WO2023050223A1 - Hydrogen production system and control method therefor - Google Patents
Hydrogen production system and control method therefor Download PDFInfo
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- WO2023050223A1 WO2023050223A1 PCT/CN2021/121939 CN2021121939W WO2023050223A1 WO 2023050223 A1 WO2023050223 A1 WO 2023050223A1 CN 2021121939 W CN2021121939 W CN 2021121939W WO 2023050223 A1 WO2023050223 A1 WO 2023050223A1
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- hydrogen
- modular multilevel
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- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 134
- 239000001257 hydrogen Substances 0.000 title claims abstract description 134
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 133
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 61
- 238000000034 method Methods 0.000 title claims description 26
- 230000002457 bidirectional effect Effects 0.000 claims description 3
- 238000010586 diagram Methods 0.000 description 15
- 238000002955 isolation Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 101000588130 Homo sapiens Microsomal triglyceride transfer protein large subunit Proteins 0.000 description 1
- 102100031545 Microsomal triglyceride transfer protein large subunit Human genes 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J3/00—Circuit arrangements for ac mains or ac distribution networks
- H02J3/38—Arrangements for parallely feeding a single network by two or more generators, converters or transformers
Definitions
- the present disclosure generally relates to the technical field of hydrogen production, and more particularly, to a hydrogen production system and a control method thereof.
- One solution to the high-power hydrogen storage topology in the prior art is to connect multiple DC/DC converters in parallel to handle the high current of the hydrogen electrolyzer.
- high currents can be further handled by using parallel switches in each module.
- High-power converters usually use IGBTs.
- the power current sharing problem of parallel IGBTs faces challenges.
- each PV module has a boost converter.
- the DC/DC converter then feeds the parallel DC/AC converter which converts the DC to AC.
- an uncontrolled AC/DC rectifier is connected to power the hydrogen electrolyzer.
- a power frequency transformer is introduced into this system, which increases the volume of the system.
- each PV module has a DC/DC converter, and the outputs are then connected in series to power the hydrogen electrolyzer.
- the main disadvantages of this scheme are as follows:
- Each photovoltaic module has its own DC/DC converter, which brings high costs and is not suitable for high-power systems.
- the photovoltaic DC/DC converter is connected in series to power the hydrogen electrolyzer, which does not match the low-voltage characteristics of the hydrogen electrolyzer.
- the system is very simple and does not contain power electronic converters.
- the voltage and power are not controlled, which affects the efficiency and lifetime of the hydrogen electrolyzer.
- the present invention proposes a hydrogen production system and a control method for the hydrogen production system.
- a hydrogen production system including: a photovoltaic module, a power grid, at least one modular multilevel converter, and a hydrogen electrolyzer, and the modular multilevel converter includes at least one Each phase unit includes an upper bridge arm and a lower bridge arm, and the upper bridge arm and the lower bridge arm respectively include at least one power module, wherein the photovoltaic module is connected to the DC bus of the modular multilevel converter side; the grid is connected to the AC bus side of the modular multilevel converter; and the DC side outputs of the power modules of the modular multilevel converter are connected in parallel to supply power to the hydrogen electrolyzer .
- the power module adopts an isolation topology circuit.
- the isolated topology circuit includes a DC/AC and a DC/DC two-stage, wherein the DC/AC is a two-level DC/AC or a three-level DC/AC Any one of, the DC/DC is any one of LLC DC/DC and full-bridge phase-shifted DC/DC.
- a method for controlling a hydrogen production system used for controlling the above-mentioned hydrogen production system, the control method includes: adjusting the power of the modular multilevel converter of the hydrogen production system The current on the DC bus side is used to track the maximum power point of the photovoltaic component, and the maximum power of the photovoltaic component is used to supply power to the hydrogen electrolyzer; and when the actual power of the photovoltaic component is less than the power reference value of the hydrogen electrolyzer , the grid provides differential power to the hydrogen electrolyzer to keep the power supplied to the hydrogen electrolyzer constant, wherein the differential power is the difference between the power reference value of the hydrogen electrolyzer and the actual power of the photovoltaic module.
- the control method further includes: when the actual power of the photovoltaic module is greater than the power reference value of the hydrogen electrolyzer , feeding the excess power generated by the photovoltaic components to the grid.
- a hydrogen production system including: a photovoltaic module, a power grid, at least one modular multilevel converter, a hydrogen electrolyzer, a photovoltaic-side DC/AC converter, and a grid-side DC/AC converter.
- the modular multilevel converter includes at least one phase unit, each phase unit includes an upper bridge arm and a lower bridge arm, and the upper bridge arm and the lower bridge arm respectively include at least one power module, wherein the The photovoltaic module is connected to the AC bus side of the modular multilevel converter through the photovoltaic side DC/AC converter; the power grid is connected to the modular multilevel converter through the grid side DC/AC converter The DC bus side of the converter; and the DC side output of the power module of the modular multilevel converter are connected in parallel to supply power to the hydrogen electrolyzer.
- the technical solution of the present invention has at least one of the following advantages.
- Fig. 1 is an exemplary topological diagram of a hydrogen production system according to an embodiment of the present invention
- FIG. 2A is a flowchart of an exemplary process of a method for controlling a hydrogen production system according to an embodiment of the present invention
- Fig. 2B is a control schematic diagram of a hydrogen production system according to an embodiment of the present invention.
- Fig. 2C is a schematic diagram of specific control of the hydrogen production system according to an embodiment of the present invention.
- Fig. 3 is an exemplary topological diagram of a hydrogen production system according to another embodiment of the present invention.
- Fig. 4A is an exemplary topological diagram of a hydrogen production system according to yet another embodiment of the present invention.
- Fig. 4B is a schematic diagram of the specific control of the hydrogen production system according to another embodiment of the present invention.
- AC-BUS AC bus side 200: Control method
- step 410 photovoltaic side DC/AC converter
- the term “comprising” and its variants represent open terms meaning “including but not limited to”.
- the term “based on” means “based at least in part on”.
- the terms “one embodiment” and “an embodiment” mean “at least one embodiment.”
- the term “another embodiment” means “at least one other embodiment.”
- the terms “first”, “second”, etc. may refer to different or the same object. The following may include other definitions, either express or implied. Unless the context clearly indicates otherwise, the definition of a term is consistent throughout the specification.
- the present invention is based on the consideration of how to maximize the use of PV power while keeping the power of the hydrogen electrolyzer stable to eliminate the intermittent impact of PV.
- a hydrogen production system powered by a photovoltaic-grid hybrid is proposed. While maximizing the use of photovoltaic power, the power provided by the grid is used to eliminate the intermittent impact of photovoltaics and maintain stable power for the hydrogen electrolyzer.
- FIG. 1 is an exemplary topological diagram of a hydrogen production system 100 according to an embodiment of the present invention.
- the hydrogen production system 100 includes a photovoltaic module 102 , a grid 104 , at least one modular multilevel converter 106 and a hydrogen electrolyzer 108 .
- the modular multilevel converter 106 includes three phase units 1062 , each phase unit includes an upper bridge arm and a lower bridge arm, and the upper bridge arm and the lower bridge arm respectively include at least one power module 1060 .
- phase units included in the modular multilevel converter 106 may not be limited to three.
- the photovoltaic module 102 is connected to the DC bus side DC-BUS of the modular multilevel converter 106; the grid 104 is connected to the AC bus side AC-BUS of the modular multilevel converter 106; The DC side outputs of the power modules of the modular multilevel converter 106 are connected in parallel to supply power to the hydrogen electrolyzer 108 .
- the isolation topology circuit includes DC/AC and DC/DC secondary, DC/AC can be, for example, two-level DC/AC or three-level DC/AC, and DC/DC can be LLC DC/DC or full-bridge phase-shifted DC/ One of a kind in DC.
- DC/AC can be, for example, two-level DC/AC or three-level DC/AC
- DC/DC can be LLC DC/DC or full-bridge phase-shifted DC/ One of a kind in DC.
- Those skilled in the art can also choose other forms of isolation topology circuits according to needs, and are not limited to the topology forms described here.
- the hydrogen production system 100 is based on a modular multilevel converter (MMC), thus inheriting the characteristics of the MMC.
- MMC modular multilevel converter
- the number of phase units of the modular multilevel converter can be set according to the power grid, photovoltaic and hydrogen electrolyzer’s rated power, and the number of power modules in each bridge arm can also be determined according to the needs, so
- the hydrogen production system according to the present invention has redundancy capability; and is easy to expand due to the modular design.
- Fig. 2A is a flowchart of an exemplary process of a method 200 for controlling a hydrogen production system according to an embodiment of the present invention.
- step S202 the current of the DC-BUS of the modular multilevel converter 106 of the hydrogen production system 100 is adjusted to track the maximum power point of the photovoltaic module 102, and the photovoltaic module 102 The maximum power of is supplied to the hydrogen electrolyzer 108.
- step S204 when the power of the photovoltaic module 102 is less than the required power of the hydrogen electrolyzer 108 , the power grid 104 provides differential power to the hydrogen electrolyzer 108 to keep the power supplied to the hydrogen electrolyzer 108 constant.
- the differential power here refers to the difference between the power required by the hydrogen electrolyzer 108 and the power provided by the photovoltaic module 102 .
- Fig. 2B is a schematic diagram of controlling the hydrogen production system according to an embodiment of the present invention
- Fig. 2C is a schematic diagram of controlling the voltage of each bridge arm of the hydrogen production system.
- abc/dq0 represents the transformation from abc coordinates to dq0 coordinates
- PG * represents the given power on the grid side (also called reference value, the same below)
- P H2 * represents the given power of the hydrogen electrolyzer
- P PV * means photovoltaic power reference
- PG means grid side power feedback (also called actual value, the same below)
- igd * means grid side d-axis current setting
- igd means grid side d-axis current feedback
- d d * means d-axis duty cycle setting
- i gq * means grid side q-axis current setting
- i gq means grid side q-axis current feedback
- d q * means q-axis duty cycle setting
- i g0 indicates the 0-axis current feedback on the grid side
- d 0 * indicates the 0-axis duty cycle setting
- P MPPT *
- maximum power point tracking (Maximum Power Point Tracking (MPPT)) of photovoltaics can be realized by controlling the current i dc of the DC-BUS of the modular multilevel converter 106 of the hydrogen production system 100 . Therefore, the MTTP loop output is set to be the reference current i dc * of i dc .
- the maximum power point of the photovoltaic module can be tracked, and the hydrogen electrolyzer can be supplied with the maximum power of the photovoltaic module.
- the power provided to the hydrogen electrolyzer can be kept constant, thereby eliminating the impact of PV intermittent on the hydrogen production system.
- the power on the grid side can also be bidirectional.
- the control method 200 may further include step S206 , when the power feedback of the photovoltaic assembly 102 is greater than the given power of the hydrogen electrolyzer 108 , the excess power generated by the photovoltaic assembly 102 may be fed to the grid 104 .
- the hydrogen production system according to the present invention can maximize the utilization rate of the electric energy generated by the photovoltaic module, and at the same time ensure that the electric energy supplied to the hydrogen electrolyzer remains stable.
- FIG. 3 shows an exemplary topology diagram of a hydrogen production system 300 according to another embodiment of the present invention.
- the hydrogen production system 300 in FIG. 3 includes a photovoltaic module 302 , a grid 304 and a hydrogen electrolyzer 308 .
- the structures and functions of the photovoltaic module 302, the grid 304, and the hydrogen electrolyzer 308 are similar to those of the photovoltaic module 102, the grid 104, and the hydrogen electrolyzer 108 described above with reference to FIG. 1 , and will not be repeated here.
- Fig. 3 Another solution of the hydrogen production system as shown in Fig. 3 is provided.
- the hydrogen production system shown in Figure 3 two modular multilevel converters are used, and the number of phase units is increased from three to six.
- the parallel output voltages of the power modules of the two modular multilevel converters are connected together in series to match the higher voltage of the hydrogen electrolyzer.
- the hydrogen production system according to this embodiment can be applied to hydrogen electrolyzers with higher power, and the number of modular multilevel converters, the number of phase units, and The number of power modules will not be described in detail here.
- Fig. 4 shows an exemplary topology diagram of a hydrogen production system 400 according to yet another embodiment of the present invention.
- the hydrogen production system 400 includes a photovoltaic module 402 , a grid 404 , at least one modular multilevel converter 406 and a hydrogen electrolyzer 408 .
- the structure and function of the photovoltaic assembly 402, the grid 404, the modular multilevel converter 406 and the hydrogen electrolyzer 408 are the same as those of the photovoltaic assembly 102, the grid 104, at least one modular multilevel converter described above with reference to FIG.
- the current flow device 106 is similar to the hydrogen electrolyzer 108, and will not be repeated here.
- the hydrogen production system 400 also includes a photovoltaic side DC/AC converter 410 and a grid side DC/AC converter 412, and the photovoltaic module 402 is connected to a modular multilevel converter via the photovoltaic side DC/AC converter 410
- the AC bus side of 406; the power grid 404 is connected to the DC bus side of the modular multilevel converter 406 via the grid side DC/AC converter 412; the DC side outputs of the power modules of the modular multilevel converter 406 are connected in parallel together supply power to the hydrogen electrolyzer 408 .
- connection positions of the grid and the photovoltaic modules are exchanged, providing a different topology.
- Those skilled in the art can select an appropriate topology of the hydrogen production system according to needs.
- Fig. 4B is a control diagram for the hydrogen production system topology shown in Fig. 4A.
- id * represents the d-axis current setting on the photovoltaic inverter side
- id represents the d-axis current feedback on the photovoltaic inverter side
- i q * represents the q-axis current setting on the photovoltaic inverter side
- i q represents the q-axis current feedback on the PV inverter side
- i 0 * represents the 0-axis current setting on the PV inverter side
- i 0 represents the 0-axis current feedback on the PV inverter side
- i 0 represents the 0-axis current feedback on the PV inverter side
- i dc * represents the bus current on the grid side
- i dc represents the grid-side bus current feedback, and the meanings of other variables are the same as those shown in Figs. 2A-2C , and will not be repeated here.
- the technical solution of the present invention has at least one of the following advantages.
- the device structures described in the above embodiments may be physical structures or logical structures, that is, some units may be implemented by the same physical entity, or some units may be respectively implemented by multiple physical entities, or may be implemented by multiple physical entities. Certain components in individual devices are implemented together.
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Abstract
A hydrogen production system (100, 400), comprising: a photovoltaic assembly (102, 402), a power grid (104, 404), at least one modular multilevel converter (106, 406) and a hydrogen electrolyzer (108, 408), the modular multilevel converter (106, 406) comprising at least one phase unit (1062, 4062), each phase unit (1062, 4062) comprising an upper bridge arm (1062-1, 4062-1) and a lower bridge arm (1062-2, 4062-2), and the upper bridge arm (1062-1, 4062-1) and the lower bridge arm (1062-2, 4062-2) each comprising at least one power module (1060, 4060), wherein the photovoltaic assembly (102, 402) is connected to a direct current bus side (DC-BUS) of the modular multilevel converter (106, 406); the power grid (104, 404) is connected to an alternating current bus side (AC-BUS) of the modular multilevel converter (106, 406); and DC side output of the power modules (1060, 4060) of the modular multilevel converter (106, 406) are connected in parallel together to supply power to the hydrogen electrolyzer (108, 408). While the use of photovoltaic power is maximized, the intermittent effect of photovoltaics is eliminated, and the function of supply to the hydrogen electrolyzer (108, 408) is maintained to be stable.
Description
本公开通常涉及制氢技术领域,更具体地,涉及制氢系统及其控制方法。The present disclosure generally relates to the technical field of hydrogen production, and more particularly, to a hydrogen production system and a control method thereof.
目前,对于使用太阳能光伏(photovoltaic,PV)能量给电解槽供电来制氢已经有很多研究,这种制氢系统具有非常低的碳足迹。At present, there has been much research on the use of solar photovoltaic (photovoltaic, PV) energy to power electrolyzers to produce hydrogen, which has a very low carbon footprint.
研究大规模制氢系统(通常用于工业生产)的拓扑结构是非常必要的。由于氢电解槽具有低电压和超高电流的特点,因此变流器的拓扑结构应该能够处理超高电流。It is very necessary to study the topology of large-scale hydrogen production systems (usually used in industrial production). Since hydrogen electrolyzers are characterized by low voltage and ultra-high current, the converter topology should be able to handle ultra-high current.
众所周知,光伏具有间歇性(intermittency),产生的功率不稳定,这样会影响氢电解槽的使用寿命。As we all know, photovoltaics are intermittent and the power generated is unstable, which will affect the service life of the hydrogen electrolyzer.
现有技术中针对大功率储氢拓扑的一种解决方案是,并联多个DC/DC变流器来处理氢电解槽的大电流。此外,在每个模块中采用并联开关,可以进一步处理大电流。大功率变流器通常采用IGBT,然而,并联IGBT的功率均流问题面临挑战。One solution to the high-power hydrogen storage topology in the prior art is to connect multiple DC/DC converters in parallel to handle the high current of the hydrogen electrolyzer. In addition, high currents can be further handled by using parallel switches in each module. High-power converters usually use IGBTs. However, the power current sharing problem of parallel IGBTs faces challenges.
在另一种解决方案中,在光伏侧,每个光伏组件都有一个升压变流器。然后,DC/DC变流器向并联DC/AC变流器馈电,并联DC/AC变流器可将DC转换为AC。然后,连接不可控的AC/DC整流器为氢电解槽供电。然而,这种方案有以下缺点:In another solution, on the PV side, each PV module has a boost converter. The DC/DC converter then feeds the parallel DC/AC converter which converts the DC to AC. Then, an uncontrolled AC/DC rectifier is connected to power the hydrogen electrolyzer. However, this solution has the following disadvantages:
1)变换级数相对较高,这可能会影响系统效率。1) The number of transformation stages is relatively high, which may affect the system efficiency.
2)在这种系统中引入了工频变压器,增加了系统体积。2) A power frequency transformer is introduced into this system, which increases the volume of the system.
在又一种解决方案中,每个光伏组件都有一个DC/DC变流器,然后将输出串联起来,为氢电解槽供电。这种方案的主要缺点如下:In yet another solution, each PV module has a DC/DC converter, and the outputs are then connected in series to power the hydrogen electrolyzer. The main disadvantages of this scheme are as follows:
1)每个光伏组件都有自己的DC/DC变流器,这带来了较高的成本,不适用于大功率系统。1) Each photovoltaic module has its own DC/DC converter, which brings high costs and is not suitable for high-power systems.
2)光伏DC/DC变流器串联连接来为氢电解槽供电,这与氢电解槽的低压特性不匹配。2) The photovoltaic DC/DC converter is connected in series to power the hydrogen electrolyzer, which does not match the low-voltage characteristics of the hydrogen electrolyzer.
在再一种解决方案中,系统非常简单,不包含电力电子变流器。然而,在这种解决方案中,电压和功率是不受控制的,这会影响氢电解槽的效率和寿命。In yet another solution, the system is very simple and does not contain power electronic converters. However, in this solution, the voltage and power are not controlled, which affects the efficiency and lifetime of the hydrogen electrolyzer.
发明内容Contents of the invention
在下文中给出关于本发明的简要概述,以便提供关于本发明的某些方面的基本理解。应当理解,这个概述并不是关于本发明的穷举性概述。它并不是意图确定本发明的关键或重要部分,也不是意图限定本发明的范围。其目的仅仅是以简化的形式给出某些概念,以此作为稍后论述的更详细描述的前序。A brief overview of the invention is given below in order to provide a basic understanding of some aspects of the invention. It should be understood that this summary is not an exhaustive overview of the invention. It is not intended to identify key or critical parts of the invention nor to delineate the scope of the invention. Its purpose is merely to present some concepts in a simplified form as a prelude to the more detailed description that is discussed later.
有鉴于此,本发明提出了一种制氢系统,以及针对制氢系统的控制方法。In view of this, the present invention proposes a hydrogen production system and a control method for the hydrogen production system.
根据本公开的一个方面,提供了一种制氢系统,包括:光伏组件、电网、至少一个模块化多电平变流器和氢电解槽,所述模块化多电平变流器包括至少一个相单元,每个相单元包括上桥臂和下桥臂,上桥臂和下桥臂分别包括至少一个功率模块,其中,所述光伏组件连接所述模块化多电平变流器的直流母线侧;所述电网连接所述模块化多电平变流器的交流母线侧;以及所述模块化多电平变流器的功率模块的直流侧输出并联连接在一起向所述氢电解槽供电。According to one aspect of the present disclosure, a hydrogen production system is provided, including: a photovoltaic module, a power grid, at least one modular multilevel converter, and a hydrogen electrolyzer, and the modular multilevel converter includes at least one Each phase unit includes an upper bridge arm and a lower bridge arm, and the upper bridge arm and the lower bridge arm respectively include at least one power module, wherein the photovoltaic module is connected to the DC bus of the modular multilevel converter side; the grid is connected to the AC bus side of the modular multilevel converter; and the DC side outputs of the power modules of the modular multilevel converter are connected in parallel to supply power to the hydrogen electrolyzer .
可选地,在上述方面的一个示例中,所述功率模块采用隔离拓扑电路。Optionally, in an example of the above aspect, the power module adopts an isolation topology circuit.
可选地,在上述方面的一个示例中,所述隔离拓扑电路包括DC/AC和DC/DC二级,其中,所述DC/AC是两电平DC/AC或三电平DC/AC中的任意一种,所述DC/DC是LLC DC/DC和全桥相移DC/DC中的任意一种。Optionally, in an example of the above aspect, the isolated topology circuit includes a DC/AC and a DC/DC two-stage, wherein the DC/AC is a two-level DC/AC or a three-level DC/AC Any one of, the DC/DC is any one of LLC DC/DC and full-bridge phase-shifted DC/DC.
根据本公开的另一方面,提供了一种制氢系统的控制方法,用于对上述制氢系统进行控制,该控制方法包括:调整所述制氢系统的模块化多电平变流器的直流母线侧的电流来跟踪光伏组件的最大功率点,以所述光伏组件的最大功率向氢电解槽供电;以及在所述光伏组件的实际功率小于所述氢电解槽的功率参考值的情况下,由电网向所述氢电解槽提供差额功率,以保持供给所述氢电解槽的功率恒定,其中所述差额功率为氢电解槽的功率参考值与光伏组件的实际功率之差。According to another aspect of the present disclosure, a method for controlling a hydrogen production system is provided, used for controlling the above-mentioned hydrogen production system, the control method includes: adjusting the power of the modular multilevel converter of the hydrogen production system The current on the DC bus side is used to track the maximum power point of the photovoltaic component, and the maximum power of the photovoltaic component is used to supply power to the hydrogen electrolyzer; and when the actual power of the photovoltaic component is less than the power reference value of the hydrogen electrolyzer , the grid provides differential power to the hydrogen electrolyzer to keep the power supplied to the hydrogen electrolyzer constant, wherein the differential power is the difference between the power reference value of the hydrogen electrolyzer and the actual power of the photovoltaic module.
可选地,在上述方面的一个示例中,所述电网侧的功率是双向的,所述控制方法还包括:在所述光伏组件的实际功率大于所述氢电解槽的功率参考值的情况下,将所述光伏组件多产生的功率馈送给所述电网。Optionally, in an example of the above aspect, the power on the grid side is bidirectional, and the control method further includes: when the actual power of the photovoltaic module is greater than the power reference value of the hydrogen electrolyzer , feeding the excess power generated by the photovoltaic components to the grid.
根据本公开的另一方面,提供了一种制氢系统,包括:光伏组件、电网、至少一个模块化多电平变流器,氢电解槽、光伏侧DC/AC变换器和网侧DC/AC变换器,所述模块化多电平变流器包括至少一个相单元,每个相单元包括上桥臂和下桥臂,上桥臂和下桥臂分别包括至少一个功率模块,其中,所述光伏组件经由所述光伏侧DC/AC变换器连接所述模块化多电平变流器的交流母线侧;所述电网经由所述网侧DC/AC变换器连接所述模块 化多电平变流器的直流母线侧;以及所述模块化多电平变流器的功率模块的直流侧输出并联连接在一起向所述氢电解槽供电。According to another aspect of the present disclosure, a hydrogen production system is provided, including: a photovoltaic module, a power grid, at least one modular multilevel converter, a hydrogen electrolyzer, a photovoltaic-side DC/AC converter, and a grid-side DC/AC converter. In an AC converter, the modular multilevel converter includes at least one phase unit, each phase unit includes an upper bridge arm and a lower bridge arm, and the upper bridge arm and the lower bridge arm respectively include at least one power module, wherein the The photovoltaic module is connected to the AC bus side of the modular multilevel converter through the photovoltaic side DC/AC converter; the power grid is connected to the modular multilevel converter through the grid side DC/AC converter The DC bus side of the converter; and the DC side output of the power module of the modular multilevel converter are connected in parallel to supply power to the hydrogen electrolyzer.
与现有技术相比,本发明的技术方案具有以下优势中的至少一项。Compared with the prior art, the technical solution of the present invention has at least one of the following advantages.
采用电网光伏混合供电,在最大化使用光伏功率的同时,利用电网提供功率来消除光伏间歇性的影响,保持给氢电解槽提供的功率稳定;Using grid photovoltaic hybrid power supply, while maximizing the use of photovoltaic power, use the power provided by the grid to eliminate the intermittent impact of photovoltaic, and maintain the stability of the power provided to the hydrogen electrolyzer;
为氢电解槽提供了超高电流和低电压输出;Provide ultra-high current and low voltage output for hydrogen electrolyzer;
具有冗余的模块化设计;Modular design with redundancy;
采用模块化多电平变流器,易于配置,以匹配电网、光伏和氢电解槽的不同额定功率;Using modular multilevel converters, it is easy to configure to match different power ratings of grid, photovoltaic and hydrogen electrolyzer;
采用高频变压器隔离,系统体积小;High-frequency transformer isolation is adopted, and the system volume is small;
效率高,转换级数相对较少。High efficiency, relatively few conversion stages.
参照下面结合附图对本发明实施例的说明,会更加容易地理解本发明的以上和其它目的、特点和优点。附图中的部件只是为了示出本发明的原理。在附图中,相同的或类似的技术特征或部件将采用相同或类似的附图标记来表示。附图中:The above and other objects, features and advantages of the present invention will be more easily understood with reference to the following description of the embodiments of the present invention in conjunction with the accompanying drawings. The components in the drawings are only to illustrate the principles of the invention. In the drawings, the same or similar technical features or components will be denoted by the same or similar reference numerals. In the attached picture:
图1为根据本发明实施例的制氢系统的示例性拓扑图;Fig. 1 is an exemplary topological diagram of a hydrogen production system according to an embodiment of the present invention;
图2A为根据本发明实施例的制氢系统的控制方法的示例性过程的流程图;2A is a flowchart of an exemplary process of a method for controlling a hydrogen production system according to an embodiment of the present invention;
图2B为根据本发明实施例的制氢系统的控制示意图;Fig. 2B is a control schematic diagram of a hydrogen production system according to an embodiment of the present invention;
图2C为对根据本发明实施例的制氢系统的具体控制示意图;Fig. 2C is a schematic diagram of specific control of the hydrogen production system according to an embodiment of the present invention;
图3为根据本发明另一实施例的制氢系统的示例性拓扑图;Fig. 3 is an exemplary topological diagram of a hydrogen production system according to another embodiment of the present invention;
图4A为根据本发明再一个实施例的制氢系统的示例性拓扑图;Fig. 4A is an exemplary topological diagram of a hydrogen production system according to yet another embodiment of the present invention;
图4B为对根据本发明再一个实施例的制氢系统的具体控制示意图。Fig. 4B is a schematic diagram of the specific control of the hydrogen production system according to another embodiment of the present invention.
其中,附图标记如下:Wherein, the reference signs are as follows:
100、300、400:制氢系统 102、302、402:光伏组件100, 300, 400: hydrogen production system 102, 302, 402: photovoltaic modules
104、304、404:电网 106、306、306-1、306-2、406:模块化104, 304, 404: power grid 106, 306, 306-1, 306-2, 406: modular
多电平变流器Multilevel Converter
108、308、408:氢电解槽 1062、4062:相单元108, 308, 408: hydrogen electrolyzer 1062, 4062: phase unit
1062-1、4062-1:上桥臂 1062-2、4062-2:下桥臂1062-1, 4062-1: upper bridge arm 1062-2, 4062-2: lower bridge arm
1060、4060:功率模块 DC-BUS:直流母线1060, 4060: power module DC-BUS: DC bus
AC-BUS:交流母线侧 200:控制方法AC-BUS: AC bus side 200: Control method
S202、S204、S206:步骤 410:光伏侧DC/AC变换器S202, S204, S206: step 410: photovoltaic side DC/AC converter
412:网侧DC/AC变换器412: Grid side DC/AC converter
现在将参考示例实施方式讨论本文描述的主题。应该理解,讨论这些实施方式只是为了使得本领域技术人员能够更好地理解从而实现本文描述的主题,并非是对权利要求书中所阐述的保护范围、适用性或者示例的限制。可以在不脱离本公开内容的保护范围的情况下,对所讨论的元素的功能和排列进行改变。各个示例可以根据需要,省略、替代或者添加各种过程或组件。例如,所描述的方法可以按照与所描述的顺序不同的顺序来执行,以及各个步骤可以被添加、省略或者组合。另外,相对一些示例所描述的特征在其它例子中也可以进行组合。The subject matter described herein will now be discussed with reference to example implementations. It should be understood that the discussion of these implementations is only to enable those skilled in the art to better understand and realize the subject matter described herein, and is not intended to limit the protection scope, applicability or examples set forth in the claims. Changes may be made in the function and arrangement of elements discussed without departing from the scope of the disclosure. Various examples may omit, substitute, or add various procedures or components as needed. For example, the methods described may be performed in an order different from that described, and various steps may be added, omitted, or combined. Additionally, features described with respect to some examples may also be combined in other examples.
如本文中使用的,术语“包括”及其变型表示开放的术语,含义是“包括但不限于”。术语“基于”表示“至少部分地基于”。术语“一个实施例”和“一实施例”表示“至少一个实施例”。术语“另一个实施例”表示“至少一个其他实施例”。术语“第一”、“第二”等可以指代不同的或相同的对象。下面可以包括其他的定义,无论是明确的还是隐含的。除非上下文中明确地指明,否则一个术语的定义在整个说明书中是一致的。As used herein, the term "comprising" and its variants represent open terms meaning "including but not limited to". The term "based on" means "based at least in part on". The terms "one embodiment" and "an embodiment" mean "at least one embodiment." The term "another embodiment" means "at least one other embodiment." The terms "first", "second", etc. may refer to different or the same object. The following may include other definitions, either express or implied. Unless the context clearly indicates otherwise, the definition of a term is consistent throughout the specification.
有鉴于此,本发明基于如何能够最大限度地利用PV功率,同时保持氢电解槽的功率稳定,以消除PV间歇的影响的考虑,提出了一种光伏-电网混合供电的制氢系统,在最大化使用光伏功率的同时,利用电网提供功率来消除光伏间歇性的影响,保持给氢电解槽提供稳定的功率。In view of this, the present invention is based on the consideration of how to maximize the use of PV power while keeping the power of the hydrogen electrolyzer stable to eliminate the intermittent impact of PV. A hydrogen production system powered by a photovoltaic-grid hybrid is proposed. While maximizing the use of photovoltaic power, the power provided by the grid is used to eliminate the intermittent impact of photovoltaics and maintain stable power for the hydrogen electrolyzer.
下面将结合附图来具体描述根据本公开的实施例的制氢系统及其控制方法。A hydrogen production system and a control method thereof according to an embodiment of the present disclosure will be described in detail below with reference to the accompanying drawings.
图1为根据本发明实施例的制氢系统100的示例性拓扑图。FIG. 1 is an exemplary topological diagram of a hydrogen production system 100 according to an embodiment of the present invention.
如图1所示,制氢系统100包括光伏组件102、电网104、至少一个模块化多电平变流器106和氢电解槽108。As shown in FIG. 1 , the hydrogen production system 100 includes a photovoltaic module 102 , a grid 104 , at least one modular multilevel converter 106 and a hydrogen electrolyzer 108 .
在图1中,模块化多电平变流器106包括三个相单元1062,每个相单元包括上桥臂和下桥臂,上桥臂和下桥臂分别包括至少一个功率模块1060。In FIG. 1 , the modular multilevel converter 106 includes three phase units 1062 , each phase unit includes an upper bridge arm and a lower bridge arm, and the upper bridge arm and the lower bridge arm respectively include at least one power module 1060 .
本领域技术人员可以理解,模块化多电平变流器106所包括的相单元的数目也可以不限于三个。Those skilled in the art can understand that the number of phase units included in the modular multilevel converter 106 may not be limited to three.
在制氢系统100中,光伏组件102连接模块化多电平变流器106的直流母线侧DC- BUS;电网104连接所述模块化多电平变流器106的交流母线侧AC-BUS;模块化多电平变流器106的功率模块的直流侧输出并联连接在一起向氢电解槽108供电。In the hydrogen production system 100, the photovoltaic module 102 is connected to the DC bus side DC-BUS of the modular multilevel converter 106; the grid 104 is connected to the AC bus side AC-BUS of the modular multilevel converter 106; The DC side outputs of the power modules of the modular multilevel converter 106 are connected in parallel to supply power to the hydrogen electrolyzer 108 .
在制氢系统100中,由于所有功率模块的直流侧输出都并联在一起,因此可以处理氢电解槽108的超高电流;并且由于输出都连接在一起,因此功率模块要采用隔离拓扑电路。隔离拓扑电路包括DC/AC和DC/DC二级,DC/AC例如可以是两电平DC/AC或三电平DC/AC,DC/DC可以是LLC DC/DC或全桥相移DC/DC中的一种。本领域技术人员也可以根据需要选择其他形式的隔离拓扑电路,而不限于这里所述的拓扑形式。In the hydrogen production system 100, since the DC side outputs of all power modules are connected in parallel, the ultra-high current of the hydrogen electrolyzer 108 can be handled; and since the outputs are all connected together, the power modules should adopt an isolated topology circuit. The isolation topology circuit includes DC/AC and DC/DC secondary, DC/AC can be, for example, two-level DC/AC or three-level DC/AC, and DC/DC can be LLC DC/DC or full-bridge phase-shifted DC/ One of a kind in DC. Those skilled in the art can also choose other forms of isolation topology circuits according to needs, and are not limited to the topology forms described here.
对于每个功率模块的功率平衡,可以采用传统的功率平衡方法,例如基于CAN的平均电流控制和下垂控制。For the power balance of each power module, traditional power balance methods can be used, such as CAN-based average current control and droop control.
可以理解,对于大功率变流器,冗余和模块化设计非常重要,即使一个模块出现故障也不会影响整个系统的运行;此外,大容量和可扩展性对于系统来说也非常重要。It can be understood that for high-power converters, redundancy and modular design are very important, even if a module fails, it will not affect the operation of the entire system; in addition, large capacity and scalability are also very important for the system.
根据本发明的制氢系统100基于模块化多电平变流器(MMC),因此继承了MMC的特征。例如,可以根据电网、光伏以及氢电解槽的额定功率等参数来设置模块化多电平变流器的相单元的数目,并且每个桥臂的功率模块的数量也可以根据需要而确定,因此根据本发明的制氢系统具有冗余能力;并且由于基于模块化设计而易于扩展。The hydrogen production system 100 according to the invention is based on a modular multilevel converter (MMC), thus inheriting the characteristics of the MMC. For example, the number of phase units of the modular multilevel converter can be set according to the power grid, photovoltaic and hydrogen electrolyzer’s rated power, and the number of power modules in each bridge arm can also be determined according to the needs, so The hydrogen production system according to the present invention has redundancy capability; and is easy to expand due to the modular design.
下面参照图2A-2C说明根据本发明实施例的制氢系统的控制方法。The control method of the hydrogen production system according to the embodiment of the present invention will be described below with reference to FIGS. 2A-2C .
图2A为根据本发明实施例的制氢系统的控制方法200的示例性过程的流程图。Fig. 2A is a flowchart of an exemplary process of a method 200 for controlling a hydrogen production system according to an embodiment of the present invention.
如图2A所示,首先,在步骤S202中,调整制氢系统100的模块化多电平变流器106的直流母线DC-BUS的电流来跟踪光伏组件102的最大功率点,以光伏组件102的最大功率向氢电解槽108供电。As shown in Figure 2A, first, in step S202, the current of the DC-BUS of the modular multilevel converter 106 of the hydrogen production system 100 is adjusted to track the maximum power point of the photovoltaic module 102, and the photovoltaic module 102 The maximum power of is supplied to the hydrogen electrolyzer 108.
在步骤S204中,在光伏组件102的功率小于氢电解槽108所需功率的情况下,由电网104向氢电解槽108提供差额功率,以保持供给氢电解槽108的功率恒定。In step S204 , when the power of the photovoltaic module 102 is less than the required power of the hydrogen electrolyzer 108 , the power grid 104 provides differential power to the hydrogen electrolyzer 108 to keep the power supplied to the hydrogen electrolyzer 108 constant.
这里的差额功率是指氢电解槽108所需功率与光伏组件102提供的功率之差。The differential power here refers to the difference between the power required by the hydrogen electrolyzer 108 and the power provided by the photovoltaic module 102 .
图2B为根据本发明实施例的制氢系统的控制示意图,图2C为对制氢系统的每一个桥臂电压进行控制的示意图。Fig. 2B is a schematic diagram of controlling the hydrogen production system according to an embodiment of the present invention, and Fig. 2C is a schematic diagram of controlling the voltage of each bridge arm of the hydrogen production system.
在图2B和2C中,abc/dq0表示从abc坐标变换到dq0坐标,P
G*表示电网侧功率给定(也称为参考值,以下相同),P
H2*表示氢电解槽功率给定,P
PV*表示光伏功率给定,P
G表示电网侧功率反馈(也可以称为实际值,以下相同),i
gd*表示电网侧d轴电流给定,i
gd表示电网侧d轴电流反馈,d
d*表示d轴占空比给定,i
gq*表示电网侧q轴电流给定,i
gq 表示电网侧q轴电流反馈,d
q*表示q轴占空比给定,i
g0*:表示电网侧0轴电流给定,i
g0表示电网侧0轴电流反馈,d
0*表示0轴占空比给定,P
MPPT*表示光伏最大功率跟踪指令,P
PV表示光伏功率反馈,i
dc*表示直流侧电流给定,i
dc表示直流侧电流反馈,d
dc*表示直流侧产生对应占空比给定,i
loop1*表示环流回路loop1电流给定,i
loop1表示环流回路loop1电流反馈,d
loop1*表示环流回路loop1产生对应占空比给定,i
loop2*表示环流回路loop2电流给定,i
loop2表示环流回路loop2电流反馈,d
loop2*表示环流回路loop2产生对应占空比给定,V
ap表示ap桥臂电压,V
ap*表示ap桥臂电压给定,V
bp表示bp桥臂电压,V
bp*表示bp桥臂电压给定,V
cp表示cp桥臂电压,V
cp*表示cp桥臂电压给定,V
an表示an桥臂电压,V
an*表示an桥臂电压给定,V
bn表示bn桥臂电压,V
bn*表示bn桥臂电压给定,V
cn表示cn桥臂电压,V
cn*表示cn桥臂电压给定,210表示支路能量平衡环路。
In Figures 2B and 2C, abc/dq0 represents the transformation from abc coordinates to dq0 coordinates, PG * represents the given power on the grid side (also called reference value, the same below), and P H2 * represents the given power of the hydrogen electrolyzer, P PV * means photovoltaic power reference, PG means grid side power feedback (also called actual value, the same below), igd * means grid side d-axis current setting, igd means grid side d-axis current feedback, d d * means d-axis duty cycle setting, i gq * means grid side q-axis current setting, i gq means grid side q-axis current feedback, d q * means q-axis duty cycle setting, i g0 *: Indicates the 0-axis current setting on the grid side, i g0 indicates the 0-axis current feedback on the grid side, d 0 * indicates the 0-axis duty cycle setting, P MPPT * indicates the photovoltaic maximum power tracking command, P PV indicates photovoltaic power feedback, i dc * indicates the current setting of the DC side, i dc indicates the current feedback of the DC side, d dc * indicates the corresponding duty cycle setting of the DC side, i loop1 * indicates the current setting of the loop1 of the circulation loop, and i loop1 indicates the current feedback of the loop1 of the circulation loop, d loop1 * indicates that the circulating current loop loop1 generates the corresponding duty ratio setting, i loop2 * indicates the circulating current loop loop2 current setting, i loop2 indicates the circulating current loop loop2 current feedback, d loop2 * indicates that the circulating current loop loop2 generates the corresponding duty ratio setting, V ap means ap bridge arm voltage, V ap * means ap bridge arm voltage given, V bp means bp bridge arm voltage, V bp * means bp bridge arm voltage given, V cp means cp bridge arm voltage, V cp * means cp bridge arm voltage given, V an means an bridge arm voltage, V an * means an bridge arm voltage given, V bn means bn bridge arm voltage, V bn * means bn bridge arm voltage given, V cn means cn bridge arm voltage Arm voltage, V cn * means cn bridge arm voltage given, 210 means branch energy balance loop.
可以理解,通过控制制氢系统100的模块化多电平变流器106的直流母线DC-BUS的电流i
dc可以实现光伏的最大功率点跟踪(Maximum Power Point Tracking(MPPT))。因此,MTTP环路输出设定为为i
dc的基准电流i
dc*。
It can be understood that maximum power point tracking (Maximum Power Point Tracking (MPPT)) of photovoltaics can be realized by controlling the current i dc of the DC-BUS of the modular multilevel converter 106 of the hydrogen production system 100 . Therefore, the MTTP loop output is set to be the reference current i dc * of i dc .
通过图2C所示的控制方法,可以跟踪光伏组件的最大功率点,以光伏组件的最大功率向氢电解槽供电。Through the control method shown in Figure 2C, the maximum power point of the photovoltaic module can be tracked, and the hydrogen electrolyzer can be supplied with the maximum power of the photovoltaic module.
电网侧功率给定被设置为氢电解槽功率给定减去光伏组件的功率反馈,即P
G*=P
H2*-P
PV。
The grid-side power reference is set to the power reference of the hydrogen electrolyzer minus the power feedback of the photovoltaic module, that is, PG *= PH2 *-P PV.
本领域技术人员结合图2A-2C可以理解对根据本发明的制氢系统进行控制的具体过程,在此不再详述。Those skilled in the art can understand the specific process of controlling the hydrogen production system according to the present invention with reference to FIGS. 2A-2C , which will not be described in detail here.
通过这样的方式,可以保持提供给氢电解槽的功率是恒定的,从而消除PV间歇对制氢系统的影响。In this way, the power provided to the hydrogen electrolyzer can be kept constant, thereby eliminating the impact of PV intermittent on the hydrogen production system.
优选地,电网侧的功率还可以是双向的。控制方法200还可以包括步骤S206,当光伏组件102的功率反馈大于氢电解槽108的功率给定的情况下,可以将光伏组件102多产生的功率馈送给电网104。Preferably, the power on the grid side can also be bidirectional. The control method 200 may further include step S206 , when the power feedback of the photovoltaic assembly 102 is greater than the given power of the hydrogen electrolyzer 108 , the excess power generated by the photovoltaic assembly 102 may be fed to the grid 104 .
通过这样的方式,根据本发明的制氢系统可以使得光伏组件所产生的电能的利用率最大化,同时可以保证供给氢电解槽的电能保持稳定。In this way, the hydrogen production system according to the present invention can maximize the utilization rate of the electric energy generated by the photovoltaic module, and at the same time ensure that the electric energy supplied to the hydrogen electrolyzer remains stable.
图3示出了根据本发明另一实施例的制氢系统300的示例性拓扑图。FIG. 3 shows an exemplary topology diagram of a hydrogen production system 300 according to another embodiment of the present invention.
图3的制氢系统300包括光伏组件302、电网304和氢电解槽308。The hydrogen production system 300 in FIG. 3 includes a photovoltaic module 302 , a grid 304 and a hydrogen electrolyzer 308 .
其中,光伏组件302、电网304和氢电解槽308的结构和功能与以上参照图1所描述的光伏组件102、电网104和氢电解槽108的结构和功能类似,在此不再赘述。The structures and functions of the photovoltaic module 302, the grid 304, and the hydrogen electrolyzer 308 are similar to those of the photovoltaic module 102, the grid 104, and the hydrogen electrolyzer 108 described above with reference to FIG. 1 , and will not be repeated here.
除此之外,在图3的制氢系统300中,包括两个模块化多电平变流器306-1和306-2。Besides, in the hydrogen production system 300 in FIG. 3 , two modular multilevel converters 306-1 and 306-2 are included.
当氢电解槽的功率增加时,氢电解槽的输入电压也增加。为了匹配更高的氢电解槽电压,提供了如图3所示的制氢系统的另一种解决方案。在图3所示的制氢系统中,采用了两个模块化多电平变流器,相单元的数目从3个增加为6个。两个模块化多电平变流器的功率模块的并联输出电压串联连接在一起以匹配氢电解槽的更高的电压。When the power of the hydrogen electrolyzer increases, the input voltage of the hydrogen electrolyzer also increases. In order to match the higher voltage of the hydrogen electrolyzer, another solution of the hydrogen production system as shown in Fig. 3 is provided. In the hydrogen production system shown in Figure 3, two modular multilevel converters are used, and the number of phase units is increased from three to six. The parallel output voltages of the power modules of the two modular multilevel converters are connected together in series to match the higher voltage of the hydrogen electrolyzer.
本领域技术人员还可以根据氢电解槽的功率需求而设置更多数目的模块化多电平变流器,而不限于图3所示的两个模块化多电平变流器。Those skilled in the art can also set more modular multilevel converters according to the power requirements of the hydrogen electrolyzer, not limited to the two modular multilevel converters shown in FIG. 3 .
根据本实施例的制氢系统可以适用于具有较高功率的氢电解槽,并且可以根据不同额定功率的氢电解槽的需要而设置模块化多电平变流器的数目、相单元的数目以及功率模块的数目,在此不再详述。The hydrogen production system according to this embodiment can be applied to hydrogen electrolyzers with higher power, and the number of modular multilevel converters, the number of phase units, and The number of power modules will not be described in detail here.
图4示出了根据本发明再一个实施例的制氢系统400的示例性拓扑图。Fig. 4 shows an exemplary topology diagram of a hydrogen production system 400 according to yet another embodiment of the present invention.
如图4所示,制氢系统400包括光伏组件402、电网404、至少一个模块化多电平变流器406和氢电解槽408。As shown in FIG. 4 , the hydrogen production system 400 includes a photovoltaic module 402 , a grid 404 , at least one modular multilevel converter 406 and a hydrogen electrolyzer 408 .
其中,光伏组件402、电网404、模块化多电平变流器406和氢电解槽408的结构和功能与以上参照图1所描述的光伏组件102、电网104、至少一个模块化多电平变流器106和氢电解槽108的类似,在此不再赘述。Among them, the structure and function of the photovoltaic assembly 402, the grid 404, the modular multilevel converter 406 and the hydrogen electrolyzer 408 are the same as those of the photovoltaic assembly 102, the grid 104, at least one modular multilevel converter described above with reference to FIG. The current flow device 106 is similar to the hydrogen electrolyzer 108, and will not be repeated here.
除此之外,制氢系统400还包括光伏侧DC/AC变换器410和网侧DC/AC变换器412,光伏组件402经由光伏侧DC/AC变换器410连接模块化多电平变流器406的交流母线侧;电网404经由网侧DC/AC变换器412连接模块化多电平变流器406的直流母线侧;模块化多电平变流器406的功率模块的直流侧输出并联连接在一起向氢电解槽408供电。In addition, the hydrogen production system 400 also includes a photovoltaic side DC/AC converter 410 and a grid side DC/AC converter 412, and the photovoltaic module 402 is connected to a modular multilevel converter via the photovoltaic side DC/AC converter 410 The AC bus side of 406; the power grid 404 is connected to the DC bus side of the modular multilevel converter 406 via the grid side DC/AC converter 412; the DC side outputs of the power modules of the modular multilevel converter 406 are connected in parallel together supply power to the hydrogen electrolyzer 408 .
在根据本发明的该实施例的制氢系统中,电网和光伏组件交换了连接位置,提供了一种不同的拓扑。本领域技术人员可以根据需要,选择适当的制氢系统的拓扑。In the hydrogen production system according to this embodiment of the present invention, the connection positions of the grid and the photovoltaic modules are exchanged, providing a different topology. Those skilled in the art can select an appropriate topology of the hydrogen production system according to needs.
在图4所示的制氢系统的拓扑中,本领域技术人员也可以根据需要设置两个MMC或者更多个MMC,多个MMC的具体连接方式和操作过程与参照图3所描述的制氢系统类似,在此不再赘述。In the topology of the hydrogen production system shown in Figure 4, those skilled in the art can also set up two MMCs or more MMCs as required, and the specific connection mode and operation process of multiple MMCs are the same as the hydrogen production described in Figure 3 The system is similar and will not be repeated here.
图4B是针对图4A所示的制氢系统拓扑的控制示意图。Fig. 4B is a control diagram for the hydrogen production system topology shown in Fig. 4A.
在图4A和4B的中,i
d*表示光伏逆变器侧d轴电流给定,i
d表示光伏逆变器侧d轴电流反馈,i
q*表示光伏逆变器侧q轴电流给定,i
q表示光伏逆变器侧q轴电流反馈,i
0*表示光伏逆变器侧0轴电流给定,i
0表示光伏逆变器侧0轴电流反馈,i
dc*表示电网侧母 线电流给定,i
dc表示电网侧母线电流反馈,其余变量的含义与图2A-2C中所示的变量的含义相同,在此不再赘述。
In Figures 4A and 4B, id * represents the d-axis current setting on the photovoltaic inverter side, id represents the d-axis current feedback on the photovoltaic inverter side, and i q * represents the q-axis current setting on the photovoltaic inverter side , i q represents the q-axis current feedback on the PV inverter side, i 0 * represents the 0-axis current setting on the PV inverter side, i 0 represents the 0-axis current feedback on the PV inverter side, and i dc * represents the bus current on the grid side Given, i dc represents the grid-side bus current feedback, and the meanings of other variables are the same as those shown in Figs. 2A-2C , and will not be repeated here.
本领域技术人员可以按照图4B所示的控制示意图来对图4A所示的制氢系统进行控制,实现以光伏组件的最大功率向氢电解槽供电,并且由电网向氢电解槽提供差额功率,以保持供给氢电解槽的功率恒定,在此不再详述。Those skilled in the art can control the hydrogen production system shown in FIG. 4A according to the control schematic diagram shown in FIG. 4B, so as to realize power supply to the hydrogen electrolyzer with the maximum power of the photovoltaic module, and provide the differential power to the hydrogen electrolyzer from the power grid. In order to keep the power supplied to the hydrogen electrolyzer constant, it will not be described in detail here.
与现有技术相比,本发明的技术方案具有以下优势中的至少一项。Compared with the prior art, the technical solution of the present invention has at least one of the following advantages.
采用电网光伏混合供电,在最大化使用光伏功率的同时,利用电网提供功率来消除光伏间歇性的影响,保持给氢电解槽提供的功率稳定;Using grid photovoltaic hybrid power supply, while maximizing the use of photovoltaic power, use the power provided by the grid to eliminate the intermittent impact of photovoltaic, and maintain the stability of the power provided to the hydrogen electrolyzer;
为氢电解槽提供了超高电流和低电压输出;Provide ultra-high current and low voltage output for hydrogen electrolyzer;
具有冗余的模块化设计;Modular design with redundancy;
采用模块化多电平变流器,易于配置,以匹配电网、光伏和氢电解槽的不同额定功率;Using modular multilevel converters, it is easy to configure to match different power ratings of grid, photovoltaic and hydrogen electrolyzer;
采用高频变压器隔离,体积小;High-frequency transformer isolation, small size;
效率高,转换级数相对较少。High efficiency, relatively few conversion stages.
应当理解的是,本说明书中的各个实施例均采用递进的方式来描述,各个实施例之间相同或相似的部分相互参见即可,每个实施例重点说明的都是与其它实施例的不同之处。It should be understood that each embodiment in this specification is described in a progressive manner, and the same or similar parts of each embodiment can be referred to each other, and each embodiment focuses on the difference with other embodiments. the difference.
上述各系统结构图中不是所有的单元都是必须的,可以根据实际的需要忽略某些单元。上述各实施例中描述的装置结构可以是物理结构,也可以是逻辑结构,即,有些单元可能由同一物理实体实现,或者,有些单元可能分别由多个物理实体实现,或者,可以由多个独立设备中的某些部件共同实现。Not all units in the above system structure diagrams are necessary, and some units can be ignored according to actual needs. The device structures described in the above embodiments may be physical structures or logical structures, that is, some units may be implemented by the same physical entity, or some units may be respectively implemented by multiple physical entities, or may be implemented by multiple physical entities. Certain components in individual devices are implemented together.
上面结合附图阐述的具体实施方式描述了示例性实施例,但并不表示可以实现的或者落入权利要求书的保护范围的所有实施例。在整个本说明书中使用的术语“示例性”意味着“用作示例、实例或例示”,并不意味着比其它实施例“优选”或“具有优势”。出于提供对所描述技术的理解的目的,具体实施方式包括具体细节。然而,可以在没有这些具体细节的情况下实施这些技术。在一些实例中,为了避免对所描述的实施例的概念造成难以理解,公知的结构和装置以框图形式示出。The specific implementation manner described above in conjunction with the accompanying drawings describes exemplary embodiments, but does not represent all embodiments that can be realized or fall within the protection scope of the claims. As used throughout this specification, the term "exemplary" means "serving as an example, instance, or illustration," and does not mean "preferred" or "advantaged" over other embodiments. The detailed description includes specific details for the purpose of providing an understanding of the described technology. However, the techniques may be practiced without these specific details. In some instances, well-known structures and devices are shown in block diagram form in order to avoid obscuring the concepts of the described embodiments.
本公开内容的上述描述被提供来使得本领域任何普通技术人员能够实现或者使用本公开内容。对于本领域普通技术人员来说,对本公开内容进行的各种修改是显而易见的,并且,也可以在不脱离本公开内容的保护范围的情况下,将本文所定义的一般性原理应用于其它变型。因此,本公开内容并不限于本文所描述的示例和设计,而是与符合本文公开的 原理和新颖性特征的最广范围相一致。The above description of the present disclosure is provided to enable any person of ordinary skill in the art to make or use the present disclosure. Various modifications to this disclosure will be readily apparent to those skilled in the art, and the general principles defined herein can also be applied to other variants without departing from the scope of this disclosure. . Thus, the disclosure is not intended to be limited to the examples and designs described herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included in the scope of the present invention. within the scope of protection.
Claims (8)
- 制氢系统(100),包括:光伏组件(102)、电网(104)、至少一个模块化多电平变流器(106)和氢电解槽(108),所述模块化多电平变流器(106)包括至少一个相单元(1062),每个相单元(1062)包括上桥臂(1062-1)和下桥臂(1062-2),上桥臂(1062-1)和下桥臂(1062-2)分别包括至少一个功率模块(1060),其中,A hydrogen production system (100), comprising: a photovoltaic module (102), a grid (104), at least one modular multilevel converter (106) and a hydrogen electrolyzer (108), the modular multilevel converter The device (106) includes at least one phase unit (1062), each phase unit (1062) includes an upper bridge arm (1062-1) and a lower bridge arm (1062-2), and an upper bridge arm (1062-1) and a lower bridge arm The arms (1062-2) respectively include at least one power module (1060), wherein,所述光伏组件(102)连接所述模块化多电平变流器(106)的直流母线侧(DC-BUS);The photovoltaic module (102) is connected to the DC bus side (DC-BUS) of the modular multilevel converter (106);所述电网(104)连接所述模块化多电平变流器(106)的交流母线侧(AC-BUS);以及The grid (104) is connected to the AC bus side (AC-BUS) of the modular multilevel converter (106); and所述模块化多电平变流器(106)的功率模块(1060)的直流侧输出并联连接在一起向所述氢电解槽(108)供电。The DC side outputs of the power modules (1060) of the modular multilevel converter (106) are connected in parallel to supply power to the hydrogen electrolyzer (108).
- 如权利要求1所述的制氢系统(100),其中,所述功率模块(1060)采用隔离拓扑电路。The hydrogen production system (100) according to claim 1, wherein the power module (1060) adopts an isolated topology circuit.
- 如权利要求2所述的制氢系统(100),其中,所述隔离拓扑电路包括DC/AC和DC/DC二级,其中,所述DC/AC是两电平DC/AC或三电平DC/AC中的任意一种,所述DC/DC是LLC DC/DC和全桥相移DC/DC中的任意一种。The hydrogen production system (100) according to claim 2, wherein the isolated topological circuit comprises DC/AC and DC/DC two stages, wherein the DC/AC is two-level DC/AC or three-level Any one of DC/AC, the DC/DC is any one of LLC DC/DC and full-bridge phase-shifted DC/DC.
- 制氢系统的控制方法,用于对根据权利要求1-3中任意一项所述的制氢系统进行控制,所述控制方法包括:A control method for a hydrogen production system, used to control the hydrogen production system according to any one of claims 1-3, the control method comprising:调整所述制氢系统的模块化多电平变流器的直流母线侧的电流来跟踪光伏组件的最大功率点,以所述光伏组件的最大功率向氢电解槽供电;以及adjusting the current on the DC bus side of the modular multilevel converter of the hydrogen production system to track the maximum power point of the photovoltaic module, and supplying power to the hydrogen electrolyzer with the maximum power of the photovoltaic module; and在所述光伏组件的实际功率小于所述氢电解槽的功率参考值的情况下,由电网向所述氢电解槽提供差额功率,以保持供给所述氢电解槽的功率恒定,其中所述差额功率为氢电解槽的功率参考值与光伏组件的实际功率之差。In the case that the actual power of the photovoltaic module is less than the power reference value of the hydrogen electrolyzer, the grid provides a balance power to the hydrogen electrolyzer to keep the power supplied to the hydrogen electrolyzer constant, wherein the difference The power is the difference between the power reference value of the hydrogen electrolyzer and the actual power of the photovoltaic module.
- 如权利要求4所述的方法,其中,所述电网侧的功率是双向的,所述控制方法还包括:The method according to claim 4, wherein the power on the grid side is bidirectional, and the control method further comprises:在所述光伏组件的实际功率大于所述氢电解槽的功率参考值的情况下,将所述光伏组件多产生的功率馈送给所述电网。In the case that the actual power of the photovoltaic component is greater than the power reference value of the hydrogen electrolyzer, the excess power generated by the photovoltaic component is fed to the grid.
- 制氢系统(400),包括:光伏组件(402)、电网(404)、至少一个模块化多电平变流器(406),氢电解槽(408)、光伏侧DC/AC变换器(410)和网侧DC/AC变换器(412),所述模块化多电平变流器(406)包括至少一个相单元(4062),每个相单元包括上桥臂(4062-1)和下桥臂(4062-2),上桥臂(4062-1)和下桥臂(4062-2)分别包括至少一个功率模块(4060),其中,A hydrogen production system (400), including: a photovoltaic module (402), a grid (404), at least one modular multilevel converter (406), a hydrogen electrolyzer (408), a photovoltaic side DC/AC converter (410 ) and a grid-side DC/AC converter (412), the modular multilevel converter (406) includes at least one phase unit (4062), each phase unit includes an upper bridge arm (4062-1) and a lower The bridge arm (4062-2), the upper bridge arm (4062-1) and the lower bridge arm (4062-2) respectively include at least one power module (4060), wherein,所述光伏组件(402)经由所述光伏侧DC/AC变换器(410)连接所述模块化多电平变流器(406)的交流母线侧(AC-BUS);The photovoltaic module (402) is connected to the AC bus side (AC-BUS) of the modular multilevel converter (406) via the photovoltaic side DC/AC converter (410);所述电网经由所述网侧DC/AC变换器(412)连接所述模块化多电平变流器(406)的直流母线侧(DC-BUS);以及The grid is connected to the DC bus side (DC-BUS) of the modular multilevel converter (406) via the grid-side DC/AC converter (412); and所述模块化多电平变流器(406)的功率模块(4060)的直流侧输出并联连接在一起向所述氢电解槽(408)供电。The DC side outputs of the power modules (4060) of the modular multilevel converter (406) are connected in parallel to supply power to the hydrogen electrolyzer (408).
- 如权利要求6所述的制氢系统(400),其中,所述功率模块(4060)采用隔离拓扑电路。The hydrogen production system (400) according to claim 6, wherein the power module (4060) adopts an isolated topology circuit.
- 如权利要求6所述的制氢系统(400),其中,所述隔离拓扑电路包括DC/AC和DC/DC二级,其中,所述DC/AC是两电平DC/AC或三电平DC/AC中的任意一种,所述DC/DC是LLC DC/DC和全桥相移DC/DC中的任意一种。The hydrogen production system (400) according to claim 6, wherein the isolated topological circuit comprises DC/AC and DC/DC two stages, wherein the DC/AC is two-level DC/AC or three-level Any one of DC/AC, the DC/DC is any one of LLC DC/DC and full-bridge phase-shifted DC/DC.
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Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103501020A (en) * | 2013-10-12 | 2014-01-08 | 电子科技大学 | Hybrid power supply system consisting of mains supply network and photovoltaic assembly and control method thereof |
CN104113082A (en) * | 2014-07-17 | 2014-10-22 | 西安交通大学 | Modular full direct current photovoltaic system and control method thereof |
CN105429177A (en) * | 2015-12-16 | 2016-03-23 | 国网青海省电力公司 | Modularized photovoltaic energy storage system |
CN106877365A (en) * | 2017-03-21 | 2017-06-20 | 合肥工业大学 | The alternate unbalanced power control method of modular multi-level converter |
CN109004665A (en) * | 2018-08-31 | 2018-12-14 | 河北科技大学 | Wind-powered electricity generation, photoelectricity off-grid grid-connected hydrogen production process and system |
CN111463807A (en) * | 2020-05-11 | 2020-07-28 | 阳光电源股份有限公司 | Distributed direct-current coupling hydrogen production system and control method thereof |
CN111697628A (en) * | 2020-07-09 | 2020-09-22 | 北京雷动智创科技有限公司 | Photovoltaic electrolyzed water hydrogen production system and control method |
CN112290580A (en) * | 2019-07-12 | 2021-01-29 | 合肥阳光新能源科技有限公司 | New energy hydrogen production system |
US20210135455A1 (en) * | 2017-03-07 | 2021-05-06 | Abb Schweiz Ag | Photovoltaic power plant system |
WO2021082423A1 (en) * | 2019-10-28 | 2021-05-06 | 阳光电源股份有限公司 | Direct-current coupling hydrogen production system and control method therefor |
-
2021
- 2021-09-29 WO PCT/CN2021/121939 patent/WO2023050223A1/en active Application Filing
- 2021-09-29 CN CN202180102321.0A patent/CN117941198A/en active Pending
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103501020A (en) * | 2013-10-12 | 2014-01-08 | 电子科技大学 | Hybrid power supply system consisting of mains supply network and photovoltaic assembly and control method thereof |
CN104113082A (en) * | 2014-07-17 | 2014-10-22 | 西安交通大学 | Modular full direct current photovoltaic system and control method thereof |
CN105429177A (en) * | 2015-12-16 | 2016-03-23 | 国网青海省电力公司 | Modularized photovoltaic energy storage system |
US20210135455A1 (en) * | 2017-03-07 | 2021-05-06 | Abb Schweiz Ag | Photovoltaic power plant system |
CN106877365A (en) * | 2017-03-21 | 2017-06-20 | 合肥工业大学 | The alternate unbalanced power control method of modular multi-level converter |
CN109004665A (en) * | 2018-08-31 | 2018-12-14 | 河北科技大学 | Wind-powered electricity generation, photoelectricity off-grid grid-connected hydrogen production process and system |
CN112290580A (en) * | 2019-07-12 | 2021-01-29 | 合肥阳光新能源科技有限公司 | New energy hydrogen production system |
WO2021082423A1 (en) * | 2019-10-28 | 2021-05-06 | 阳光电源股份有限公司 | Direct-current coupling hydrogen production system and control method therefor |
CN111463807A (en) * | 2020-05-11 | 2020-07-28 | 阳光电源股份有限公司 | Distributed direct-current coupling hydrogen production system and control method thereof |
CN111697628A (en) * | 2020-07-09 | 2020-09-22 | 北京雷动智创科技有限公司 | Photovoltaic electrolyzed water hydrogen production system and control method |
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