WO2022193551A1 - Method for adding electrolyte to molten carbonate fuel cell - Google Patents
Method for adding electrolyte to molten carbonate fuel cell Download PDFInfo
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- WO2022193551A1 WO2022193551A1 PCT/CN2021/114307 CN2021114307W WO2022193551A1 WO 2022193551 A1 WO2022193551 A1 WO 2022193551A1 CN 2021114307 W CN2021114307 W CN 2021114307W WO 2022193551 A1 WO2022193551 A1 WO 2022193551A1
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- 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
- H01M8/14—Fuel cells with fused electrolytes
- H01M8/144—Fuel cells with fused electrolytes characterised by the electrolyte material
- H01M8/145—Fuel cells with fused electrolytes characterised by the electrolyte material comprising carbonates
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/8605—Porous electrodes
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- 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
- H01M8/02—Details
- H01M8/0289—Means for holding the electrolyte
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- 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
- H01M8/14—Fuel cells with fused electrolytes
- H01M2008/147—Fuel cells with molten carbonates
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- 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
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- the present application relates to the field of molten carbonate fuel cells, in particular to a method for adding electrolytes to molten carbonate fuel cells.
- the electrolyte of molten carbonate fuel cell is mainly carbonate, such as Li 2 CO 3 and K 2 CO 3 or LiCO 3 and Na 2 CO 3 .
- the electrolyte is prepared into a carbonate salt membrane, or the electrolyte and the diaphragm are prepared at the same time, or the electrolyte is put into the flow channel.
- This foreign electrolyte preparation technology is set for its molten carbonate structure, but has certain limitations for domestic fuel cells.
- the purpose of this application is to provide a molten carbonate fuel cell electrolyte addition method to overcome the defects of the prior art.
- the electrolyte is added to the electrode to reduce the distribution of the electrolyte in the flow channel, which can effectively reduce the bipolar
- a method for adding molten carbonate fuel cell electrolyte comprising the following steps:
- Step 1 mix the electrolyte with water and ethanol, and stir to obtain an electrolyte mixed solution
- Step 2 Weigh the mass of the electrode and measure the porosity of the electrode, and calculate the theoretical required mass of the electrolyte inside the electrode;
- Step 3 Put the electrode into the container, and add the electrolyte mixed solution
- Step 4 place the container under drying conditions until the water and ethanol are completely volatilized
- Step 5 Weigh the total mass of the electrode and the electrolyte attached to the electrode after drying, and then calculate the mass of the electrolyte attached to the electrode. If the electrolyte quality does not meet the actual required quality of the electrolyte inside the electrode, repeat steps 3 and 3 Fourth, if the quality of the electrolyte exceeds the actual required quality of the electrolyte inside the electrode, scrape off the excess electrolyte until the actual required quality range of the electrolyte inside the electrode is met. %;
- Step 6 heating the electrode obtained in step 5, and cooling after the heating and heating, that is, the addition of the molten carbonate fuel cell electrolyte is completed.
- the electrolyte is a mixture of Li 2 CO 3 and K 2 CO 3 , and the molar ratio between Li 2 CO 3 and K 2 CO 3 is 31:19.
- step 1 the mass ratio of electrolyte to water and ethanol is 1:(1-2):(1.5-2).
- stirring time in step 1 is 1.5-2h.
- melectrolyte represents the theoretical demand mass of the electrolyte inside the electrode
- ⁇ electrolyte represents the density of the electrolyte
- Vpore represents the electrode pore volume
- Velectrode represents the volume of the electrode
- melectrode represents the mass of the electrode
- ⁇ nickel represents the density of metallic nickel .
- drying conditions in step 4 are as follows: the temperature is 30°C, and the ventilation is carried out.
- the heating and temperature increase program in step 6 is specifically as follows: firstly, the temperature is raised from room temperature to 450°C in a nitrogen atmosphere, then the temperature is raised from 450°C to 650°C in a hydrogen atmosphere, and finally, the temperature is kept at 650°C for 2 hours under a hydrogen atmosphere.
- the temperature was increased from normal temperature to 450° C. for 5 h.
- the temperature was increased from 450°C to 650°C for 10 h.
- the electrolyte is added to the electrode, because the electrode material is a porous structure, and more than 70% of the interior is porosity, which can be filled with a certain quality of electrolyte, while the electrolyte of conventional molten carbonate fuel cells is generally placed in the flow channel, through this method
- the electrolyte is immersed in the pores of the electrolyte by heating and heating to realize the addition of the electrolyte.
- This method of adding electrolyte can reduce the distribution of the electrolyte in the flow channel, which can effectively reduce the thickness of the bipolar plate, and the electrolyte is added to the cathode material.
- nickel can chemically react with lithium carbonate to generate LiNiO 2 , so as to quickly realize the lithiation process of the cathode material and improve the performance of the fuel cell.
- the present application precisely controls the heating program.
- the heating process from room temperature to 450 °C, the oxidation of the electrode is prevented under the protection of nitrogen gas.
- the electrolyte is melted and immersed in the electrode pores.
- the partially oxidized nickel electrode is reduced, and the heat preservation at 650°C can make the nickel react with lithium carbonate to form LiNiO 2 , so as to quickly realize the lithiation process of the cathode material.
- FIG. 1 is a schematic diagram of adding electrolyte to the electrode of the present application.
- a method for adding molten carbonate fuel cell electrolyte comprising the following steps:
- melectrolyte represents the theoretical demand mass of the electrolyte inside the electrode
- ⁇ electrolyte represents the density of the electrolyte
- Vpore represents the electrode pore volume
- Velectrode represents the volume of the electrode
- melectrode represents the mass of the electrode
- ⁇ nickel represents the density of metallic nickel .
- the heating program is normal temperature to 450°C ( N2 protection) for 5h, 450-650°C ( H2 protection) for 10h, 650°C ( H2 protection) for 2h, and cooling with the furnace ( H2 protection), nitrogen and hydrogen atmospheres prevent the oxidation of the electrodes.
- the electrolyte is mixed with water and ethanol to form a solution.
- the electrolyte is dissolved in water and ethanol.
- the addition of ethanol is conducive to the rapid volatilization of the solvent.
- the electrolyte is placed in the electrode by heating, which is different from the traditional electrolyte and electrode. Mixing preparation, heating process Gas protection is used to prevent the oxidation of nickel electrodes.
- the addition of catholyte needs to be strictly controlled according to the formula and the quality range of electrolyte requirements to ensure effective electrolyte in the electrode and prevent waste of electrolyte.
- the heating program is normal temperature to 450°C (N 2 protection) for 5h, 450-650°C (H 2 protection) for 10h, 650°C for 2h (H 2 protection), and cool down with the furnace ( H2 protection), nitrogen and hydrogen atmospheres prevent the oxidation of the electrodes.
- the electrode into a single cell for performance testing.
- the single cell requires 50g of electrolyte, the electrode contains 17.9g of salt, and the rest of the electrolyte is placed in the flow channel.
- the open circuit voltage of a single cell is 1.3905V, and the current density of the battery is 93A/cm 2 .
- the open circuit voltage is increased by 0.05V, and the current density is increased by 10A/cm 2 .
- the heating program is normal temperature to 450°C (N 2 protection) for 5h, 450-650°C (H 2 protection) for 10h, 650°C for 2h (H 2 protection), and cool down with the furnace ( H2 protection), nitrogen and hydrogen atmospheres prevent the oxidation of the electrodes.
- the weight of the electrode and electrolyte after cooling is weighed to 43g, and the mass of the added electrolyte is calculated to be 13g.
- the single cell requires 50g of electrolyte, 13g of salt in the electrode, and the rest of the electrolyte is placed in the flow channel.
- the single cell open circuit voltage is 1.3885V, and the battery current density is 94A/cm 2 .
- the open circuit voltage is increased by 0.04V, and the current density is increased by 9A/cm 2 .
- the common mass of the electrode and the electrolyte is weighed to 56.1g, which meets the required mass range of the electrolyte inside the electrode (78% of the theoretical electrode electrolyte requirement).
- the heating program is normal temperature to 450°C (N 2 protection) for 5h, 450-650°C (H 2 protection) for 10h, 650°C for 2h (H 2 protection), and cool down with the furnace ( H2 protection), nitrogen and hydrogen atmospheres prevent the oxidation of the electrodes.
- the single cell requires 50g of electrolyte, the electrode contains 20.1g of salt, and the rest of the electrolyte is placed in the flow channel.
- the single cell open circuit voltage is 1.401V, and the battery current density is 96A/cm 2 .
- the open circuit voltage is increased by 0.06V, and the current density is increased by 12A/cm 2 .
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Abstract
Description
本申请涉及熔融碳酸盐燃料电池领域,具体涉及一种熔融碳酸盐燃料电池电解质添加方法。The present application relates to the field of molten carbonate fuel cells, in particular to a method for adding electrolytes to molten carbonate fuel cells.
熔融碳酸盐燃料电池发电技术作为一种高温燃料电池发电技术,因其具备燃料来源广、模块化和发电效率高等优点在国外得到广泛应用。近年来,随着国内氢能领域的技术不断发展,燃料电池发电技术也不断进入国内视野。尤其在燃料电池关键材料的制备方式上,熔融碳酸盐燃料电池电解质主要是碳酸盐,如Li 2CO 3和K 2CO 3或LiCO 3和Na 2CO 3。国外采用的是将电解质制备成碳酸盐盐膜,或将电解质与隔膜进行同时制备,或将电解质放入到流道内。国外这种电解质制备技术针对其熔融碳酸盐结构件而设定,而对于国内燃料电池具有一定的受限性。 As a high-temperature fuel cell power generation technology, molten carbonate fuel cell power generation technology is widely used abroad because of its advantages of wide fuel sources, modularization and high power generation efficiency. In recent years, with the continuous development of technology in the domestic hydrogen energy field, fuel cell power generation technology has also entered the domestic field of vision. Especially in the preparation method of key fuel cell materials, the electrolyte of molten carbonate fuel cell is mainly carbonate, such as Li 2 CO 3 and K 2 CO 3 or LiCO 3 and Na 2 CO 3 . In foreign countries, the electrolyte is prepared into a carbonate salt membrane, or the electrolyte and the diaphragm are prepared at the same time, or the electrolyte is put into the flow channel. This foreign electrolyte preparation technology is set for its molten carbonate structure, but has certain limitations for domestic fuel cells.
发明内容SUMMARY OF THE INVENTION
本申请的目的在于提供一种熔融碳酸盐燃料电池电解质添加方法,以克服现有技术存在的缺陷,本申请通过将电解质添加到电极中,来减少电解质在流道内分布,可有效降低双极板的厚度,并且通过在阴极中添加电解质可以快速实现阴极材料的锂化过程,提高燃料电池的性能。The purpose of this application is to provide a molten carbonate fuel cell electrolyte addition method to overcome the defects of the prior art. In this application, the electrolyte is added to the electrode to reduce the distribution of the electrolyte in the flow channel, which can effectively reduce the bipolar The thickness of the plate, and by adding an electrolyte to the cathode, the lithiation process of the cathode material can be quickly achieved, improving the performance of the fuel cell.
为达到上述目的,本申请采用如下技术方案:To achieve the above object, the application adopts the following technical solutions:
一种熔融碳酸盐燃料电池电解质添加方法,包括以下步骤:A method for adding molten carbonate fuel cell electrolyte, comprising the following steps:
步骤一:将电解质与水和乙醇进行混合,并搅拌,得到电解质混合溶液;Step 1: mix the electrolyte with water and ethanol, and stir to obtain an electrolyte mixed solution;
步骤二:称量电极质量并测量电极的孔隙率,计算得出电极内部电解质的理论需求质量;Step 2: Weigh the mass of the electrode and measure the porosity of the electrode, and calculate the theoretical required mass of the electrolyte inside the electrode;
步骤三:将电极放入容器中,并加入电解质混合溶液;Step 3: Put the electrode into the container, and add the electrolyte mixed solution;
步骤四:将容器置于烘干条件下,直至水和乙醇完全挥发;Step 4: place the container under drying conditions until the water and ethanol are completely volatilized;
步骤五:称量烘干后电极以及附着在电极上的电解质的总质量,进而计算得到附着在电极上的电解质质量,若电解质质量未满足电极内部电解质的实际需求质量,则重复步骤三和步骤四,若电解质质量超出电极内部电解质的实际需求质量,则刮除多余的电解质,直至满足电极内部电解质实际需求质量范围,电极内部电解质实际需求质量范围为电极内部电解质理论需求质量的60%-80%;Step 5: Weigh the total mass of the electrode and the electrolyte attached to the electrode after drying, and then calculate the mass of the electrolyte attached to the electrode. If the electrolyte quality does not meet the actual required quality of the electrolyte inside the electrode, repeat steps 3 and 3 Fourth, if the quality of the electrolyte exceeds the actual required quality of the electrolyte inside the electrode, scrape off the excess electrolyte until the actual required quality range of the electrolyte inside the electrode is met. %;
步骤六:将步骤五得到的电极进行加热升温,加热升温结束后冷却,即完成熔融碳酸盐燃料电池电解质添加。Step 6: heating the electrode obtained in step 5, and cooling after the heating and heating, that is, the addition of the molten carbonate fuel cell electrolyte is completed.
进一步地,步骤一中电解质采用Li 2CO 3和K 2CO 3的混合物,且Li 2CO 3和K 2CO 3之间的摩尔比为31:19。 Further, in the first step, the electrolyte is a mixture of Li 2 CO 3 and K 2 CO 3 , and the molar ratio between Li 2 CO 3 and K 2 CO 3 is 31:19.
进一步地,步骤一中电解质与水和乙醇的质量比为1:(1-2):(1.5-2)。Further, in step 1, the mass ratio of electrolyte to water and ethanol is 1:(1-2):(1.5-2).
进一步地,步骤一中搅拌时间为1.5-2h。Further, the stirring time in step 1 is 1.5-2h.
进一步地,步骤二中计算电极内部电解质的理论需求质量的公式为:Further, the formula for calculating the theoretical required mass of the electrolyte inside the electrode in step 2 is:
其中,m 电解质表示电极内部电解质的理论需求质量,ρ 电解质表示电解质的密度,V 孔隙表示电极孔隙体积,V 电极表示电极的体积,m 电极表示电极的质量,ρ 镍表示金属镍的密度。 Among them, melectrolyte represents the theoretical demand mass of the electrolyte inside the electrode, ρelectrolyte represents the density of the electrolyte , Vpore represents the electrode pore volume, Velectrode represents the volume of the electrode , melectrode represents the mass of the electrode, and ρnickel represents the density of metallic nickel .
进一步地,步骤四中烘干条件具体为:温度30℃,通风。Further, the drying conditions in step 4 are as follows: the temperature is 30°C, and the ventilation is carried out.
进一步地,步骤六中加热升温程序具体为:首先在氮气氛围下由常温升温至450℃,然后在氢气氛围下由450℃升温至650℃,最后在氢气分为下于650℃下保温2h。Further, the heating and temperature increase program in step 6 is specifically as follows: firstly, the temperature is raised from room temperature to 450°C in a nitrogen atmosphere, then the temperature is raised from 450°C to 650°C in a hydrogen atmosphere, and finally, the temperature is kept at 650°C for 2 hours under a hydrogen atmosphere.
进一步地,由常温升温至450℃,时间为5h。Further, the temperature was increased from normal temperature to 450° C. for 5 h.
进一步地,由450℃升温至650℃,时间为10h。Further, the temperature was increased from 450°C to 650°C for 10 h.
与现有技术相比,本申请具有以下有益的技术效果:Compared with the prior art, the present application has the following beneficial technical effects:
本申请通过将电解质添加到电极中,因电极材料为多孔结构,内部70%以上为孔隙,可以填充一定质量的电解质,而常规熔融碳酸盐燃料电池的电解质一般放置于流道中,通过此方法利用加热升温将电解质浸入电解质的孔隙中,实现了电解质的添加,这种电解质的添加方法能减少电解质在流道内分布,进而可有效降低双极板的厚度,并且阴极材料中添加电解质,在加热升温过程镍可以通过与碳酸锂发生化学反应生成LiNiO 2,来快速实现阴极材料的锂化过程,提高燃料电池的性能。 In this application, the electrolyte is added to the electrode, because the electrode material is a porous structure, and more than 70% of the interior is porosity, which can be filled with a certain quality of electrolyte, while the electrolyte of conventional molten carbonate fuel cells is generally placed in the flow channel, through this method The electrolyte is immersed in the pores of the electrolyte by heating and heating to realize the addition of the electrolyte. This method of adding electrolyte can reduce the distribution of the electrolyte in the flow channel, which can effectively reduce the thickness of the bipolar plate, and the electrolyte is added to the cathode material. During the heating process, nickel can chemically react with lithium carbonate to generate LiNiO 2 , so as to quickly realize the lithiation process of the cathode material and improve the performance of the fuel cell.
进一步地,本申请精确控制升温程序,室温至450℃升温过程中在氮气的保护下防止电极的氧化,450℃至650℃在氢气的保护下,电解质融化并浸入电极孔隙中,氢气氛围下可以还原部分氧化的镍电极,650℃的保温能使镍与碳酸锂发生化学反应生成LiNiO 2,以快速实现阴极材料的锂化过程。 Further, the present application precisely controls the heating program. During the heating process from room temperature to 450 °C, the oxidation of the electrode is prevented under the protection of nitrogen gas. Under the protection of hydrogen gas from 450 °C to 650 °C, the electrolyte is melted and immersed in the electrode pores. The partially oxidized nickel electrode is reduced, and the heat preservation at 650°C can make the nickel react with lithium carbonate to form LiNiO 2 , so as to quickly realize the lithiation process of the cathode material.
图1是本申请电极添加电解质示意图。FIG. 1 is a schematic diagram of adding electrolyte to the electrode of the present application.
下面对本申请的实施方式做进一步详细描述:Embodiments of the present application are described in further detail below:
一种熔融碳酸盐燃料电池电解质添加方法,包含以下步骤:A method for adding molten carbonate fuel cell electrolyte, comprising the following steps:
1、将电解质(Li 2CO 3和K 2CO 3,二者之间摩尔比为31:19)与水、乙醇进行按1:(1-2):(1.5-2)的质量比例混合,并搅拌1.5-2h,得到电解质混合溶液; 1. Mix the electrolyte (Li 2 CO 3 and K 2 CO 3 , the molar ratio between the two is 31:19) with water and ethanol in a mass ratio of 1:(1-2):(1.5-2), And stir for 1.5-2h to obtain electrolyte mixed solution;
2、称量电极质量和测量电极的孔隙率,计算出电极内部电解质的需求量,计算公式为:2. Weigh the electrode mass and measure the porosity of the electrode, and calculate the demand for electrolyte inside the electrode. The calculation formula is:
其中,m 电解质表示电极内部电解质的理论需求质量,ρ 电解质表示电解质的密度,V 孔隙表示电极孔隙体积,V 电极表示电极的体积,m 电极表示电极的质量,ρ 镍表示金属镍的密度。 Among them, melectrolyte represents the theoretical demand mass of the electrolyte inside the electrode, ρelectrolyte represents the density of the electrolyte , Vpore represents the electrode pore volume, Velectrode represents the volume of the electrode , melectrode represents the mass of the electrode, and ρnickel represents the density of metallic nickel .
3、将电极放入托盘中,并加入电解质混合溶液;3. Put the electrode into the tray, and add the electrolyte mixed solution;
4、将托盘放入烘箱中,保持温度30℃和通风,直至水和乙醇挥发完全;4. Put the tray into the oven, keep the temperature at 30℃ and ventilate until the water and ethanol evaporate completely;
5、称量电极和电解质的共同质量,进而计算得到附着在电极上的电解质质量,若电解质质量未满足电极内部电解质的实际需求质量,则重复步骤三和步骤四,若电解质质量超出电极内部电解质的实际需求质量,则刮除多余的电解质,直至满足电极内部电解质实际需求质量范围,电极内部电解质实际需求质量范围为电极内部电解质理论需求质量的60%-80%;5. Weigh the common mass of the electrode and the electrolyte, and then calculate the mass of the electrolyte attached to the electrode. If the mass of the electrolyte does not meet the actual demanded mass of the electrolyte inside the electrode, repeat steps 3 and 4. If the mass of the electrolyte exceeds that of the electrolyte inside the electrode If the actual demanded mass of the electrode is reached, scrape off the excess electrolyte until the actual demanded mass of the electrolyte inside the electrode is met, and the actual demanded mass of the internal electrolyte of the electrode is 60%-80% of the theoretical demanded mass of the internal electrolyte of the electrode;
6、将电极和电解质放入加热炉中,加热程序为常温至450℃(N 2保护)5h,450-650℃(H 2保护)10h,650℃保温(H 2保护)2h,随炉降温(H 2保护),氮气和氢气氛围阻止电极的氧化。 6. Put the electrode and electrolyte into the heating furnace, the heating program is normal temperature to 450°C ( N2 protection) for 5h, 450-650°C ( H2 protection) for 10h, 650°C ( H2 protection) for 2h, and cooling with the furnace ( H2 protection), nitrogen and hydrogen atmospheres prevent the oxidation of the electrodes.
本申请将电解质和水、乙醇混合成溶液,电解质溶于水和乙醇中,乙醇的加入利于溶剂的快速挥发,通过加热方式将电解质置于电极中,区别与传统电解质和电极混合制备,加热过程中采用气体保护,防止镍电极的氧化,阴极电解质的添加需要依据公式和电解质需求质量范围进行严格控制量,保证电极中有效电解质,防止电解质的浪费。In this application, the electrolyte is mixed with water and ethanol to form a solution. The electrolyte is dissolved in water and ethanol. The addition of ethanol is conducive to the rapid volatilization of the solvent. The electrolyte is placed in the electrode by heating, which is different from the traditional electrolyte and electrode. Mixing preparation, heating process Gas protection is used to prevent the oxidation of nickel electrodes. The addition of catholyte needs to be strictly controlled according to the formula and the quality range of electrolyte requirements to ensure effective electrolyte in the electrode and prevent waste of electrolyte.
下面结合实施例对本申请做进一步详细描述:Below in conjunction with embodiment, this application is described in further detail:
实施例1Example 1
1、将电解质Li 2CO 3、K 2CO 3与水、乙醇进行按比例混合(20:20:30,质量比),并搅拌1.5h; 1. Mix electrolyte Li 2 CO 3 , K 2 CO 3 with water and ethanol in proportion (20:20:30, mass ratio), and stir for 1.5h;
2、称量电极质量33g和测量电极的孔隙率77%,计算出电极内部电解质的理论需求量25.3g;2. Weigh the electrode mass of 33g and measure the porosity of the electrode to 77%, and calculate the theoretical demand for the electrolyte inside the electrode to be 25.3g;
3、将需要添加电解的电极放入托盘中,并加入电解质与乙醇的混合溶液,质量100g;3. Put the electrode that needs to be electrolyzed into the tray, and add the mixed solution of electrolyte and ethanol, the mass is 100g;
4、将托盘放入烘箱,温度30℃和通风,直至乙醇挥发完全;4. Put the tray into the oven at 30℃ and ventilate until the ethanol evaporates completely;
5、称量电极和电解质的共同质量52g,满足电极内部电解质需求质量范 围(75%理论需求量)。5. Weigh the common mass of the electrode and the electrolyte to 52g, which meets the required mass range of the electrolyte inside the electrode (75% of the theoretical requirement).
6、将电极和电解质放入加热炉中,加热程序为常温至450℃(N 2保护)5h,450-650℃(H 2保护)10h,650℃保温2h(H 2保护),随炉降温(H 2保护),氮气和氢气氛围阻止电极的氧化。 6. Put the electrode and electrolyte into the heating furnace, the heating program is normal temperature to 450°C (N 2 protection) for 5h, 450-650°C (H 2 protection) for 10h, 650°C for 2h (H 2 protection), and cool down with the furnace ( H2 protection), nitrogen and hydrogen atmospheres prevent the oxidation of the electrodes.
7、称量冷却后的电极和电解质重量50.9g,计算添加电解质的质量为17.9g。7. Weigh 50.9 g of the electrode and electrolyte after cooling, and calculate the mass of the added electrolyte to be 17.9 g.
8、将电极组装成单电池进行性能测试,其中单电池需要电解质50g,电极中含盐17.9g,其余电解质置于流道中。单电池开路电压1.3905V,电池电流密度93A/cm 2,比常规在流道内添加电解质50g的方法开路电压增加了0.05V,电流密度增加了10A/cm 2。 8. Assemble the electrode into a single cell for performance testing. The single cell requires 50g of electrolyte, the electrode contains 17.9g of salt, and the rest of the electrolyte is placed in the flow channel. The open circuit voltage of a single cell is 1.3905V, and the current density of the battery is 93A/cm 2 . Compared with the conventional method of adding 50g of electrolyte in the flow channel, the open circuit voltage is increased by 0.05V, and the current density is increased by 10A/cm 2 .
实施例2Example 2
1、将电解质Li 2CO 3、K 2CO 3与水、乙醇进行按比例混合(20:40:40,质量比),并搅拌1.8h; 1. Mix electrolyte Li 2 CO 3 , K 2 CO 3 with water and ethanol in proportion (20:40:40, mass ratio), and stir for 1.8h;
2、称量电极质量30g和测量电极的孔隙率77%,计算出电极内部电解质的理论需求量24.1g;2. Weigh the electrode mass of 30g and measure the porosity of the electrode to 77%, and calculate the theoretical demand for the electrolyte inside the electrode to be 24.1g;
3、将需要添加电解的电极放入托盘中,并加入电解质与乙醇的混合溶液,质量100g;3. Put the electrode that needs to be electrolyzed into the tray, and add the mixed solution of electrolyte and ethanol, the mass is 100g;
4、将托盘放入烘箱,温度30℃和通风,直至乙醇挥发完全;4. Put the tray into the oven at 30℃ and ventilate until the ethanol evaporates completely;
5、称量电极和电解质的共同质量44.5g,满足电极内部电解质需求质量范围(60%理论电极电解质质量)。5. Weigh the common mass of the electrode and the electrolyte to 44.5g, which meets the required mass range of the electrolyte inside the electrode (60% of the theoretical electrode electrolyte mass).
6、将电极和电解质放入加热炉中,加热程序为常温至450℃(N 2保护)5h,450-650℃(H 2保护)10h,650℃保温2h(H 2保护),随炉降温(H 2保护),氮气和氢气氛围阻止电极的氧化。 6. Put the electrode and electrolyte into the heating furnace, the heating program is normal temperature to 450°C (N 2 protection) for 5h, 450-650°C (H 2 protection) for 10h, 650°C for 2h (H 2 protection), and cool down with the furnace ( H2 protection), nitrogen and hydrogen atmospheres prevent the oxidation of the electrodes.
7、称量冷却后的电极和电解质重量43g,计算添加电解质的质量为13g。7. The weight of the electrode and electrolyte after cooling is weighed to 43g, and the mass of the added electrolyte is calculated to be 13g.
8、将电极组装成单电池进行性能测试,其中单电池需要电解质50g,电 极中含盐13g,其余电解质置于流道中。单电池开路电压1.3885V,电池电流密度94A/cm 2,比常规在流道内添加电解质50g的方法开路电压增加了0.04V,电流密度增加了9A/cm 2。 8. Assemble the electrode into a single cell for performance testing. The single cell requires 50g of electrolyte, 13g of salt in the electrode, and the rest of the electrolyte is placed in the flow channel. The single cell open circuit voltage is 1.3885V, and the battery current density is 94A/cm 2 . Compared with the conventional method of adding 50g of electrolyte in the flow channel, the open circuit voltage is increased by 0.04V, and the current density is increased by 9A/cm 2 .
实施例3Example 3
1、将电解质Li 2CO 3、K 2CO 3与水、乙醇进行按比例混合(20:30:35,质量比),并搅拌2h; 1. Mix the electrolyte Li 2 CO 3 and K 2 CO 3 with water and ethanol in proportion (20:30:35, mass ratio), and stir for 2h;
2、称量电极质量35g和测量电极的孔隙率77%,计算出电极内部电解质的理论需求量27.1g;2. Weigh the electrode mass of 35g and measure the porosity of the electrode to 77%, and calculate the theoretical demand for the electrolyte inside the electrode to be 27.1g;
3、将需要添加电解的电极放入托盘中,并加入电解质与乙醇的混合溶液,质量100g;3. Put the electrode that needs to be electrolyzed into the tray, and add the mixed solution of electrolyte and ethanol, the mass is 100g;
4、将托盘放入烘箱,温度30℃和通风,直至乙醇挥发完全;4. Put the tray into the oven at 30℃ and ventilate until the ethanol evaporates completely;
5、称量电极和电解质的共同质量56.1g,满足电极内部电解质需求质量范围(78%理论电极电解质需求量)。5. The common mass of the electrode and the electrolyte is weighed to 56.1g, which meets the required mass range of the electrolyte inside the electrode (78% of the theoretical electrode electrolyte requirement).
6、将电极和电解质放入加热炉中,加热程序为常温至450℃(N 2保护)5h,450-650℃(H 2保护)10h,650℃保温2h(H 2保护),随炉降温(H 2保护),氮气和氢气氛围阻止电极的氧化。 6. Put the electrode and electrolyte into the heating furnace, the heating program is normal temperature to 450°C (N 2 protection) for 5h, 450-650°C (H 2 protection) for 10h, 650°C for 2h (H 2 protection), and cool down with the furnace ( H2 protection), nitrogen and hydrogen atmospheres prevent the oxidation of the electrodes.
7、称量冷却后的电极和电解质重量55.1g,计算添加电解质的质量为20.1g。7. Weigh 55.1 g of the electrode and electrolyte after cooling, and calculate the mass of the added electrolyte to be 20.1 g.
8、将电极组装成单电池进行性能测试,其中单电池需要电解质50g,电极中含盐20.1g,其余电解质置于流道中。单电池开路电压1.401V,电池电流密度96A/cm 2,比常规在流道内添加电解质50g的方法开路电压增加了0.06V,电流密度增加了12A/cm 2。 8. Assemble the electrode into a single cell for performance testing. The single cell requires 50g of electrolyte, the electrode contains 20.1g of salt, and the rest of the electrolyte is placed in the flow channel. The single cell open circuit voltage is 1.401V, and the battery current density is 96A/cm 2 . Compared with the conventional method of adding 50 g of electrolyte in the flow channel, the open circuit voltage is increased by 0.06V, and the current density is increased by 12A/cm 2 .
以上所述仅为本申请的较佳实施例而已,并不用以限制本申请,凡在本申请的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本申请的保护范围之内。The above descriptions are only preferred embodiments of the present application, and are not intended to limit the present application. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present application shall be included in the scope of the present application. within the scope of protection.
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| KR20000003203A (en) * | 1998-06-26 | 2000-01-15 | 이해규 | Electrode manufacturing method for fuel battery impregnating electrolyte |
| US20080160181A1 (en) * | 2006-12-28 | 2008-07-03 | Doosan Heavy Industries & Construction Co., Ltd. | Manufacturing Method of Electrolyte Filled Cathode for Molten Carbonate Fuel Cell |
| CN204529990U (en) * | 2015-02-04 | 2015-08-05 | 中国华能集团清洁能源技术研究院有限公司 | A kind of based on the electrolysis CO2 of fused carbonate electrolyzer and the system of H2O producing synthesis gas |
| CN106935887A (en) * | 2017-03-08 | 2017-07-07 | 中国华能集团清洁能源技术研究院有限公司 | A kind of startup method of molten carbonate fuel cell heap |
| CN112820923A (en) * | 2021-03-19 | 2021-05-18 | 华能国际电力股份有限公司 | Electrolyte adding method for molten carbonate fuel cell |
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| JPH0760684B2 (en) * | 1986-09-08 | 1995-06-28 | 松下電器産業株式会社 | Method for manufacturing electrodes for molten carbonate fuel cells |
| JPH0711407Y2 (en) * | 1988-06-20 | 1995-03-15 | 石川島播磨重工業株式会社 | Structure of fuel cell electrode |
| CN104078698B (en) * | 2014-06-30 | 2016-03-30 | 中国华能集团清洁能源技术研究院有限公司 | A Method for Storage and Compensation of Molten Carbonate Fuel Cell Electrolyte |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20000003203A (en) * | 1998-06-26 | 2000-01-15 | 이해규 | Electrode manufacturing method for fuel battery impregnating electrolyte |
| US20080160181A1 (en) * | 2006-12-28 | 2008-07-03 | Doosan Heavy Industries & Construction Co., Ltd. | Manufacturing Method of Electrolyte Filled Cathode for Molten Carbonate Fuel Cell |
| CN204529990U (en) * | 2015-02-04 | 2015-08-05 | 中国华能集团清洁能源技术研究院有限公司 | A kind of based on the electrolysis CO2 of fused carbonate electrolyzer and the system of H2O producing synthesis gas |
| CN106935887A (en) * | 2017-03-08 | 2017-07-07 | 中国华能集团清洁能源技术研究院有限公司 | A kind of startup method of molten carbonate fuel cell heap |
| CN112820923A (en) * | 2021-03-19 | 2021-05-18 | 华能国际电力股份有限公司 | Electrolyte adding method for molten carbonate fuel cell |
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