CN100448066C - A sealing material of solid oxide fuel cell and its sealing method - Google Patents
A sealing material of solid oxide fuel cell and its sealing method Download PDFInfo
- Publication number
- CN100448066C CN100448066C CNB2007100525194A CN200710052519A CN100448066C CN 100448066 C CN100448066 C CN 100448066C CN B2007100525194 A CNB2007100525194 A CN B2007100525194A CN 200710052519 A CN200710052519 A CN 200710052519A CN 100448066 C CN100448066 C CN 100448066C
- Authority
- CN
- China
- Prior art keywords
- particle
- solid particle
- solid
- size
- ceramic
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Abstract
The invention discloses a sealing material and sealing method of solid oxide fuel battery in the element sealing material and sealing method, which comprises the following parts: solid particle or solid particle and ceramic fiber, organic binder and plasticizer, wherein the solid particle can be ceramic, metal or glass with size at 0.5-6um; the whole or most of particle is ceramic particle, which is selected from alumina, zirconia, titania or magnesia; the ceramic fiber is ceramic alumina fiber or alumina-silica ceramic fiber with most diameter less than 3um. The making method comprises the following steps: preparing raw material; allocating; pressurizing; heating. The invention possesses chemical stability and electric insulation for industrial manufacturing, which possesses excellent sealing property for sealing plane-typed SOFC and analog ceramic and metal.
Description
Technical field
The invention belongs to components and parts encapsulant and encapsulating method, be used for the sealing of Solid Oxide Fuel Cell.
Background technology
Solid Oxide Fuel Cell (SOFC) is a kind of efficient, free of contamination Blast Furnace Top Gas Recovery Turbine Unit (TRT), and at present, that the structure of SOFC mainly contains is flat, tubular type and corrugated three kinds.Flat SOFC has the element manufacturing and assembling is simple, production cost is low and characteristics such as power density height, and its cost performance is better than tubular type and corrugated SOFC, is the focus of development both at home and abroad.Flat SOFC chief component is: the electrochemical cell monomer, the metal connector that has gas passage and the encapsulant between battery cell and metal connector that are made of electrolyte both sides composite cathode and anode.For the chemical energy in the fuel gas is converted into electric energy, the anode-side of SOFC battery cell must be exposed to fuel gas, and cathode side must be exposed in the air, and all component all is in 600 ℃ or the higher temperature environment.For guaranteeing the operate as normal of SOFC, encapsulant must provide enough air-tightness, guarantees that two kinds of working gass do not mix; Sufficient electrical insulating property must be provided between battery cell and metal connector.In addition, encapsulant preferably also possesses features such as chemical compatibility between long-term stability, heat-resisting cyclicity and adjacent component and low cost of manufacture, reliability height.
At present, the encapsulating method of flat SOFC mainly contains two kinds, firmly sealing and means of press seals.Hard sealing is meant that encapsulant is connected firmly with the SOFC inter-module, encapsulant can not produce the sealing means of plastic deformation after the sealing-in, and its advantage is that air-tightness is good.This class encapsulant is representative with glass and glass-ceramic material.Glass and glass-ceramic base encapsulant are easy to scale preparation, sealing-in is simple, with low cost, also have some inevitable defectives simultaneously.The thermal coefficient of expansion of glass or glass-ceramic material and adjacent component can not mate fully, can produce stress in the thermal cycle process, because the fragility of glass self can cause breaking and losing efficacy.Glass belongs to the astable phase of thermodynamics, under the long term high temperature condition, and the trend of oriented more stable crystal transition (crystallization), the variation that may bring volume, thermal coefficient of expansion, internal stress etc. thus, will shorten dramatically useful life.Also there is deficiency in the chemical compatibility of glass and glass-ceramic material and battery cell, there are some researches show the alkali metal meeting Poisoning cathode that comprises in the glass material, causes SOFC power to descend.
Means of press seals is meant by by external force encapsulant and parts to be sealed being compressed and realizes that sealing, its advantage are not need accurate heat coupling between encapsulant and adjacent component.The encapsulant of available technology adopting means of press seals mode mainly contains mica and ceramic blankets.Mica needs bigger impressed pressure just can provide sufficient sealing, but excessive impressed pressure might damage the dielectric substrate of battery cell in the practical operation.Occurred some mica-based composite materials in the prior art,, and in mica, flooded some phase as the silver foil that adds glassy layer or flexibility at the interface between mica and adjacent component.Although these technology have improved the air-tightness of mica under less impressed pressure, all increased the complexity of sealing.The problem of mica-based encapsulant maximum is meeting seepage mineral matter in battery, makes catalyst poisoning.Ceramic blankets or the ceramic blankets of having flooded a large amount of tiny solid particles need equally big impressed pressure just can provide enough sealings.In addition, because the inconsistency in the sealing manufacture of materials process is difficult to guarantee the effectively formation of sealing.
Therefore, this area needs a kind of suitable industrial production control, the reliable SOFC encapsulant of steady quality, to alleviate the difficulty of prior art.
Summary of the invention
The invention provides a kind of Solid Oxide Fuel Cell encapsulant, purpose is that chemical stability and electrical insulating property are good under the SOFC operational environment, and sealing reliability height, and overcome the problem that exists in the existing means of press seals material, the encapsulating method that uses this material is provided simultaneously, is applicable to the sealing of flat SOFC and other similar pottery and metal.
Solid Oxide Fuel Cell encapsulant of the present invention comprises solid particle and organic binder bond and plasticizer, and the mass ratio of solid particle and organic binder bond, these two kinds of material sums of plasticizer is 100: 20~40; Described solid particle is the composition that constitutes of ceramic particle and glass micro mist or ceramic particle and the composition of metal fine powder, these two kinds of materials formations of glass micro mist, described ceramic particle be in aluminium oxide, zirconia, titanium dioxide or the magnesium oxide one or both; Described metal fine powder be in aluminium, titanium, magnesium or the silicon one or both, it is characterized in that:
(1) ratio of quality in the solid particle gross mass of the quality of glass micro mist or glass micro mist, these two kinds of material sums of metal fine powder is 5~35%; (2) described glass micro mist softens in the SOFC working temperature but does not condense, and wherein the total content of sodium oxide molybdena and potassium oxide is less than 0.3%; (3) size accounts for ratio 〉=80% of solid particle gross mass at the solid particle of 0.5~6 mu m range.
Described Solid Oxide Fuel Cell encapsulant, it is characterized in that: described solid particle is made up of the different solid particle of two parts average-size, mass ratio is: the solid particle 60~80% that average-size is big, the solid particle 20~40% that average-size is little, bulky grain average-size are more than 3 times of granule average-size.
Described Solid Oxide Fuel Cell encapsulant is characterized in that: the mass ratio of (1) solid particle and organic binder bond, these two kinds of material sums of plasticizer is 100: 20~28; (2) ratio of the quality of glass micro mist in the solid particle gross mass is 10~25%; The ratio of quality in the solid particle gross mass of glass micro mist, these two kinds of material sums of metal fine powder is 15~25%; (3) size accounts for ratio 〉=60% of solid particle gross mass less than the solid particle of 3 μ m.
Described Solid Oxide Fuel Cell encapsulant is characterized in that: the average particle size particle size of metal fine powder and glass micro mist is less than the average particle size particle size of ceramic particle.
Use the encapsulating method of described Solid Oxide Fuel Cell with encapsulant, comprising: (1) material preparation process cuts into described encapsulant the diaphragm seal that requires size; (2) installation step directly the shop spreads on diaphragm seal to need the zone that seals in the battery pile, press connector pedestal, diaphragm seal, battery cell, diaphragm seal, connector, diaphragm seal, battery cell, diaphragm seal, connector order, and the rest may be inferred, the formation battery pile; (3) pressurization steps applies 150~700kPa pressure to the outermost connector of battery pile on perpendicular to the sealing surface direction; (4) heating step slowly is warming up to the Solid Oxide Fuel Cell working temperature with the battery pile that assembles, 1~3 ℃/min of programming rate.
Described use Solid Oxide Fuel Cell is characterized in that in (1) described material preparation process with the encapsulating method of encapsulant, cut into diaphragm seal after, place forcing press to carry out precompressed, pressure is 5~30MPa, pressurize 5~10min; (2) described installation step process is: apply the ground floor diaphragm seal in the shop, position that has on the connector pedestal of gas passage, desire is placed battery cell, put battery cell again, the periphery of battery cell is pressed on this layer diaphragm seal, apply second layer diaphragm seal in the periphery shop of battery cell again, put second layer connector then, repave on it and apply the three-layer sealed, the rest may be inferred, forms battery pile; (3) in the described heating step, programming rate is 1~1.5 ℃/min; Perhaps programming rate is 1.5~3 ℃/min, at 200 ℃ of insulation 1~2h.
Described Solid Oxide Fuel Cell with the encapsulant preparation process is: according to the raw material proportioning of described solid particle or solid particle and ceramic fibre, weighing needed raw material; Add ceramic grinding ball, solvent and dispersant successively in ball grinder, add raw material again, ball milling fully disperses raw material, adds organic binder bond and plasticizer then successively, and ball milling makes it to form slurry stable, modest viscosity once more; Slurry is carried out vacuum degassing handle, curtain coating can obtain described encapsulant after 25 ℃ of left and right sides air dry a period of times then.
Encapsulant required thickness of the present invention is even, is convenient to by required form cutting or punching, and has pliability preferably.Have only encapsulant to have pliability preferably, just be implemented under the less impressed pressure easily and adjacent component closely cooperates, even there are certain roughness in battery cell or connector surface, encapsulant can be out of shape and adapt with it, thereby can guarantee to obtain good sealing effectiveness.
Organic principle in the encapsulant of the present invention can be burnt in temperature-rise period, and remaining whole or major part all is a ceramic particle, and metal fine powder is the stable ceramic phase of oxidation generation gradually, glass also can be in the SOFC operational environment stable existence.These characteristics determined they in the SOFC operational environment, have good chemical stability and electrical insulating property.
Encapsulant of the present invention can not provide airtight sealing fully, in order to realize effective seal, must reduce the size of leakage path in the material and the tortuosity of increase gas leakage approach as far as possible.Therefore, selected solid particle As soon as possible Promising Policy closestpacking, and reduce the size of solid particle as far as possible.In addition, consider that particle is reduced to a certain degree, below 0.5 μ m, reunite easily, influence the tightly packed of particle, bring difficulty for the dispersion process in the material preparation process.Whole or most of solid particles have micron or other size of submicron order among the present invention, and wherein size accounts for ratio 〉=80% of solid particle gross mass at the solid particle of 0.5~6 mu m range; The less part of particle size can comprise average particle size particle size in the solid particle and reach the less two parts of average particle size particle size more greatly, so that can be filled in the gap of particle size major part particle.
For further improving the reliability of material seal, the invention provides two kinds of Basic Ways: (1) adds metal fine powder, one side utilizes the reaction bonding of metal several ceramic particles to be connected into the particle chain or the particle cluster in irregular shape of staggered interlock, improved the energy to failure of material, another aspect, there is certain volumetric expansion during burning, can the blocking portion leakage path, help promoting the sealing effectiveness of material.But consider and add the electrical insulating property that metal may have influence on material, select for use the ratio of metal fine powder quality in the solid particle gross mass should be less than 30%.(2) add the glass micro mist, owing to selected glass can soften in the SOFC working temperature, under the impressed pressure effect, ceramic particle can be embedded in the glassy phase, not only improve the energy to failure of material, and improved the compactness extent of material, thereby can promote the reliability of material seal.Consider when glass micro mist addition is more too much that problems that appear in the glass-ceramic material also can display, thereby select for use the ratio of quality in the solid particle gross mass of glass micro mist should be less than 35%.
Be used for further to carry out precompressed before the SOFC heap to diaphragm seal.Because precompressed step institute plus-pressure can reach more than tens of MPas, the density of diaphragm seal can be greatly improved, and still, excessive preload pressure may cause diaphragm seal to encounter difficulties when press takes off, therefore preload pressure generally is controlled at 5~30Mpa, and pressurize 5~10min.
The sealing effectiveness of encapsulant of the present invention and impressed pressure have bigger relation, and impressed pressure is big more usually, and sealing effectiveness is good more.Under 150~700Kpa impressed pressure condition, the leak rate of encapsulant of the present invention usually can be less than 0.1mL/min/cm, and the encapsulant leak rate of adding metal fine powder or glass micro mist can be lower.Because ceramic particle is at SOFC working temperature sintering not, material can be slightly crooked, meets to expand or contraction can not broken yet, even and when having hot difference between adjacent component, particle can slide mutually, and does not damage the validity of material seal.
Encapsulant chemical stability of the present invention and electrical insulating property are good, and the preparation method is simple, suitability for industrialized production; Assembling simply can closely be mated with adjacent component under less impressed pressure during use, favorable sealing property, even and have certain thermal mismatching between adjacent component, also can keep good sealability.
Description of drawings
Fig. 1 is the structural representation of a kind of flat SOFC heap sealing, has showed the position of encapsulant of the present invention;
Fig. 2 is to be that the encapsulant that the alumina particle of 3 μ m constitutes uses the electron scanning micrograph of back under 2000 times by average grain diameter all;
Fig. 3 is to be that the encapsulant that the alumina particle of 3 μ m and aluminium micro mist that the 20wt% average grain diameter is 1.5 μ m constitute uses the electron scanning micrograph of back under 2000 times by the 80wt% average grain diameter;
Fig. 4 is to be that the encapsulant that the alumina particle of 3 μ m and ceramic alumina fiber that the 20wt% average diameter is 2 μ m constitute uses the electron scanning micrograph of back under 2000 times by the 80wt% average grain diameter.
Embodiment
The raw material mass mixture ratio of embodiment 1~20 sees Table 1~3.
The proportioning of table 1 ceramic particle, metal fine powder, organic binder bond and plasticizer
Annotate: institute's solid particles particle diameter is the average grain diameter of solid particle in the table.
The proportioning of table 2 ceramic particle, metal fine powder, glass micro mist, organic binder bond and plasticizer
Annotate: institute's solid particles particle diameter is the average grain diameter of solid particle in the table.
* 1 refers to that glass herein is BaO-Al
2O
3-CaO-SiO
2Glass, softening but do not condense in the SOFC working temperature, wherein BaO, Al
2O
3, CaO and SiO
2Shared quality proportion is respectively 40.8%, 2.5%, 8.4% and 35.3%; Oxygen-free sodium and potassium oxide.
The proportioning of table 3 ceramic particle, ceramic fibre, metal fine powder, glass micro mist, organic binder bond and plasticizer
Annotate: institute's solid particles particle diameter is the average grain diameter of solid particle in the table.
*2 refer to that glass herein is BaO-B2O3-MgO-ZnO-SiO2 glass, and softening but do not condense in the SOFC working temperature, wherein the shared quality proportion of BaO, B2O3, MgO, ZnO and SiO2 is respectively 25.5%, 17.5%, 13.4%, 13.5% and 30.1%; Oxygen-free sodium and potassium oxide.
Among the embodiment 1~6, solid particle is only arranged, be ceramic particle.Size accounts for the ratio of solid particle gross mass all greater than 80% at the solid particle of 0.5~6 mu m range.Wherein size accounts for ratio 〉=60% of solid particle gross mass among the embodiment 1~3 less than the solid particle of 3 mu m ranges; The mass ratio of embodiment 3~6 solid particles and organic binder bond+plasticizer is 100: 20~28; The solid particle 60~80% that average-size is big among the embodiment 4~6, the solid particle 20~40% that average-size is little, the bulky grain average-size is more than 3 times of granule average-size.
Among the embodiment 7~10, solid particle is only arranged, be ceramic particle and metal fine powder.Size accounts for the ratio of solid particle gross mass all greater than 80% at the solid particle of 0.5~6 mu m range.Wherein size accounts for ratio 〉=60% of solid particle gross mass among the embodiment 7,8 less than the solid particle of 3 mu m ranges; The ratio of metal fine powder quality in the solid particle gross mass is 10~20% among the embodiment 9 and 10; The average particle size particle size of embodiment 8,9 and 10 metal fine powders is less than the average particle size particle size of ceramic particle.
Among the embodiment 11~20, solid particle is only arranged, be ceramic particle and glass micro mist or ceramic particle, metal fine powder and glass micro mist.Size accounts for the ratio of solid particle gross mass all greater than 80% at the solid particle of 0.5~6 mu m range.Wherein the mass ratio of embodiment 15 solid particles and organic binder bond+plasticizer is 100: 20~28; The ratio of quality in the solid particle gross mass of embodiment 16,17 glass micro mists is 10~25%; The average particle size particle size of embodiment 16,17,18 metal fine powders and glass micro mist is less than the average particle size particle size of ceramic particle; The ratio of quality in the solid particle gross mass of embodiment 18,19,20 glass micro mist+metal fine powders is 15~25%.
Among the embodiment 21~28, be the situation of solid particle and ceramic fibre combination.Diameter accounts for ratio 〉=75% of ceramic fibre gross mass less than the ceramic fibre of 3 μ m.The mass ratio of embodiment 24 solid particles+ceramic fibre and organic binder bond+plasticizer is 100: 20~28; The percentage that embodiment 25~28 ceramic fibres account for solid particle and ceramic fibre gross mass is 10~15%; The ratio of quality in the solid particle gross mass of embodiment 27,28 glass micro mist+metal fine powders is 15~25%; The average particle size particle size of embodiment 25~28 metal fine powders and glass micro mist is less than the average particle size particle size of ceramic particle.
The preparation of embodiment 29 encapsulants
According to the raw material proportioning of embodiment in the table 14 respectively weighing 70g average grain diameter be the Al of 3 μ m
2O
3Ceramic particle and 30g average grain diameter are the Al of 0.6 μ m
2O
3Ceramic particle, total amount 100g.In ball grinder, add 300g zirconia ball, 68ml dimethylbenzene/alcohol mixed solution and 2g herring oil successively, the ceramic particle that adds total amount 100g again, ball milling 20 hours, raw material is fully disperseed, add 8g BBP, 9g PVB and 8g PAG then successively, about ball milling 24h, make it to form slurry stable, modest viscosity once more.Slurry is carried out degassing processing, curtain coating then, air dry 24h can obtain required encapsulant.
The preparation of embodiment 30 encapsulants
According to the raw material proportioning of embodiment in the table 3 23 respectively weighing 65g average grain diameter be the Al of 2.5 μ m
2O
3Ceramic particle and 15g average grain diameter are the ZrO of 0.7 μ m
2Ceramic particle, the 20g diameter is less than the Al of 2 μ m
2O
3Ceramic fibre, total amount 100g.In ball grinder, add 300g zirconia ball, 76ml dimethylbenzene/alcohol mixed solution and 2g herring oil successively, add 80g ceramic aggregate particle and 10g ceramic fibre again, add remaining 10g ceramic fibre behind the ball milling 3h again, continued ball milling 17 hours, raw material is fully disperseed, add 11gBBP, 11g PMA and 12g PAG then successively, about ball milling 24h, make it to form slurry stable, modest viscosity once more.Slurry is carried out degassing processing, curtain coating then, air dry 24h can obtain required encapsulant.
The enforcement of embodiment 31SOFC heap sealing, as shown in Figure 1:
The encapsulant of preparation among the embodiment in the table 14 is cut into the diaphragm seal that requires size.The connector pedestal 1 that will have gas passage places ground floor, place the shop, position of battery cell in desire and apply ground floor diaphragm seal 2, put battery cell 3, the periphery of battery cell just in time is pressed on this layer diaphragm seal, apply second layer diaphragm seal 2 in the periphery shop of battery cell again, put second layer metallic interconnect materials 4 then, repave and apply three-layer sealed material 2, the rest may be inferred, forms battery pile.Apply 300Kpa pressure in the battery pile external vertical in the sealing surface direction, be warming up to the sealing that the Solid Oxide Fuel Cell working temperature can realize battery pile by the programming rate of 1 ℃/min.
The enforcement of embodiment 32SOFC heap sealing, as shown in Figure 1:
The encapsulant of preparation among the embodiment 23 is cut into the diaphragm seal that requires size, precompressed on hydraulic press, pressure 20Mpa, and voltage stabilizing 10 minutes.The connector pedestal 1 that will have gas passage places ground floor, place the shop, position of battery cell in desire and apply ground floor diaphragm seal 2, put battery cell 3, the periphery of battery cell just in time is pressed on this layer diaphragm seal, apply second layer diaphragm seal 2 in the periphery shop of battery cell again, put second layer metallic interconnect materials 4 then, repave and apply three-layer sealed material 2, the rest may be inferred, forms battery pile.Apply 500Kpa pressure in the battery pile external vertical in the sealing surface direction, programming rate by 2 ℃/min is warming up to 200 ℃, at 200 ℃ of insulation 1.5h, continue then to be warming up to the Solid Oxide Fuel Cell working temperature by the programming rate of 2 ℃/min, can realize the sealing of battery pile.
Claims (6)
1. a Solid Oxide Fuel Cell encapsulant comprises solid particle and organic binder bond and plasticizer, and the mass ratio of solid particle and organic binder bond, these two kinds of material sums of plasticizer is 100: 20~40; Described solid particle is the composition that constitutes of ceramic particle and glass micro mist or ceramic particle and the composition of metal fine powder, these two kinds of materials formations of glass micro mist, described ceramic particle be in aluminium oxide, zirconia, titanium dioxide or the magnesium oxide one or both; Described metal fine powder be in aluminium, titanium, magnesium or the silicon one or both, it is characterized in that:
(1) ratio of quality in the solid particle gross mass of the quality of glass micro mist or glass micro mist, these two kinds of material sums of metal fine powder is 5~35%; (2) described glass micro mist softens in the SOFC working temperature but does not condense, and wherein the total content of sodium oxide molybdena and potassium oxide is less than 0.3%; (3) size accounts for ratio 〉=80% of solid particle gross mass at the solid particle of 0.5~6 mu m range.
2. Solid Oxide Fuel Cell encapsulant as claimed in claim 1, it is characterized in that: described solid particle is made up of the different solid particle of two parts average-size, mass ratio is: the solid particle 60~80% that average-size is big, the solid particle 20~40% that average-size is little, bulky grain average-size are more than 3 times of granule average-size.
3. Solid Oxide Fuel Cell encapsulant as claimed in claim 1 or 2 is characterized in that: the mass ratio of (1) solid particle and organic binder bond, these two kinds of material sums of plasticizer is 100: 20~28; (2) ratio of the quality of glass micro mist in the solid particle gross mass is 10~25%; The ratio of quality in the solid particle gross mass of glass micro mist, these two kinds of material sums of metal fine powder is 15~25%; (3) size accounts for ratio 〉=60% of solid particle gross mass less than the solid particle of 3 mu m ranges.
4. Solid Oxide Fuel Cell encapsulant as claimed in claim 3 is characterized in that: the average particle size particle size of metal fine powder and glass micro mist is less than the average particle size particle size of ceramic particle.
5. use claim 1 or the 2 described Solid Oxide Fuel Cell encapsulating method with encapsulant, comprising: (1) material preparation process cuts into described encapsulant the diaphragm seal that requires size; (2) installation step directly the shop spreads on diaphragm seal to need the zone that seals in the battery pile, press connector pedestal, diaphragm seal, battery cell, diaphragm seal, connector, diaphragm seal, battery cell, diaphragm seal, connector order, and the rest may be inferred, the formation battery pile; (3) pressurization steps applies 150~700kPa pressure to the outermost connector of battery pile on perpendicular to the sealing surface direction; (4) heating step slowly is warming up to the Solid Oxide Fuel Cell working temperature with the battery pile that assembles, 1~3 ℃/min of programming rate.
6. as the encapsulating method of use Solid Oxide Fuel Cell as described in the claim 5, it is characterized in that in (1) described material preparation process with encapsulant, cut into diaphragm seal after, place forcing press to carry out precompressed, pressure is 5~30MPa, pressurize 5~10min; (2) described installation step process is: apply the ground floor diaphragm seal in the shop, position that has on the connector pedestal of gas passage, desire is placed battery cell, put battery cell again, the periphery of battery cell is pressed on this layer diaphragm seal, apply second layer diaphragm seal in the periphery shop of battery cell again, put second layer connector then, repave on it and apply the three-layer sealed, the rest may be inferred, forms battery pile; (3) in the described heating step, programming rate is 1~1.5 ℃/min; Perhaps programming rate is 1.5~3 ℃/min, at 200 ℃ of insulation 1~2h.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2007100525194A CN100448066C (en) | 2007-06-20 | 2007-06-20 | A sealing material of solid oxide fuel cell and its sealing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2007100525194A CN100448066C (en) | 2007-06-20 | 2007-06-20 | A sealing material of solid oxide fuel cell and its sealing method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101079476A CN101079476A (en) | 2007-11-28 |
CN100448066C true CN100448066C (en) | 2008-12-31 |
Family
ID=38906798
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB2007100525194A Expired - Fee Related CN100448066C (en) | 2007-06-20 | 2007-06-20 | A sealing material of solid oxide fuel cell and its sealing method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN100448066C (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102701591A (en) * | 2012-06-07 | 2012-10-03 | 上海大学 | Laser packaged glass powder sealing material for photoelectric device packaging |
CN103319819B (en) * | 2013-05-27 | 2015-10-28 | 镇江春环密封件集团有限公司 | A kind of rubber seal |
CN106739606B (en) * | 2016-12-16 | 2018-11-09 | 娄底市安地亚斯电子陶瓷有限公司 | A kind of power battery ceramic-seal ring insurance electrode preparation method |
CN107021635B (en) * | 2017-04-26 | 2020-02-04 | 南京广兆测控技术有限公司 | Glass solder and preparation method thereof |
CN108054408A (en) * | 2017-12-15 | 2018-05-18 | 武汉华科福赛新能源有限责任公司 | A kind of solid-oxide fuel cell stack compression sealing material and preparation method thereof |
CN109761585B (en) * | 2019-03-06 | 2020-05-01 | 娄底市安地亚斯电子陶瓷有限公司 | Power battery ceramic sealing material and application thereof |
CN109748574B (en) * | 2019-03-06 | 2021-08-31 | 娄底市安地亚斯电子陶瓷有限公司 | Ceramic connecting material and application thereof |
CN109761589A (en) * | 2019-03-15 | 2019-05-17 | 沈阳君威新能科技有限公司 | A kind of ceramics thermal battery inertia block ring and preparation method thereof |
CN112928299B (en) * | 2019-12-06 | 2022-10-18 | 中国科学院大连化学物理研究所 | High-temperature composite sealing material and application thereof |
CN111707419B (en) * | 2020-07-01 | 2022-05-03 | 郑州佛光发电设备有限公司 | Detection method for simulating sealing performance of fuel cell at target temperature |
CN113381049B (en) * | 2021-06-09 | 2022-04-12 | 广东石油化工学院 | SOFC cell stack of button type fuel cell integrated fuel reformer |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1454398A (en) * | 2000-08-18 | 2003-11-05 | 全球热电公司 | High temperature gas seals |
WO2004010523A2 (en) * | 2002-07-23 | 2004-01-29 | Global Thermoelectric Inc. | High temperature gas seals |
CN1494176A (en) * | 2003-09-03 | 2004-05-05 | �й���ѧԺ�����о��� | Medium and high temperature sealing method of plate type solid oxide fuel battery and its sealing material |
WO2004059761A2 (en) * | 2002-12-24 | 2004-07-15 | Global Thermoelectric Inc. | High temperature gas seal |
CN2714310Y (en) * | 2004-04-14 | 2005-08-03 | 中材科技股份有限公司 | Ceramic fiber laminated board |
CN1746252A (en) * | 2004-09-06 | 2006-03-15 | 中国科学技术大学 | The sealing agent of intermediate temperature solid oxide fuel cell |
-
2007
- 2007-06-20 CN CNB2007100525194A patent/CN100448066C/en not_active Expired - Fee Related
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1454398A (en) * | 2000-08-18 | 2003-11-05 | 全球热电公司 | High temperature gas seals |
WO2004010523A2 (en) * | 2002-07-23 | 2004-01-29 | Global Thermoelectric Inc. | High temperature gas seals |
WO2004059761A2 (en) * | 2002-12-24 | 2004-07-15 | Global Thermoelectric Inc. | High temperature gas seal |
CN1494176A (en) * | 2003-09-03 | 2004-05-05 | �й���ѧԺ�����о��� | Medium and high temperature sealing method of plate type solid oxide fuel battery and its sealing material |
CN2714310Y (en) * | 2004-04-14 | 2005-08-03 | 中材科技股份有限公司 | Ceramic fiber laminated board |
CN1746252A (en) * | 2004-09-06 | 2006-03-15 | 中国科学技术大学 | The sealing agent of intermediate temperature solid oxide fuel cell |
Also Published As
Publication number | Publication date |
---|---|
CN101079476A (en) | 2007-11-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100448066C (en) | A sealing material of solid oxide fuel cell and its sealing method | |
CA2419334C (en) | High temperature gas seals | |
KR102126944B1 (en) | Gasket for fuel cells | |
EP1500157B1 (en) | Multi-layer seal for electrochemical devices | |
EP1590840B1 (en) | High temperature gas seal | |
CN101072676A (en) | Glass and glass-ceramic sealant compositions | |
CN102723448B (en) | Sealing material of medium temperature plate type solid-oxide fuel battery stack and sealing method | |
CN105103352A (en) | Sanbornite-based glass-ceramic seal for high-temperature applications | |
EP2104172A1 (en) | A composite glass seal for a solid oxide electrolyser cell stack | |
KR20060093643A (en) | Methods of sealing solid oxide fuel cells | |
JP5451653B2 (en) | Gas seal material | |
JP3495654B2 (en) | Cell tube seal structure | |
CN103443978A (en) | Bonding material for solid oxide fuel cell, solid oxide fuel cell and solid oxide fuel cell module | |
CN104505527B (en) | A kind of middle temperature plate type solid-oxide fuel battery pile sealer and preparation method thereof | |
JP3331313B2 (en) | Electrolyte matrix for molten carbonate fuel cells | |
CN102299350A (en) | Diaphragm of molten carbonate fuel cell and preparation of diaphragm with composite pore structure | |
CN109075363B (en) | Solid oxide fuel cell | |
EP2104171A1 (en) | Deformable glass based composite seal for high temperature application | |
US20060286428A1 (en) | Composite sealing structure for SOFC modules and stacks and related method | |
CN113113664A (en) | Modified NASICON type sodium ion ceramic electrolyte and preparation method and application thereof | |
CN112928299B (en) | High-temperature composite sealing material and application thereof | |
KR100693938B1 (en) | High temperature sealiong material for solid oxide fuel cell | |
CN1812159A (en) | Mesotherm hermetic glass and hermetic method for solid oxide fuel cell | |
KR101209983B1 (en) | Manufacturing method of the glass-ceramics gasket for solid oxide fuel cell | |
KR101013845B1 (en) | Manufacturing Method of Sealing Glass for Intermediate Temperature Planar SOFC |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081231 Termination date: 20150620 |
|
EXPY | Termination of patent right or utility model |