Integrated fluorine gasket manufactured by injection molding for hydrogen fuel cells
09640807 ยท 2017-05-02
Assignee
- Hyundai Motor Company (Seoul, KR)
- Donga Manufacturing Corp. (Ansan, Gyeonggi-do, KR)
- E.I. Du Pont De Nemours And Company (Wilmington, DE)
Inventors
- Bo Ki Hong (Seoul, KR)
- Byeong Heon Jeong (Gyeonggi-Do, KR)
- Seung Kyung Ko (Gyeonggi-do, KR)
- Stephen Bowers (Le Grand Sacconex, CH)
- Ho Jin Lee (Incheon, KR)
- Yoon Gue Choi (Gyeonggi-do, KR)
Cpc classification
B32B15/06
PERFORMING OPERATIONS; TRANSPORTING
C08L27/16
CHEMISTRY; METALLURGY
Y02P70/50
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
B32B25/14
PERFORMING OPERATIONS; TRANSPORTING
H01M8/0273
ELECTRICITY
C08L27/20
CHEMISTRY; METALLURGY
H01M8/0271
ELECTRICITY
Y02E60/10
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
Y02E60/50
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
B32B25/04
PERFORMING OPERATIONS; TRANSPORTING
International classification
B32B15/06
PERFORMING OPERATIONS; TRANSPORTING
C08L27/20
CHEMISTRY; METALLURGY
C08L27/16
CHEMISTRY; METALLURGY
H01M8/0271
ELECTRICITY
H01M8/0273
ELECTRICITY
B32B25/04
PERFORMING OPERATIONS; TRANSPORTING
B32B25/14
PERFORMING OPERATIONS; TRANSPORTING
Abstract
Disclosed is an integrated fluorine gasket manufactured by injection molding for hydrogen fuel cells. In particular, a fluorine compound having a fluorine content of about 60 to 75 parts by weight based on 100 parts by weight of a fluoroelastomer is disposed in a gasket. The resulting fluorine gasket is integrated with a thin bipolar plate having a thickness of about 200 m or less to have a thickness of about 750 m or less by injection molding on the thin bipolar plate and by cross-linking.
Claims
1. An integrated fluorine gasket manufactured by injection molding for hydrogen fuel cells, wherein the integrated fluorine gasket comprises a fluorine compound and a thin bipolar plate, wherein the thin bipolar plate has a thickness of about 200 m or less, wherein the fluorine compound is injection molded on the thin bipolar plate and first cross-linked, wherein the integrated fluorine gasket has a thickness of about 750 m or less, wherein the fluorine compound comprising a fluoroelastomer has a fluorine content of about 60 to 75 parts by weight based on 100 parts by weight of the fluoroelastomer, wherein the fluorine compound has Mooney viscosity of about 10 to 24 in a condition of ISO 289-1(2005): ML(1+4)/125 C., and wherein the fluorine compound has a scorch time of about 1.7 to 3.0 minutes that is measured by using a moving die rheometer (MDR) based on ISO 6502:1999(E) in a condition of temperature about 185 C./oscillation amplitude 0.5/time 10 minutes.
2. The integrated fluorine gasket of claim 1, wherein, the fluorine compound is secondly post-cross-linked at a temperature of at least 200 C.
3. The integrated fluorine gasket of claim 1, wherein the fluorine compound has shore A hardness of about 35 to 65 in a condition of ASTM D2240.
4. The integrated fluorine gasket of claim 1, wherein the fluorine compound has about a 90% cure time of about 3.5 to 5.0 minutes that is measured by using a moving die rheometer (MDR) based on ISO 6502:1999(E) in a condition of temperature 185 C./oscillation amplitude 0.5/time 10 minutes.
5. The integrated fluorine gasket of claim 1, wherein the fluorine compound has M of at least 10.5 dN.Math.m that is a difference between highest torque and minimum torque by using a moving die rheometer (MDR) based on ISO 6502:1999(E) in a condition of temperature 185 C./oscillation amplitude 0.5/time 10 minutes.
6. The integrated fluorine gasket of claim 1, wherein the fluorine compound has a filling percentage of spider mold flow of 75% or more by using a 1.6 mm-sprue in a condition of temperature 180 C./pressure 6 MPa/time 7 minutes.
7. The integrated fluorine gasket of claim 1, wherein the fluorine gasket formed from the fluorine compound on the bipolar plate has a compression set of about 4% or less as a fluorine gasket in a condition of ASTM D395 (Method B, 25% Deflection, 150 C./72 hours).
8. The integrated fluorine gasket of claim 1, wherein fluorine gasket formed from the fluorine compound on the bipolar plate has a compression set of about 9% or less as a fluorine gasket in a condition of ASTM D395 (Method B, 25% Deflection, 150 C./336 hours).
9. The integrated fluorine gasket of claim 1, wherein the fluorine gasket formed from the fluorine compound on the bipolar plate comprises a fluorine gasket in which, when a degree of deformation of the thin bipolar plate is measured in 15 positions of the thin bipolar plate by using a contour measuring device, wherein the bipolar plate has an average value of degrees of deformation of less than 60 m.
10. The integrated fluorine gasket of claim 1, wherein the fluorine gasket formed from the fluorine compound on the bipolar plate has compressibility of about 65 to 85%.
11. The integrated fluorine gasket of claim 1, wherein the fluoroelastomer comprises binary copolymer containing vinylidene fluoride (VDF) and hexafluoropropene (HFP).
12. An integrated fluorine gasket manufactured by injection molding for hydrogen fuel cells, wherein the integrated fluorine gasket comprises a fluorine compound and a thin bipolar plate, wherein the thin bipolar plate has a thickness of about 200 m or less, wherein the fluorine compound is injection molded on the thin bipolar plate and first cross-linked, wherein the integrated fluorine gasket has a thickness of about 750 m or less, wherein the fluorine compound comprising a fluoroelastomer has a fluorine content of about 60 to 75 parts by weight based on 100 parts by weight of the fluoroelastomer, wherein the fluorine compound has Mooney viscosity of about 10 to 24 in a condition of ISO 289-1(2005): ML(1+4)/125 C., wherein the fluorine compound has M of at least 10.5 dN.Math.m that is a difference between highest torque and minimum torque by using a moving die rheometer (MDR) based on ISO 6502:1999(E) in a condition of temperature 185 C./oscillation amplitude 0.5/time 10 minutes.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The above and other features and advantages of the present invention will become more apparent by describing in detail exemplary embodiments thereof with reference to the attached drawings in which:
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DETAILED DESCRIPTION OF THE INVENTION
(12) The present invention will now be described more fully with reference to the accompanying drawings, in which exemplary embodiments of the invention are shown.
(13) The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used herein, the singular forms a, an and the are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms comprises and/or comprising, when used in this specification, specify the presence of stated features, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof. As used herein, the term and/or includes any and all combinations of one or more of the associated listed items.
(14) Unless specifically stated or obvious from context, as used herein, the term about is understood as within a range of normal tolerance in the art, for example within 2 standard deviations of the mean. About can be understood as within 10%, 9%, 8%, 7%, 6%, 5%, 4%, 3%, 2%, 1%, 0.5%, 0.1%, 0.05%, or 0.01% of the stated value. Unless otherwise clear from the context, all numerical values provided herein are modified by the term about.
(15) Fluoroelastomer may be manufactured as a copolymer by copolymerizing various monomers. Representative monomers include vinylidene fluoride (VDF), tetrafluoroethylene (TFE), hexafluoropropene (HFP), and perfluoroalkyl vinyl ether (PAVE).
(16) Preferably, only binary or ternary copolymer including these monomers, or copolymer that is blended with another at least one thermoplastic/thermoset)/rubber polymer or is mixed with organic/inorganic materials, may be used as a material for a fluorine gasket for a stack for hydrogen fuel cell vehicles.
(17) An integrated fluorine gasket manufactured by injection molding for hydrogen fuel cells according to the exemplary embodiment of the present invention is characterized by including VDF and HFP, by using a fluorine compound having a fluorine content of about 60 to 75 parts by weight based on 100 parts by weight of a fluoroelastomer as a binary copolymer compound in a gasket, and by integrating a fluorine gasket by injection molding the fluorine gasket on a thin bipolar plate having a thickness of about 200 m or less to have a thickness of about 750 m or less and by crosslinking the fluorine gasket.
(18) In this case, the fluorine content of the fluoroelastomer may be about 60 to 75 parts by weight based on 100 parts by weight of the fluoroelastomer. This is because, if the fluorine content is less than about 60 parts by weight, unique and excellent characteristics of the fluoroelastomer, such as thermal resistance, resistance to chemistry, and resistance to hydrolysis described above, are lowered and if the fluorine content exceeds about 75 parts by weight, low temperature flexibility of the fluoroelastomer is greatly lowered and thus the fluoroelastomer cannot be easily used at a low temperature (e.g., less than 0 C.).
(19) Here, for better understanding, after describing an existing comparative example, an embodiment of the present invention will be described below.
Comparative Example
(20) A ternary copolymer compound including VDF, HFP, and TFE among conventional commercialized fluorine-based elastomers and having a fluorine content of 66 parts by weight based on 100 parts by weight of a fluoroelastomer was used as a fluorine compound in a comparative example. Like in the following embodiment, even in the comparative example, a fluorine compound is based on the fluoroelastomer. The fluorine compound was manufactured by adding a crosslinking agent, a co-agent or an accelerator, an acid scavenger, an activator, a filler, and other additives to the fluoroelastomer-based fluorine compound, and bisphenol was used as the crosslinking agent.
(21) In order to compare an injection molding processability of gaskets in an injection molding machine actually used in a gasket for hydrogen fuel cells, as an example for manufacturing a fluorine gasket according to the comparative example, a fluorine gasket was manufactured in the same manner as the above-described manufacturing example of the embodiment and was used.
Exemplary Embodiment
(22) A binary copolymer compound including VDF and HFP among conventional commercialized fluorine-based elastomers and having a fluorine content of 66 parts by weight based on 100 parts by weight of a fluoroelastomer was used as a fluorine compound in the exemplary embodiment of the present invention. The fluorine compound according the present embodiment has low Mooney viscosity compared to the comparative example, has high fluidity and simultaneously high crosslinking density and thus is designed to further increase elasticity.
(23) The fluorine compound according to the present exemplary embodiment is based on the fluoroelastomer. The fluorine compound was manufactured by adding a crosslinking agent, a co-agent or an accelerator, an acid scavenger, an activator, a filler, and other additives to the fluoroelastomer-based fluorine compound.
(24) The fluorine compound according to the present exemplary embodiment may use a crosslinking agent as preferably only one among bisphenol/organic peroxide/diamine or by mixing two or more bisphenol/organic peroxide/diamine, and in the present embodiment, bisphenol was used as the crosslinking agent.
(25) In an exemplary embodiment of the present invention, since a bipolar plate that is actually used in hydrogen fuel cell vehicles needs to be sufficiently thin so as to attain a high output in a limited amount of space, a bipolar plate having a thickness of 200 m or less is adopted. In addition, the thickness of a gasket that is to be integrated with the bipolar plate by injection molding on the bipolar plate, may be as small as possible in a range in which sealing can still be maintained. In order to mount the gasket on a hydrogen fuel cell vehicle, the gasket may, for example, have a thickness of 750 m or less.
(26) Thus, in order to compare an injection molding processability of gaskets in an injection molding machine to be actually used in a gasket for a hydrogen fuel cell as an example for manufacturing a fluorine gasket according to the exemplary embodiment of the present invention, a fluorine compound was injection-molded on an outside surface of a metallic thin bipolar plate having a thickness of 100 m and was first cross-linked so that a fluorine gasket was manufactured to be integrated with the metallic thin bipolar plate.
(27) In this case, a thin gasket was manufactured by controlling the thickness of a gasket that was injection-molded on the metallic thin bipolar plate so that the maximum thickness of the gasket does not exceed 680 m. The fluorine gasket that was integrated with the metallic thin bipolar plate, was secondly post-cross-linked or post-cured sufficiently at a high temperature of at least 200 C. and then was used as a gasket for a stack.
Experimental Example
(28) Material properties of the fluorine gasket according to the existing comparative example and the embodiment of the present invention, respectively, were measured as below: Hardness: Shore A hardness was measured based on ASTM D2240. Mooney viscosity: Mooney viscosity of the fluorine compound was measured in a condition of ML(1+4)/125 C. based on ISO 289-1(2005). Compression set: standard test samples were manufactured based on ASTM D395 (method B, 25% deflection) and were thermally treated at 150 C. for 72, 168, and 336 hours, respectively. Filling percentage of spider mold flow: was measured using a 1.6 mm-sprue in a condition of temperature 180 C./pressure 6 MPa/time 7 minutes. Crosslinking or curing kinetics: a crosslinking speed was calculated by measuring a cure curve by using a moving die rheometer (MDR) based on ISO 6502:1999(E) in a condition of temperature 185 C./oscillation amplitude 0.5/time 10 minutes. Degree of deformation of metallic bipolar plate: after fluorine compounds were injection-molded on a metallic bipolar plate so as to manufacture integrated gaskets, the gaskets were removed from the metallic bipolar plates and the degree of deformation of the metallic bipolar plate was measured in a quantitative manner by applying a measuring force of 30 mN by using a contour measuring instrument: Contracer CV-3000 Model, Mitutoyo Co., Japan.
(29) In this case, five metallic bipolar plates with which fluorine gaskets according to a comparative example and an exemplary embodiment of the present invention were integrated, were used and their degrees of deformation were measured, and an average value of the degrees of deformations was used, and measurement was performed in total 16 positions of each metallic bipolar plate. Repetitive compression behavior of gasket: after the fluorine compounds were sufficiently cross-linked, test samples having a similar shape to an O-ring (width 3.0 mm, area 7.257 cm.sup.2) were manufactured, and variations in thicknesses of the test samples were measured as a function of compression pressure from 0.01 to 67.6 MPa by using a commercialized compression test machine, Dae Kyung Tech., Korea. Electrochemical cell performance: first, after the fluorine gaskets according to a comparative example and an embodiment of the present invention were integrated with the metallic bipolar plate by injection molding and crosslinking, 5-cell stacks were manufactured for each example. The same MEA and the gas diffusion layer were used when stacks were manufactured according to the comparative example and the exemplary embodiment of the present invention, respectively.
(30) In addition, potential-current density polarization of fuel cell stacks including bipolar plates with which the fluorine gaskets were integrated according to the comparative example and the embodiment of the present invention was measured using existing commercialized equipment, 5 kW Test Station Model, Won-A Tech Co., Korea.
(31) In addition, in order to compare contact resistances in the stacks including the integrated fluorine gaskets according to the comparative example and the embodiment of the present invention, high frequency resistance (HFR) was measured using existing commercialized equipment, Galvanostat, Z# Navigator Model, Won-A Tech Co., Korea in a condition of amplitude of 14 mA/cm.sup.2 and a frequency of 1 kHz.
(32) In this case, electrochemical cell performance and contact resistance of the 5-cell stacks were measured in the following operation conditions. inlet temperature of a cell for a hydrogen fuel cell=65 C.; reactant gases: anode/cathode=hydrogen/air; gas pressure=near ambient pressure; hydrogen anode/air cathode relative humidity (R.H.)=100%/100%; hydrogen anode/air cathode stoichiometric ratio (S.R.)=1.5/2.0.
(33) As a result of the experimental example, the result of evaluating the material properties of the fluorine gaskets according to the existing comparative example and the embodiment of the present invention is as follows.
(34) Hardness
(35) Although a fluorine gasket having high Shore A hardness that exceeds 65 and is less than 90 has been widely in existing industries, when a gasket having such high hardness is used as a gasket for a fuel cell stack for hydrogen fuel cell vehicles, it is difficult to maintain intimate contact and a seal between several tens of repetitive components inside the stack. Thus, a gasket having hardness of 65 or less should be used.
(36) On the other hand, when the hardness is too low and is less than 35, cross-linking density is very low, and elasticity of the gasket is greatly decreased, and a compression set that is inversely proportional to elasticity exceeds a proper level. Additionally, the excessive compression of a cell may occur due to low hardness. Thus, a gasket having hardness of 35 or more should preferably be used. Thus, a fluorine gasket having Shore A hardness of about 35 to 65 may be used for a stack for hydrogen fuel cell vehicles.
(37) Thus, in the existing comparative example and the embodiment of the present invention, after fluorine gaskets having Shore A hardness of 51 were manufactured so as to make the same hardness, other general material properties and performance were measured and compared.
(38) Fluidity
(39) Mooney viscosity is a significant index indicating fluidity and may be used in approximately analogizing a molding processability of a fluorine compound before being injection molded. If Mooney viscosity is less than about 10, general material properties of the fluorine gasket, such as a mechanical property and a handling property, may be greatly lowered, and if Mooney viscosity exceeds about 26, a precise injection molding processability may be lowered so that gasket productivity may be lowered. Thus, in a gasket for a stack for hydrogen fuel cells, the fluorine compound may have Mooney viscosity of about 10 to 26.
(40) As shown in the following Table 1, although Mooney viscosity of an existing fluorine compound according to a comparative example is 27, Mooney viscosity of a fluorine compound according to an embodiment of the present invention is 21, which indicates that fluidity of the fluorine compound according to the embodiment of the present invention is higher than that of the fluorine compound according to the comparative example.
(41) TABLE-US-00001 TABLE 1 Comparative Item Unit example Embodiment Mooney viscosity 27 21 Filling percentage of spider mold % 71 78 flow
(42) A filling percentage of spider mold flow may be used as another index indicating fluidity of the fluorine compound. The filling percentage of spider mold flow may be at least 75% or more in order to precisely mold a gasket on a thin bipolar plate.
(43) As a result of measuring and comparing filling percentages of spider mold flow according to the existing comparative example and the embodiment of the present invention, as shown in the above Table 1, filling percentages of spider mold flow were measured as 71% and 78%, respectively, and the fluorine compound according to the present exemplary embodiment shows better fluidity, and thus this means that injection molding to form an actual gasket can be more precisely and easily performed.
(44) Cross-Linking Kinetics
(45) As described above, a gasket for a stack for hydrogen fuel cells is injection molded and first cross-linked on the peripheral area of a metallic bipolar plate and is manufactured as a thin gasket and then undergoes an additional secondary post-crosslinking process. Thus, it is very important to maintain an appropriate crosslinking rate when a thin gasket is injection molded in a mold. This is because, when a crosslinking rate is too high when a fluorine compound is injection molded, excessive pre-curing or scorch occurs before the fluorine compound is sufficiently molded in the form of a gasket so that gasket non-molding problem may occur and if the crosslinking rate is too low, the time required to remain inside the mold after the injection is increased so that a cycle time for gasket production may be increased and gasket productivity may be lowered. The crosslinking rate when the fluorine compound is actually injection molded may be indicated using an MDR technique.
(46) A scorch time t.sub.s1 of a fluorine compound for a gasket in MDR may be about 1.7 to 3.0 minutes. This is because, when the scorch time t.sub.s1 is less than about 1.7 minutes, an injection molding processability may be lowered due to excessive pre-curing and when the scorch time t.sub.s1 exceeds about 3.0 minutes, a cycle time for gasket production may be increased.
(47) In addition, about a 90% cure time t.sub.c(90) may be about 3.5 to 5.0 minutes. This is because, when the 90% cure time t.sub.c(90) is less than about 3.5 minutes, an injection molding processability may be lowered due to pre-curing and when the 90% cure time t.sub.c(90) exceeds about 5.0 minutes, a cycle time for gasket production may be increased.
(48) Results of MDR measurement according to the above-described comparative example and the embodiment of the present invention are as shown in the following Table 2. In the exemplary embodiment of the present invention, the crosslinking rate is controlled to be properly delayed to be suitable for injection molding compared to the comparative example so that t.sub.s1 and t.sub.c(90) may be 1.9 minutes and 4.1 minutes, respectively and the fluorine compound may be sufficiently well molded in the form of a gasket.
(49) TABLE-US-00002 TABLE 2 Comparative Item Unit example Embodiment t.sub.s1 min 1.5 1.9 t.sub.c(90) min 3.2 4.1
Injection Molding Processability and Degree of Deformation of Metallic Bipolar Plate
(50) In order to perform a sensory test of the degree of deformation of thin metallic bipolar plates when gaskets are injection molded on the thin metallic bipolar plates in a qualitative manner, integrated gasket manufactured by injection molding in the above experimental conditions are removed from the thin metallic bipolar plates, and shapes of the gaskets are compared with each other.
(51) In the comparative example, as illustrated in
(52) In the exemplary embodiment of the present invention, as illustrated in
(53) As a result of observing the degree of deformation of the thin metallic bipolar plates in another part,
(54) The parts of the gaskets observed illustrated in
(55) As shown in the comparative example of
(56) In order to compare the degree of deformation of the metallic bipolar plates with which the gaskets are integrated according to the existing comparative example and the exemplary embodiment of the present invention in a quantitative manner, five metallic bipolar plates were measured according to their positions, as described above.
(57)
(58) As illustrated in
(59) That is, an average value and standard deviation value of 16 parts of the metallic bipolar plate in the existing comparative example is 14959 m, whereas an average value and a standard deviation value of 16 parts of the metallic bipolar plate in the exemplary embodiment of the present invention is reduced to 2718 m so that the effect of reducing the degree of deformation of the metallic bipolar plate of about 82% based on the average value can be obtained.
(60) In this way, when the gasket is injection molded so as to be integrated with the metallic bipolar plate by using a fluorine compound according to the exemplary embodiment of the present invention, the degree of deformation of a thin metallic bipolar plate is greatly reduced so that productivity of the gasket can be greatly increased and simultaneously, when several hundreds of cells are assembled as a stack, the stability of connecting the stack can be remarkably improved.
(61) Elasticity and Repetitive Compression Behavior
(62) In a gasket for a PEMFC, a difference M between the highest torque M.sub.H and minimum torque M.sub.L of MDR is directly related to crosslinking density and thus it is advantageous for a gasket of PEMFC to have M of at least 10.5 dN.Math.m. As shown in the following Table 3, M of a fluorine gasket according to an existing comparative example and an exemplary embodiment of the present invention is 9.9 and 11.1 dN.Math.m, respectively, and M in the exemplary embodiment of the present invention is greater than M in the existing comparative example. This means that the fluorine gasket of the exemplary embodiment of the present invention has higher crosslinking density and thus lower compression set and enhanced elasticity compared with that of the comparative example.
(63) TABLE-US-00003 TABLE 3 Comparative Item Unit example Embodiment M.sub.L dN .Math. m 0.3 0.2 M.sub.H dN .Math. m 10.2 11.3 M(M.sub.H M.sub.L) dN .Math. m 9.9 11.1
(64) In order to compare elasticity of the fluorine gasket according to the existing comparative example and the exemplary embodiment of the present invention, each compression set is measured in the above-described evaluation condition and is shown in
(65) The following Table 4 shows compression sets and compression movement properties of the fluorine compound according to the comparative example and the exemplary embodiment of the present invention.
(66) TABLE-US-00004 TABLE 4 Comparative Item Evaluation condition.sup.1) Unit example Embodiment Compression set ASTM D395: 150 C./72 hours % 5 4 Method B 150 C./168 hours % 8 6 25% Deflection 150 C./336 hours % 12 9 Compressibility [Sample thickness when 1.sup.st % 76 76 compression is performed (@10 MPa)/ sample thickness when 1.sup.st compression is performed (@0.3 MPa)] 100 .sup.1)Measured by manufacturing the fluorine compound as a standard test sample after being cross-linked.
(67) As shown in
(68) Since the stack for hydrogen fuel cell vehicles is manufactured by stacking and assembling several hundreds of cells, as described above, it is important to understand compression behavior of the gasket when the fluorine gasket is used in the stack. In particular, in order to stably operate and maintain hydrogen fuel cell vehicles for a long time, cells of which performance is rapidly decreased as time elapses, or cells showing unexpectedly unusual behavior should be replaced or repaired. In this case, since the stack undergoes repetitive disassembly-reassembly, all cells in the stack are repeatedly compressed.
(69)
(70) In addition, in order to compare compressibility of samples, ratios at which a sample thickness under compression pressure about 10 MPa when 1st compression is performed is divided by a sample thickness under compression pressure about 0.3 MPa, are compared so that compressibility of each sample according to the comparative example and the embodiment of the present invention is about 76% and is the same.
(71) In general, compressibility from about 65% to 85% is preferable. When compressibility is less than 65%, an excessive compression problem of stack occurs so that durability may be lowered. When compressibility exceeds about 85%, compression is not easily performed so that proper stack assembly cannot be performed and proper contact resistance cannot be obtained.
(72) As a result, the gasket according to the exemplary embodiment of the present invention has proper compressibility. This means that, when the gasket is manufactured based on the fluorine compound according to the embodiment of the present invention, an injection molding processability and elasticity can be increased compared to the existing comparative example and when a stack is assembled, the same compression conditions as in the existing comparative example can be used so that compatibility is high.
(73) Electrochemical Cell Performance and Contact Resistance of Stack
(74) In order to compare the effect of fluorine gaskets according to an existing comparative example and an embodiment of the present invention on electrochemical cell performance and contact resistance of a hydrogen fuel cell, 5-cell stacks were manufactured in the above-described conditions and their performances were compared. The results of the electrochemical cell performances of the 5-cell stacks of the comparative example and an embodiment of the present invention are shown in
(75) As shown in
(76) As illustrated in
(77) When comparing the cell performances shown in
(78) As described above, the present invention provides the following effects:
(79) In a fluorine gasket for hydrogen fuel cells according to the present invention in which a high fluidity/high elasticity fluorine compound for hydrogen fuel cells is integrated with a bipolar plate by injection molding on the bipolar plate, Mooney viscosity is lower than an existing fluorine compound so that fluidity is enhanced, and a scorch time of the fluorine compound is increased to prevent pre-curing. Thus, an injection molding processability can be greatly improved and simultaneously, a low compression set causes a further increase in elasticity so that sealing durability of a stack can be increased.
(80) When a fluorine gasket according to the present invention is used in a fuel cell stack for hydrogen fuel cells, the same repetitive compression behavior, electrochemical cell performance and contact resistance characteristics as an existing fluorine gasket are shown with the above-described advantages so that a fuel cell stack can be stably used in the same stack assembly condition and the same operation condition without changing existing conditions.
(81) While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it will be understood by those of ordinary skill in the art that various changes in form and details may be made therein without departing from the spirit and scope of the present invention as defined by the following claims.