clustering center, The k-means clustering algorithm is used to generate typical running scenarios. 5.根据权利要求4所述的一种考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法,其特征在于,步骤4进一步包括:5. A method for coordinating and dispatching a virtual power plant considering hydrogen fuel vehicles and hydrogen energy storage according to claim 4, wherein step 4 further comprises: 建立虚拟电厂协调调度优化目标模型,目标函数表示为如式(13)所示:A virtual power plant coordination scheduling optimization objective model is established, and the objective function is expressed as formula (13):
Figure RE-FDA0003810563930000061
Figure RE-FDA0003810563930000061
其中,Is,i(X0)、Cs,i(X0)分别为场景s下各项运行收益和成本指标函数,X0为优化变量;所述各项运行收益和成本指标函数分别包括:Among them, I s,i (X 0 ), C s,i (X 0 ) are the respective operating benefit and cost index functions under the scenario s, and X 0 is the optimization variable; the operating benefit and cost index functions are respectively include: (1)场景s下虚拟电厂参与日前能量市场、旋转备用和调峰市场的售电总收益表示为如式(14)所示:(1) Under scenario s, the total revenue of electricity sales of virtual power plants participating in the day-ahead energy market, rotating reserve and peak shaving market is expressed as formula (14):
Figure RE-FDA0003810563930000062
Figure RE-FDA0003810563930000062
其中,
Figure RE-FDA0003810563930000063
表示t时段的日前电能量市场电价;
Figure RE-FDA0003810563930000064
表示t时段的备用容量市场电价;
Figure RE-FDA0003810563930000065
Figure RE-FDA0003810563930000066
分别表示t时段的向上调峰和向下调峰电价;
Figure RE-FDA0003810563930000067
Figure RE-FDA0003810563930000068
分别表示场景s下t时段虚拟电厂的日前电能量出力、备用出力和向上向下调峰;
Figure RE-FDA0003810563930000069
表示场景s下t时段虚拟电厂的热出力。
Figure RE-FDA00038105639300000610
分别表示t时段的EM、SRM、向上调峰和向下调峰电价;
Figure RE-FDA00038105639300000611
分别为场景s下t时段风、光、电解槽实际出力;
Figure RE-FDA00038105639300000612
分别为CHP机组和HFC参与EM、SRM和向上、向下调峰市场的出力;
in,
Figure RE-FDA0003810563930000063
Represents the day-ahead electric energy market price in t period;
Figure RE-FDA0003810563930000064
represents the market electricity price of reserve capacity in period t;
Figure RE-FDA0003810563930000065
and
Figure RE-FDA0003810563930000066
Respectively represent the up-peak and down-peak electricity prices in the t period;
Figure RE-FDA0003810563930000067
and
Figure RE-FDA0003810563930000068
Respectively represent the day-ahead power output, standby output and peak-down peaking of the virtual power plant in the period t under the scenario s;
Figure RE-FDA0003810563930000069
Indicates the heat output of the virtual power plant in the t period under the scenario s.
Figure RE-FDA00038105639300000610
Respectively represent the EM, SRM, peak-up and down-peak electricity prices in t period;
Figure RE-FDA00038105639300000611
are the actual outputs of wind, light, and electrolytic cells in the t period of the scene s, respectively;
Figure RE-FDA00038105639300000612
The output of CHP unit and HFC participating in EM, SRM and up and down peak markets respectively;
(2)场景s下虚拟电厂供热的收益表示为如式(15)所示:(2) The revenue of virtual power plant heating under scenario s is expressed as formula (15):
Figure RE-FDA0003810563930000071
Figure RE-FDA0003810563930000071
其中,
Figure RE-FDA0003810563930000072
分别为CHP机组、HFC和热储能储、放的热功率;
in,
Figure RE-FDA0003810563930000072
are the thermal power of CHP unit, HFC and thermal energy storage and discharge respectively;
(3)场景s下虚拟电厂出售氢气的收益表示为如式(16)所示:(3) In the scenario s, the revenue from the sale of hydrogen by the virtual power plant is expressed as formula (16):
Figure RE-FDA0003810563930000073
Figure RE-FDA0003810563930000073
其中,
Figure RE-FDA0003810563930000074
表示氢气价格;
in,
Figure RE-FDA0003810563930000074
represents the hydrogen price;
(4)碳交易收益表示为如式(17)所示:(4) The carbon trading revenue is expressed as formula (17):
Figure RE-FDA0003810563930000075
Figure RE-FDA0003810563930000075
其中,CCM为碳交易价格;
Figure RE-FDA0003810563930000076
为场景s下t时段虚拟电厂的碳排放配额;γe、γh分别为CHP机组的供电基准值和供热基准值;Fr为机组供热量修正系数;
Among them, C CM is the carbon trading price;
Figure RE-FDA0003810563930000076
is the carbon emission quota of the virtual power plant in the period t under the scenario s; γ e and γ h are the reference value of power supply and the reference value of heat supply of the CHP unit, respectively; F r is the correction coefficient of heat supply of the unit;
(5)场景s下风光发电的运行维护成本表示为如式(18)所示:(5) The operation and maintenance cost of wind and solar power generation in scenario s is expressed as formula (18):
Figure RE-FDA0003810563930000077
Figure RE-FDA0003810563930000077
其中,kW、kPV分别为风光发电的单位运行维护成本;
Figure RE-FDA0003810563930000078
分别为场景s下t时段风、光实际出力;
Among them, k W and k PV are the unit operation and maintenance costs of wind and solar power generation respectively;
Figure RE-FDA0003810563930000078
are the actual output of wind and light in time period t under scene s, respectively;
(6)场景s下虚拟电厂与调度指令偏差的惩罚成本表示为如式(19)所示:(6) In the scenario s, the penalty cost of the deviation between the virtual power plant and the dispatch instruction is expressed as formula (19):
Figure RE-FDA0003810563930000081
Figure RE-FDA0003810563930000081
其中,
Figure RE-FDA0003810563930000082
表示场景s下t时段EM、向上向下调峰的偏差量;γem、γru、γrd分别为EM、向上向下调峰的惩罚系数;
in,
Figure RE-FDA0003810563930000082
Represents the deviation amount of EM, upward and downward peak reduction in the t period of scene s; γ em , γ ru , and γ rd are the penalty coefficients of EM and upward and downward peak reduction, respectively;
(7)场景s下CHP机组的成本表示为如式(20)所示:(7) The cost of CHP unit under scenario s is expressed as formula (20):
Figure RE-FDA0003810563930000083
Figure RE-FDA0003810563930000083
其中,α0、α1、α2、α3、α4、α5为CHP机组能耗系数;
Figure RE-FDA0003810563930000084
表示CHP机组的电出力;
Among them, α 0 , α 1 , α 2 , α 3 , α 4 , α 5 are the energy consumption coefficients of CHP units;
Figure RE-FDA0003810563930000084
Indicates the electrical output of the CHP unit;
(8)场景s下氢储能的成本包括电解槽、燃料电池和储氢罐的运行维护成本,被表示为如式(21)所示:(8) The cost of hydrogen energy storage in scenario s includes the operation and maintenance costs of electrolyzers, fuel cells and hydrogen storage tanks, and is expressed as equation (21):
Figure RE-FDA0003810563930000085
Figure RE-FDA0003810563930000085
其中,
Figure RE-FDA0003810563930000086
表示场景s下t时段电解槽、HFC、储氢罐的运行维护成本;λPtH、λHFC、λHS分别为电解槽、HFC和储氢罐的单位运行维护成本;
Figure RE-FDA0003810563930000087
为场景s下t时段储氢罐储氢质量。
in,
Figure RE-FDA0003810563930000086
represents the operation and maintenance costs of the electrolyzer, HFC, and hydrogen storage tank in the t period of the scenario s; λ PtH , λ HFC , and λ HS are the unit operation and maintenance costs of the electrolyzer, HFC and hydrogen storage tank, respectively;
Figure RE-FDA0003810563930000087
is the hydrogen storage quality of the hydrogen storage tank in the t period of the scenario s.
6.根据权利要求5所述的一种考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法,其特征在于,所述目标函数采用系统运行集约束,包括虚拟电厂整体运行约束和设备运行约束,其中,所述虚拟电厂整体运行约束包括:日前电能量市场功率平衡约束、备用容量约束、向上调峰功率约束、向下调峰功率约束和热功率平衡约束,分别表达为如下所示:6. A virtual power plant coordination scheduling method considering hydrogen fuel vehicles and hydrogen energy storage according to claim 5, wherein the objective function adopts system operation set constraints, including virtual power plant overall operation constraints and equipment operation constraints , wherein the overall operation constraints of the virtual power plant include: day-ahead electric energy market power balance constraints, reserve capacity constraints, up-peak power constraints, down-peak power constraints, and thermal power balance constraints, which are respectively expressed as follows: (1)日前电能量市场功率平衡约束被表示为如式(22)所示:(1) The power balance constraint of the day-ahead electric energy market is expressed as formula (22):
Figure RE-FDA0003810563930000091
Figure RE-FDA0003810563930000091
式中,
Figure RE-FDA0003810563930000092
为上级电网下发的t时段EM电量指令;
Figure RE-FDA0003810563930000093
分别为场景s下t时段CHP机组和HFC电能量市场的功率;
In the formula,
Figure RE-FDA0003810563930000092
The EM power command issued by the upper-level power grid in the t period;
Figure RE-FDA0003810563930000093
are the power of the CHP unit and the HFC power market in the t period of the scenario s, respectively;
(2)备用容量约束被表示为如式(23)所示:(2) The reserve capacity constraint is expressed as Eq. (23):
Figure RE-FDA0003810563930000094
Figure RE-FDA0003810563930000094
式中,
Figure RE-FDA0003810563930000095
分别为场景s下t时段CHP机组和HFC在备用容量市场的备用容量;
In the formula,
Figure RE-FDA0003810563930000095
are the spare capacity of CHP units and HFC in the spare capacity market in the period t under scenario s, respectively;
(3)向上、下调峰功率约束被表示为如式(24)所示:(3) The up and down peak power constraints are expressed as equation (24):
Figure RE-FDA0003810563930000096
Figure RE-FDA0003810563930000096
式中,
Figure RE-FDA0003810563930000097
分别为上级电网下发的t时段向上向下调峰的指令功率;
Figure RE-FDA0003810563930000098
分别为场景s下t时段CHP机组和HFC在灵活调峰市场向上向下调峰的功率;
In the formula,
Figure RE-FDA0003810563930000097
are the command power for peaking up and down in t period issued by the upper-level power grid, respectively;
Figure RE-FDA0003810563930000098
are the powers of CHP units and HFC in the flexible peak shaving market up and down in the t period under scenario s, respectively;
(5)热功率平衡约束被表示为如式(25)所示:(5) The thermal power balance constraint is expressed as Eq. (25):
Figure RE-FDA0003810563930000101
Figure RE-FDA0003810563930000101
式中,Ht为t时段虚拟电厂热负荷需求;
Figure RE-FDA0003810563930000102
为场景s下t时段CHP机组的热功率;
Figure RE-FDA0003810563930000103
分别为场景s下t时段热储能的充、放热功率;
In the formula, H t is the heat load demand of the virtual power plant in period t;
Figure RE-FDA0003810563930000102
is the thermal power of the CHP unit in the t period under the scenario s;
Figure RE-FDA0003810563930000103
are the charging and discharging powers of the thermal energy storage in the t period of the scene s, respectively;
所述设备运行约束包括CHP机组出力约束、电解槽出力及爬坡约束、燃料电池运行及爬坡约束和储氢罐和热储能约束,分别表示为:The equipment operation constraints include CHP unit output constraints, electrolyzer output and ramp constraints, fuel cell operation and ramp constraints, and hydrogen storage tank and thermal energy storage constraints, which are expressed as: (6))CHP机组出力约束(6)) Output constraints of CHP units 将CHP机组的运行区间限定为四边形ABCD的范围内,边界AD、AB、BC、CD分别代表蒸汽喷射的最小极限、最大热率、燃料喷射的最大极限、输出电功率的最大极限,定义转角点,即边界交点的电功率、热功率为(xk,yk);CHP机组的电功率、热功率与边界交点坐标的关系被表示为如式(26)所示:The operating interval of the CHP unit is limited to the range of the quadrilateral ABCD, and the boundaries AD, AB, BC, and CD represent the minimum limit of steam injection, the maximum heat rate, the maximum limit of fuel injection, and the maximum limit of output electric power, respectively. Define the corner point, That is, the electrical power and thermal power of the boundary intersection point are (x k , y k ); the relationship between the electrical power and thermal power of the CHP unit and the coordinates of the boundary intersection point is expressed as formula (26):
Figure RE-FDA0003810563930000104
Figure RE-FDA0003810563930000104
式中,Mi为CHP机组的边界交点总数,组合系数满足如式(27)所示约束方程:In the formula, M i is the total number of boundary intersection points of the CHP unit, and the combination coefficient satisfies the constraint equation shown in Eq. (27):
Figure RE-FDA0003810563930000111
Figure RE-FDA0003810563930000111
(7)电解槽出力及爬坡约束被表示为如式(28)、(29)所示:(7) The output of the electrolytic cell and the constraints of climbing are expressed as formulas (28) and (29):
Figure RE-FDA0003810563930000112
Figure RE-FDA0003810563930000112
Figure RE-FDA0003810563930000113
Figure RE-FDA0003810563930000113
式中,
Figure RE-FDA0003810563930000114
分别为电解槽出力上、下限;RPtH为电解槽出力爬坡速率约束;
In the formula,
Figure RE-FDA0003810563930000114
are the upper and lower limits of the output of the electrolytic cell, respectively; R PtH is the limit of the ramp rate of the output of the electrolytic cell;
(8)燃料电池运行及爬坡约束被表示为如式(30)、(31)、(32)所示:(8) The fuel cell operation and climbing constraints are expressed as equations (30), (31), (32):
Figure RE-FDA0003810563930000115
Figure RE-FDA0003810563930000115
Figure RE-FDA0003810563930000116
Figure RE-FDA0003810563930000116
Figure RE-FDA0003810563930000117
Figure RE-FDA0003810563930000117
式中,
Figure RE-FDA0003810563930000118
分别为燃料电池出力上、下限;RHFC为燃料电池出力爬坡速率约束;
In the formula,
Figure RE-FDA0003810563930000118
are the upper and lower limits of fuel cell output, respectively; R HFC is the fuel cell output ramp rate constraint;
(9)储氢罐和热储能约束被表示为如式(33)-(39)所示:(9) The hydrogen storage tank and thermal energy storage constraints are expressed as equations (33)-(39):
Figure RE-FDA0003810563930000119
Figure RE-FDA0003810563930000119
Figure RE-FDA00038105639300001110
Figure RE-FDA00038105639300001110
Figure RE-FDA00038105639300001111
Figure RE-FDA00038105639300001111
Figure RE-FDA00038105639300001112
Figure RE-FDA00038105639300001112
Figure RE-FDA00038105639300001113
Figure RE-FDA00038105639300001113
Figure RE-FDA0003810563930000121
Figure RE-FDA0003810563930000121
Figure RE-FDA0003810563930000122
Figure RE-FDA0003810563930000122
式中,
Figure RE-FDA0003810563930000123
分别为储氢的上、下限;
Figure RE-FDA0003810563930000124
分别为储氢量在一天的始、末值。
Figure RE-FDA0003810563930000125
分别为储、放热功率的最大值;布尔变量
Figure RE-FDA0003810563930000126
分别表示场景s下t时段储热装置是否储放热,是则置1,否则置0;
Figure RE-FDA0003810563930000127
分别为储热容量的上、下限;
Figure RE-FDA0003810563930000128
分别为储热容量在一天的始、末值。
In the formula,
Figure RE-FDA0003810563930000123
are the upper and lower limits of hydrogen storage, respectively;
Figure RE-FDA0003810563930000124
are the hydrogen storage capacity at the beginning and end of the day, respectively.
Figure RE-FDA0003810563930000125
are the maximum values of storage and heat release power, respectively; Boolean variable
Figure RE-FDA0003810563930000126
Respectively indicate whether the heat storage device stores and releases heat in the t period of the scene s, if it is, it is set to 1, otherwise it is set to 0;
Figure RE-FDA0003810563930000127
are the upper and lower limits of the heat storage capacity, respectively;
Figure RE-FDA0003810563930000128
are the beginning and end values of the heat storage capacity in a day, respectively.
7.根据权利要求1-6任一所述的一种考虑氢燃料汽车与氢储能的虚拟电厂协调调度方法,其特征在于,所述虚拟电厂由1台CHP机组、1个风电场、1个光伏电站、1台电解制氢装置,1台燃料电池,1个储氢罐和1个储热装置组成;所述电解制氢装置的最大功率为5MW,爬坡率为1MW;所述燃料电池的最大功率为5MW,爬坡率为2MW;所述储氢罐的最大容量为1000kg,最小容量为100kg,初始容量为500kg;所述储热装置的最大容量为10MW·h,最小容量为1MW·h,初始容量为5MW·h,储放热效率为0.88。7. A virtual power plant coordination scheduling method considering hydrogen fuel vehicles and hydrogen energy storage according to any one of claims 1-6, wherein the virtual power plant consists of 1 CHP unit, 1 wind farm, 1 It consists of a photovoltaic power station, an electrolysis hydrogen production device, a fuel cell, a hydrogen storage tank and a heat storage device; the maximum power of the electrolytic hydrogen production device is 5MW, and the ramp rate is 1MW; the fuel The maximum power of the battery is 5MW, and the ramp rate is 2MW; the maximum capacity of the hydrogen storage tank is 1000kg, the minimum capacity is 100kg, and the initial capacity is 500kg; the maximum capacity of the heat storage device is 10MW·h, and the minimum capacity is 1MW·h, the initial capacity is 5MW·h, and the heat storage and release efficiency is 0.88.
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