CN116435541A - A negative carbon emission power generation system and method based on efficient utilization of biomass - Google Patents
A negative carbon emission power generation system and method based on efficient utilization of biomass Download PDFInfo
- Publication number
- CN116435541A CN116435541A CN202310241238.2A CN202310241238A CN116435541A CN 116435541 A CN116435541 A CN 116435541A CN 202310241238 A CN202310241238 A CN 202310241238A CN 116435541 A CN116435541 A CN 116435541A
- Authority
- CN
- China
- Prior art keywords
- solid oxide
- biomass
- raw material
- fuel cell
- power generation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04037—Electrical heating
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0662—Treatment of gaseous reactants or gaseous residues, e.g. cleaning
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/16—Biochemical fuel cells, i.e. cells in which microorganisms function as catalysts
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Biochemistry (AREA)
- Microbiology (AREA)
- Fuel Cell (AREA)
Abstract
本发明公开了一种基于生物质高效利用负碳排放发电系统及方法,所述系统包括生物质气化装置、固体氧化物燃料电池和固体氧化物电解池;固体氧化物电解池的阳极电解产物分为三部分,分别作为生物质气化原料、氧化剂和氧气存储;所述固体氧化物燃料电池的阳极产物与氧化剂燃烧做功后,一部分提供给生物质气化装置作为原料,另一部分提供给固体氧化物电解池作为电解原料;本发明通过BG‑SOFC发电系统和SOEC共电解系统的协调控制,该系统除可实现高效率发电外,还能对烟气中CO2和H2O以及其包含的能量充分回收,进而实现整个系统的负碳排放。
The invention discloses a negative carbon emission power generation system and method based on high-efficiency utilization of biomass. The system includes a biomass gasification device, a solid oxide fuel cell and a solid oxide electrolytic cell; the anode electrolysis product of the solid oxide electrolytic cell It is divided into three parts, which are respectively used as biomass gasification raw material, oxidant and oxygen storage; after the anode product of the solid oxide fuel cell and the oxidant are burned to do work, one part is provided to the biomass gasification device as raw material, and the other part is provided to the solid The oxide electrolytic cell is used as the raw material for electrolysis; the present invention adopts the coordinated control of the BG-SOFC power generation system and the SOEC co-electrolysis system. In addition to realizing high-efficiency power generation, the system can also control CO 2 and H 2 O in the flue gas as well as the The energy is fully recovered, thereby realizing the negative carbon emission of the entire system.
Description
技术领域technical field
本发明涉及生物质发电技术领域,具体涉及一种基于生物质高效利用负碳排放发电系统及方法。The invention relates to the technical field of biomass power generation, in particular to a negative carbon emission power generation system and method based on efficient utilization of biomass.
背景技术Background technique
全球变暖和能源危机给人类的生存和发展带来了巨大挑战。大量温室气体,尤其是二氧化碳的排放使得温室效应急剧加剧。减少发电过程中的碳排放,提高能源转换效率以及可再生能源高效利用被认为是解决这一问题的有效手段。与太阳能、风能等可再生能源相比生物质能具有连续发电的优势。与燃烧、发酵、热解等传统生物质高效利用方式相比,气化具有污染物排放低、合成气体积大、转化效率高等优点,受到了全世界研究者的广泛关注。在生物质气利用场景中,与其他原动机相比,固体氧化物燃料电池展现出高发电效率和低污染性等特点。此外,固体氧化物电解池还具有燃料适应性强,电解效率高的特点,这为实现高效碳捕集提供了可能。Global warming and energy crisis have brought great challenges to human survival and development. The emission of a large amount of greenhouse gases, especially carbon dioxide, has sharply aggravated the greenhouse effect. Reducing carbon emissions during power generation, improving energy conversion efficiency, and efficient use of renewable energy are considered to be effective means to solve this problem. Compared with renewable energy such as solar energy and wind energy, biomass energy has the advantage of continuous power generation. Compared with traditional biomass efficient utilization methods such as combustion, fermentation, and pyrolysis, gasification has the advantages of low pollutant emissions, large volume of syngas, and high conversion efficiency, and has attracted extensive attention from researchers all over the world. In the biomass gas utilization scenario, compared with other prime movers, solid oxide fuel cells exhibit high power generation efficiency and low pollution. In addition, the solid oxide electrolysis cell also has the characteristics of strong fuel adaptability and high electrolysis efficiency, which provides the possibility to achieve high-efficiency carbon capture.
发明人发现,现有的固体氧化物燃料电池/固体氧化物电解池/生物质气化技术一体化方案中,因固体氧化物电解池耗能高,因此,系统发电效率还有待提高,此外由于烟气中二氧化碳浓度低,所需捕捉能耗高,而现有技术大多都未对二氧化碳进行捕捉。The inventors found that in the existing solid oxide fuel cell/solid oxide electrolytic cell/biomass gasification technology integration scheme, the power generation efficiency of the system needs to be improved due to the high energy consumption of the solid oxide electrolytic cell. The concentration of carbon dioxide in flue gas is low, and the energy consumption required for capture is high, but most of the existing technologies do not capture carbon dioxide.
发明内容Contents of the invention
针对现有技术存在的问题,本发明提供一种基于生物质高效利用负碳排放发电系统和方法,以解决现有生物质发电系统发电效率低、二氧化碳捕捉能耗高的问题。Aiming at the problems existing in the prior art, the present invention provides a negative carbon emission power generation system and method based on efficient utilization of biomass to solve the problems of low power generation efficiency and high energy consumption of carbon dioxide capture in existing biomass power generation systems.
本发明的技术方案如下:Technical scheme of the present invention is as follows:
在本发明的第一方面,一种基于生物质高效利用负碳排放发电系统,包括生物质气化装置、固体氧化物燃料电池和固体氧化物电解池;In the first aspect of the present invention, a negative carbon emission power generation system based on efficient utilization of biomass, including a biomass gasification device, a solid oxide fuel cell and a solid oxide electrolytic cell;
其中,所述生物质气化装置为固体氧化物燃料电池提供阳极原料,所述固体氧化物电解池的阴极电解产物作为固体氧化物燃料电池阳极原料的补充;Wherein, the biomass gasification device provides the anode raw material for the solid oxide fuel cell, and the cathode electrolysis product of the solid oxide electrolytic cell is used as a supplement for the anode raw material of the solid oxide fuel cell;
固体氧化物电解池的阳极电解产物分为三部分,分别作为生物质气化原料、氧化剂和氧气存储;所述固体氧化物燃料电池的阳极产物与氧化剂燃烧做功后,一部分提供给生物质气化装置作为原料,另一部分提供给固体氧化物电解池作为电解原料。The anode electrolysis product of the solid oxide electrolytic cell is divided into three parts, which are respectively used as biomass gasification raw material, oxidant and oxygen storage; after the anode product of the solid oxide fuel cell and the oxidant are burned to do work, a part is provided for biomass gasification The device is used as raw material, and the other part is provided to the solid oxide electrolytic cell as electrolytic raw material.
在本发明的一些实施方式中,所述生物质气化装置的原料入口分别与第一分流器、第二分流器以及生物质源相连,生物质气化装置的合成气出口依次连接第二空气加热器、合成压缩机和第一混合器。In some embodiments of the present invention, the raw material inlet of the biomass gasification device is connected to the first splitter, the second splitter and the biomass source respectively, and the syngas outlet of the biomass gasification device is connected to the second air heater, synthesis compressor and first mixer.
在本发明的一些实施方式中,水源依次经过水泵、水加热器、第二混合器与第一混合器相连,所述第一混合器的出口与固体氧化物燃料电池的阳极原料入口相连。In some embodiments of the present invention, the water source is connected to the first mixer sequentially through the water pump, the water heater, and the second mixer, and the outlet of the first mixer is connected to the anode raw material inlet of the solid oxide fuel cell.
在本发明的一些实施方式中,所述第二混合器的入口还与固体氧化物电解池的阴极产物出口相连。In some embodiments of the present invention, the inlet of the second mixer is also connected with the cathode product outlet of the solid oxide electrolytic cell.
在本发明的一些实施方式中,空气经过空气压缩机、第一空气加热器、第二空气加热器、第三空气加热器与固体氧化物燃料电池的阴极原料入口相连。In some embodiments of the present invention, the air is connected to the cathode raw material inlet of the solid oxide fuel cell through the air compressor, the first air heater, the second air heater, and the third air heater.
在本发明的一些实施方式中,所述固体氧化物燃料电池的阴极产物出口依次连接空气轮机、第一空气加热器、水加热器。In some embodiments of the present invention, the cathode product outlet of the solid oxide fuel cell is sequentially connected to an air turbine, a first air heater, and a water heater.
在本发明的一些实施方式中,所述固体氧化物燃料电池的阳极产物出口依次连接燃烧室、燃气轮机、第一分流器,所述第一分流器的一个出口与生物质气化装置相连,另一个出口经过第三空气加热器与固体氧化物电解池的原料入口相连。In some embodiments of the present invention, the anode product outlet of the solid oxide fuel cell is sequentially connected to the combustion chamber, the gas turbine, and the first splitter, one outlet of the first splitter is connected to the biomass gasification device, and the other One outlet is connected with the raw material inlet of the solid oxide electrolytic cell through the third air heater.
在本发明的一些实施方式中,所述固体氧化物电解池的阳极电解产物出口与第二分流器相连,所述第二分流器上设置三个出口,分别连接生物质气化装置、燃烧室、氧气存储装置。In some embodiments of the present invention, the anode electrolysis product outlet of the solid oxide electrolytic cell is connected to the second flow divider, and the second flow divider is provided with three outlets, which are respectively connected to the biomass gasification device and the combustion chamber , Oxygen storage device.
在本发明的一些实施方式中,所述固体氧化物电解池的电力由固体氧化物燃料电池提供。In some embodiments of the present invention, the solid oxide electrolysis cell is powered by a solid oxide fuel cell.
在本发明的第二方面,提供了一种基于生物质高效利用负碳排放发电方法,包括:固体氧化物燃料电池在发电提供电力的同时,将自身产生的高温烟气一部分通过生物质气化装置回收,另一部分烟气则作为固体氧化物电解池的高温原料;同时,固体氧化物电解池将电解产物供给固体氧化物燃料电池,其中阴极电解产物作为固体氧化物燃料电池的电化学反应补充原料,阳极电解产物作为固体氧化物燃料电池富氧燃烧和生物质气化的原料。In the second aspect of the present invention, a method for generating electricity with negative carbon emissions based on efficient use of biomass is provided, including: while the solid oxide fuel cell generates electricity to provide electricity, part of the high-temperature flue gas generated by itself is gasified by biomass The other part of the flue gas is used as high-temperature raw material for the solid oxide electrolytic cell; at the same time, the solid oxide electrolytic cell supplies the electrolysis product to the solid oxide fuel cell, and the cathode electrolysis product is used as a supplement for the electrochemical reaction of the solid oxide fuel cell Raw materials, anode electrolysis products are used as raw materials for solid oxide fuel cell oxygen-rich combustion and biomass gasification.
本发明一个或多个技术方案具有以下有益效果:One or more technical solutions of the present invention have the following beneficial effects:
本发明提供的系统基于能量梯级利用的原理将生物质气化-固体氧化物燃料电池(BG-SOFC)发电系统和固体氧化物电解池(SOEC)共电解系统高度集成。BG-SOFC发电系统提供电力的同时,将自身产生的部分高温烟气(CO2+H2O)通过气化装置回收,另一部分烟气则作为SOEC共电解系统的高温原料;同时,SOEC共电解系统将电解产物(主要包含CO+H2+O2)供给BG-SOFC发电系统,其中CO+H2作为SOFC电化学反应补充原料,O2作为BG-SOFC发电系统富氧燃烧和生物质气化的原料。通过BG-SOFC发电系统和SOEC共电解系统的协调控制,该系统除可实现高效率发电外,还能对烟气中CO2+H2O以及其包含的能量充分回收,进而实现整个系统的负碳排放。该系统及以此为基础的改进型可以在生物质发电领域发挥重要作用。The system provided by the invention highly integrates a biomass gasification-solid oxide fuel cell (BG-SOFC) power generation system and a solid oxide electrolytic cell (SOEC) co-electrolysis system based on the principle of energy cascade utilization. While the BG-SOFC power generation system provides electricity, part of the high-temperature flue gas (CO 2 +H 2 O) generated by itself is recovered through the gasification device, and the other part of the flue gas is used as high-temperature raw material for the SOEC co-electrolysis system; at the same time, the SOEC co-electrolysis system The electrolysis system supplies the electrolysis products (mainly including CO+H 2 +O 2 ) to the BG-SOFC power generation system, in which CO+H 2 is used as the supplementary raw material for the electrochemical reaction of SOFC, and O 2 is used as the oxygen-enriched combustion and biomass of the BG-SOFC power generation system Gasified raw materials. Through the coordinated control of the BG-SOFC power generation system and the SOEC co-electrolysis system, the system can not only achieve high-efficiency power generation, but also fully recover CO 2 +H 2 O and the energy contained in the flue gas, thereby realizing the energy efficiency of the entire system. Negative carbon emissions. The system and the improved model based on it can play an important role in the field of biomass power generation.
本发明的系统通过设置的空气轮机和燃气轮机可以将固体氧化物燃料电池的阴极产物和阳极产物转化为机械功使用,通过设置的多个空气加热器和水加热器,实现将固体氧化物燃料电池的阴极产物和阳极产物的热能进行回收利用;固体氧化物电解池的电能来源于固体氧化物燃料电池,无需提供额外的电能;该系统能够实现系统中各种能量的充分回收利用,在保证高效率发电的同时实现整个系统的负碳排放。The system of the present invention can convert the cathode product and anode product of the solid oxide fuel cell into mechanical work through the provided air turbine and gas turbine, and realize the solid oxide fuel cell through the provided multiple air heaters and water heaters. The thermal energy of the cathode product and the anode product is recycled; the electric energy of the solid oxide electrolytic cell comes from the solid oxide fuel cell, and there is no need to provide additional electric energy; the system can realize the full recovery and utilization of various energies in the system, ensuring high Efficient power generation while achieving negative carbon emissions for the entire system.
附图说明Description of drawings
图1为基于生物质高效利用负碳排放发电系统示意图。Figure 1 is a schematic diagram of a negative carbon emission power generation system based on efficient utilization of biomass.
其中,1、生物质;2、第一部分高温烟气;3、合成气;4、低温合成气;5、高温高压合成气;6、阳极原料;7、阳极产物;8、燃烧产物;9、第二做功后气体;10、第二部分高温烟气;11、电解原料;12、阴极电解产物;13、阳极电解产物;14、第一部分氧气;15、第二部分氧气;16、第三部分氧气;17、空气;18、压缩空气;19、一次加热空气;20、二次加热空气;21、阴极原料;22、阴极产物;23、第一做功后气体;24、一次降温气体;25、二次降温气体;26、水源;27、加压水;28、水蒸气;29、混合气;Among them, 1. Biomass; 2. The first part of high-temperature flue gas; 3. Syngas; 4. Low-temperature synthesis gas; 5. High-temperature and high-pressure synthesis gas; 6. Anode raw materials; 7. Anode products; 8. Combustion products; 9. The gas after the second work; 10. The second part of high-temperature flue gas; 11. The raw material for electrolysis; 12. The cathode electrolysis product; 13. The anode electrolysis product; 14. The first part of oxygen; 15. The second part of oxygen; 16. The third part Oxygen; 17. Air; 18. Compressed air; 19. Primary heating air; 20. Secondary heating air; 21. Cathode raw material; 22. Cathode product; 23. Gas after the first work; 24. Primary cooling gas; 25. Secondary cooling gas; 26. Water source; 27. Pressurized water; 28. Water vapor; 29. Mixed gas;
AB为燃烧室;AC为空气压缩机;AH1为第一空气加热器;AH2为第二空气加热器;AH3为第三空气加热器;WP为水泵;WH为水加热器;M1为第一混合器;M2为第二混合器;SC为合成气压缩机;SOFC为固体氧化物燃料电池;T1为空气轮机;T2为燃气轮机;SP1为第一分流器;SP2为第二分流器;GAS为生物质气化装置;SOEC为固体氧化物电解池;OSU为氧气存储装置;Inv为逆变器。AB is the combustion chamber; AC is the air compressor; AH1 is the first air heater; AH2 is the second air heater; AH3 is the third air heater; WP is the water pump; WH is the water heater; M1 is the first mixing M2 is the second mixer; SC is the syngas compressor; SOFC is the solid oxide fuel cell; T1 is the air turbine; T2 is the gas turbine; SP1 is the first splitter; SP2 is the second splitter; Material gasification device; SOEC is solid oxide electrolytic cell; OSU is oxygen storage device; Inv is inverter.
具体实施方式Detailed ways
实施例1Example 1
本发明的一种典型的实施方式中,如图1所示,提出一种基于生物质高效利用负碳排放发电系统,包括生物质气化装置GAS、固体氧化物燃料电池SOFC和固体氧化物电解池SOEC,其中,所述生物质气化装置GAS为固体氧化物燃料电池SOFC提供阳极原料,所述固体氧化物电解池SOEC的阴极电解产物作为固体氧化物燃料电池SOFC阳极原料的补充;固体氧化物电解池SOEC的阳极电解产物分为三部分,分别作为生物质气化原料、氧化剂和氧气存储;所述固体氧化物燃料电池SOFC的阳极产物与氧化剂燃烧做功后,一部分提供给生物质气化装置作为原料,另一部分提供给固体氧化物电解池作为电解原料。In a typical implementation of the present invention, as shown in Figure 1, a negative carbon emission power generation system based on efficient utilization of biomass is proposed, including biomass gasification device GAS, solid oxide fuel cell SOFC and solid oxide electrolysis Pond SOEC, wherein, the biomass gasification device GAS provides anode raw material for solid oxide fuel cell SOFC, and the cathode electrolysis product of the solid oxide electrolytic cell SOEC is used as a supplement for the solid oxide fuel cell SOFC anode raw material; The anode electrolysis product of the solid oxide fuel cell SOEC is divided into three parts, which are respectively used as biomass gasification raw materials, oxidant and oxygen storage; after the anode product of the solid oxide fuel cell SOFC and the oxidant are burned to do work, a part is provided for biomass gasification The device is used as raw material, and the other part is provided to the solid oxide electrolytic cell as electrolytic raw material.
具体的,生物质气化装置GAS是利用热化学反应将固态生物质转换为气体燃料的过程,所述生物质气化装置的原料入口分别与第一分流器SP1、第二分流器SP2以及生物质1相连,生物质气化装置GAS的合成气3出口依次连接第二空气加热器AH2、合成压缩机SC和第一混合器M1相连。Specifically, the biomass gasification device GAS is a process of converting solid biomass into gaseous fuel by using thermochemical reactions. The substance 1 is connected, and the outlet of the
固体氧化物燃料电池SOFC属于高温燃料电池,以碳氢化合物作为其发电的燃料,将燃料的化学能转化为电能,实现发电。水源26依次经过水泵WP、水加热器WH、第二混合器M2与第一混合器M1相连,所述第一混合器M1的出口与固体氧化物燃料电池SOFC的阳极原料入口相连;所述第二混合器M2的入口还与固体氧化物电解池SOEC的阴极产物出口相连。空气17经过空气压缩机AC、第一空气加热器AH1、第二空气加热器AH2、第三空气加热器AH3与固体氧化物燃料电池SOFC的阴极原料入口相连。所述固体氧化物燃料电池SOFC的阴极产物出口依次连接空气轮机T1、第一空气加热器AH1、水加热器WH。所述固体氧化物燃料电池SOFC的阳极产物出口依次连接燃烧室AB、燃气轮机T2、第一分流器SP1,所述第一分流器SP1的一个出口与生物质气化装置GAS相连,另一个出口经过第三空气加热器AH3与固体氧化物电解池SOEC的原料入口相连。Solid Oxide Fuel Cell (SOFC) is a high-temperature fuel cell that uses hydrocarbons as its fuel for power generation, and converts the chemical energy of the fuel into electrical energy to achieve power generation. The
固体氧化物电解池SOEC是反向运行的固体氧化物燃料电池,在外加电压、高温下进行电解反应,实现将电能和热能转化为化学能,所述固体氧化物电解池SOEC的阳极电解产物出口与第二分流器SP2相连,所述第二分流器SP2上设置三个出口,分别连接生物质气化装置GAS、燃烧室AB、氧气存储装置OSU。The solid oxide electrolytic cell SOEC is a solid oxide fuel cell that operates in reverse. It performs an electrolytic reaction at an applied voltage and high temperature to convert electrical energy and thermal energy into chemical energy. The anode electrolysis product outlet of the solid oxide electrolytic cell SOEC is It is connected with the second splitter SP2, and the second splitter SP2 is provided with three outlets, respectively connected to the biomass gasification device GAS, the combustion chamber AB, and the oxygen storage device OSU.
在本实施例中,所述固体氧化物电解池SOEC的电力由固体氧化物燃料电池SOFC提供,固体氧化物燃料电池SOFC还与逆变器Inv相连,实现电能的应用。In this embodiment, the power of the solid oxide electrolytic cell SOEC is provided by a solid oxide fuel cell SOFC, and the solid oxide fuel cell SOFC is also connected to the inverter Inv to realize the application of electric energy.
本实施例提供的基于生物质高效利用负碳排放发电系统的工作原理如下:The working principle of the negative carbon emission power generation system based on efficient utilization of biomass provided in this example is as follows:
生物质1与来自第一分流器SP1含有H2O和CO2的第一部分高温烟气2及来自第二分流器SP2的第三部分氧气16在生物质气化装置GAS中发生气化反应,生成合成气3;接着合成气3通过第二空气加热器AH2对来自第一次空气加热器AH1的一次加热空气19进行加热,合成气温度降低,变成低温合成气4,然后被合成气压缩机SC压缩送至第一混合器M1;同时,外部水源26通过水泵WP加压,成为加压水27,并经过水加热器WH加热变成水蒸气28,被送至第二混合器M2,在第二混合器M2中与来自固体氧化物电解池SOEC的阴极电解产物12(主要含有CO和H2)混合;接着混合气29在第一混合器M1中与高温高压合成气5混合后,作为SOFC阳极原料6。Biomass 1 and the first part of high-
大气中的空气17通过空气压缩机AC压缩后,依次通过第一空气加热器AH1、第二空气加热器AH2、第三空气加热器AH3加热后作为阴极原料21送至固体氧化物燃料电池SOFC的阴极;然后,阴级原料21和阳极原料6在固体氧化物燃料电池SOFC内发生电化学反应,产生电能,接着通过逆变器Inv将直流电转化为交流电。The
阴极产物22推动空气轮机T1对外做功后,即第一做功后气体23,依次通过第一空气加热器AH1和水加热器WH对外释放热量,最后被排至大气;阳极产物7与来自第二分流器SP2的第一部分氧气14在燃烧室AB化学计量数燃烧(CO2和H2O被富集);燃烧产物8通过燃气轮机T2对外做功后,即第二做功后气体9被送至第一分流器SP1被分成两部分,其中,第一部分高温烟气2被直接送至生物气化装置作为气化剂(无需提供额外的热量),第二部分高温烟气10通过第三空气加热器AH3释放热量后被送至固体氧化物电解池SOEC作为电解原料11(无需提供额外的热量)。After the
固体氧化物电解池SOEC的电力由固体氧化物燃料电池SOFC提供,电解原料11来自第三空气加热器AH3;阳极电解产物13(O2)被分成三部分,第一部分氧气14作为固体氧化物燃料电池SOFC阳极产物燃烧的氧化剂,第二部分氧气15则被储存在氧气存储装置OSU中,第三部分氧气16被用作生物质气化装置GAS的部分气化剂;阴极电解产物12被送至第二混合器M2作为固体氧化物燃料电池SOFC的阳极补充原料。The power of the solid oxide electrolysis cell SOEC is provided by the solid oxide fuel cell SOFC, and the
实施例2Example 2
本发明的一种典型的实施方式中,提出一种基于生物质高效利用负碳排放发电方法,包括:固体氧化物燃料电池在发电提供电力的同时,将自身产生的高温烟气一部分通过生物质气化装置回收,另一部分烟气则作为固体氧化物电解池的高温原料;同时,固体氧化物电解池将电解产物供给固体氧化物燃料电池,其中阴极电解产物作为固体氧化物燃料电池的电化学反应补充原料,阳极电解产物作为固体氧化物燃料电池富氧燃烧和生物质气化的原料。In a typical implementation of the present invention, a method for generating electricity with negative carbon emissions based on efficient use of biomass is proposed, including: while the solid oxide fuel cell generates electricity to provide electricity, part of the high-temperature flue gas generated by itself passes through the biomass The gasification device recovers, and the other part of the flue gas is used as the high-temperature raw material of the solid oxide electrolytic cell; at the same time, the solid oxide electrolytic cell supplies the electrolysis product to the solid oxide fuel cell, and the cathode electrolysis product is used as the electrochemical fuel cell of the solid oxide fuel cell. The reaction supplements the raw material, and the anode electrolysis product is used as the raw material for the oxygen-rich combustion and biomass gasification of the solid oxide fuel cell.
以上所述的实施例对本发明的技术方案进行了详细说明,应理解的是以上所述仅为本发明的具体实施例,并不用于限制本发明,凡在本发明的原则范围内所做的任何修改、补充或类似方式替代等,均应包含在本发明的保护范围之内。The embodiments described above have described the technical solutions of the present invention in detail. It should be understood that the above descriptions are only specific embodiments of the present invention, and are not intended to limit the present invention. All done within the principle scope of the present invention Any modification, supplement or substitution in a similar manner shall be included within the protection scope of the present invention.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310241238.2A CN116435541A (en) | 2023-03-09 | 2023-03-09 | A negative carbon emission power generation system and method based on efficient utilization of biomass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310241238.2A CN116435541A (en) | 2023-03-09 | 2023-03-09 | A negative carbon emission power generation system and method based on efficient utilization of biomass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN116435541A true CN116435541A (en) | 2023-07-14 |
Family
ID=87088084
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202310241238.2A Pending CN116435541A (en) | 2023-03-09 | 2023-03-09 | A negative carbon emission power generation system and method based on efficient utilization of biomass |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN116435541A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118507785A (en) * | 2024-05-10 | 2024-08-16 | 华北电力大学 | Oxygen-enriched combustion SOFC zero-carbon power generation system based on low-temperature water electrolysis to produce oxygen |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1330700A (en) * | 1998-11-05 | 2002-01-09 | 株式会社荏原制作所 | Combustible gasification power generation system |
| KR20160036881A (en) * | 2014-09-26 | 2016-04-05 | 한국전력공사 | Recycling method of carbon dioxide and recycling apparatus using the same |
| CN107829786A (en) * | 2017-11-29 | 2018-03-23 | 中国华能集团清洁能源技术研究院有限公司 | A kind of near-zero release coal gasification power generation system and electricity-generating method with pollutant catabolic gene |
| CN109473702A (en) * | 2018-11-16 | 2019-03-15 | 山西晋城无烟煤矿业集团有限责任公司 | A solid oxide fuel cell exhaust gas treatment system and treatment method |
| CN114744264A (en) * | 2022-04-07 | 2022-07-12 | 山东大学 | A multi-generation system based on biomass gasification and solid oxide fuel cells |
| CN115371267A (en) * | 2022-07-25 | 2022-11-22 | 山东大学 | Integrated energy system integrating combined supply of cold, heat and electricity and seawater desalination and control method thereof |
| CN115558524A (en) * | 2022-09-22 | 2023-01-03 | 山西潞安矿业(集团)有限责任公司 | Coal gasification hydrogen production and tail gas zero emission process |
-
2023
- 2023-03-09 CN CN202310241238.2A patent/CN116435541A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1330700A (en) * | 1998-11-05 | 2002-01-09 | 株式会社荏原制作所 | Combustible gasification power generation system |
| KR20160036881A (en) * | 2014-09-26 | 2016-04-05 | 한국전력공사 | Recycling method of carbon dioxide and recycling apparatus using the same |
| CN107829786A (en) * | 2017-11-29 | 2018-03-23 | 中国华能集团清洁能源技术研究院有限公司 | A kind of near-zero release coal gasification power generation system and electricity-generating method with pollutant catabolic gene |
| CN109473702A (en) * | 2018-11-16 | 2019-03-15 | 山西晋城无烟煤矿业集团有限责任公司 | A solid oxide fuel cell exhaust gas treatment system and treatment method |
| CN114744264A (en) * | 2022-04-07 | 2022-07-12 | 山东大学 | A multi-generation system based on biomass gasification and solid oxide fuel cells |
| CN115371267A (en) * | 2022-07-25 | 2022-11-22 | 山东大学 | Integrated energy system integrating combined supply of cold, heat and electricity and seawater desalination and control method thereof |
| CN115558524A (en) * | 2022-09-22 | 2023-01-03 | 山西潞安矿业(集团)有限责任公司 | Coal gasification hydrogen production and tail gas zero emission process |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118507785A (en) * | 2024-05-10 | 2024-08-16 | 华北电力大学 | Oxygen-enriched combustion SOFC zero-carbon power generation system based on low-temperature water electrolysis to produce oxygen |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN210068320U (en) | Combined power generation system for biomass gasification driven by solar energy | |
| CN112448413A (en) | Distributed energy supply system and method with near-zero carbon emission | |
| CN104377375A (en) | Integrated gasification molten carbonate fuel cell power generating system | |
| CN109473702A (en) | A solid oxide fuel cell exhaust gas treatment system and treatment method | |
| CN208955118U (en) | A kind of solid oxide fuel cell exhaust treatment system based on electrolytic tank of solid oxide | |
| Liu et al. | A comparison of two schemes for pure hydrogen injection into a syngas-fueled SOFC: Thermoeconomic and environmental-based investigations | |
| CN115821286B (en) | A water electrolysis device and a biomass solar energy cogeneration system using the same | |
| CN116435541A (en) | A negative carbon emission power generation system and method based on efficient utilization of biomass | |
| CN217362587U (en) | Carbon-rich renewable combustion circulation system driven by new energy | |
| CN1151575C (en) | Solid Oxide Fuel Cell Steam Turbine Combined Power Generation System | |
| CN116317175A (en) | Solar-driven RSOC distributed polygeneration system and method for cogeneration thereof | |
| CN1151574C (en) | Molten Carbonate Fuel Cell Steam Turbine Combined Power Generation System | |
| CN115976539A (en) | Renewable energy utilization system based on nitrogen-free combustion and carbon dioxide cycle | |
| CN115354345A (en) | Photovoltaic photo-thermal coupling co-electrolysis combined garbage power generation comprehensive energy system and process method thereof | |
| CN218325037U (en) | An IGCC power generation system based on SOEC co-electrolysis | |
| CN216213576U (en) | Power generation system of molten carbonate fuel cell | |
| CN113921863B (en) | Molten carbonate fuel cell power generation system and method | |
| CN217354502U (en) | Carbon-based renewable combustion cycle system driven by new energy | |
| CN217334159U (en) | Zero-carbon-emission high-temperature reversible fuel cell energy supply/storage system for LNG receiving station | |
| CN206397600U (en) | Mixing energy supplying system based on gas turbine and SOFC | |
| CN117823279A (en) | Multi-energy cogeneration system based on biomass gas drive and working method | |
| CN110364755A (en) | Chemical Looping Partial Oxidation Reforming Conversion Directly Coupled Fuel Cell Power Generation System | |
| CN117673418A (en) | Carbon dioxide zero-emission solar photo-thermal and coal hydrogen production coupling power generation system | |
| CN114583223A (en) | Zero-carbon-emission high-temperature reversible fuel cell energy supply/storage system for LNG receiving station | |
| CN108301924A (en) | Mixing energy supplying system based on gas turbine and solid oxide fuel cell |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |
