CN1195337C - Self-humidifying solid electrolyte composite membrane and manufacturing process thereof - Google Patents
Self-humidifying solid electrolyte composite membrane and manufacturing process thereof Download PDFInfo
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- CN1195337C CN1195337C CNB031405274A CN03140527A CN1195337C CN 1195337 C CN1195337 C CN 1195337C CN B031405274 A CNB031405274 A CN B031405274A CN 03140527 A CN03140527 A CN 03140527A CN 1195337 C CN1195337 C CN 1195337C
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- 239000012528 membrane Substances 0.000 title claims abstract description 92
- 239000002131 composite material Substances 0.000 title claims abstract description 63
- 239000007784 solid electrolyte Substances 0.000 title abstract description 13
- 238000004519 manufacturing process Methods 0.000 title abstract description 7
- 239000011347 resin Substances 0.000 claims abstract description 42
- 229920005989 resin Polymers 0.000 claims abstract description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000006277 sulfonation reaction Methods 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 16
- 238000002360 preparation method Methods 0.000 claims abstract description 14
- 239000000758 substrate Substances 0.000 claims abstract description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 44
- 229910052760 oxygen Inorganic materials 0.000 claims description 39
- 239000000243 solution Substances 0.000 claims description 37
- 150000001875 compounds Chemical class 0.000 claims description 21
- 229920000642 polymer Polymers 0.000 claims description 21
- 239000002904 solvent Substances 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 18
- 238000005516 engineering process Methods 0.000 claims description 17
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 16
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 16
- 239000003792 electrolyte Substances 0.000 claims description 16
- 239000007787 solid Substances 0.000 claims description 16
- 239000002245 particle Substances 0.000 claims description 14
- 150000003460 sulfonic acids Chemical class 0.000 claims description 12
- 238000010345 tape casting Methods 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 10
- 230000001186 cumulative effect Effects 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 9
- 239000011261 inert gas Substances 0.000 claims description 9
- 125000003118 aryl group Chemical group 0.000 claims description 7
- 229920002492 poly(sulfone) Polymers 0.000 claims description 7
- 239000004952 Polyamide Substances 0.000 claims description 4
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 4
- 239000004734 Polyphenylene sulfide Substances 0.000 claims description 4
- 239000008367 deionised water Substances 0.000 claims description 4
- 229910021645 metal ion Inorganic materials 0.000 claims description 4
- 229920002647 polyamide Polymers 0.000 claims description 4
- 229920000728 polyester Polymers 0.000 claims description 4
- 229920001470 polyketone Polymers 0.000 claims description 4
- 229920006380 polyphenylene oxide Polymers 0.000 claims description 4
- 229920000069 polyphenylene sulfide Polymers 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- 239000008240 homogeneous mixture Substances 0.000 claims description 3
- 239000012535 impurity Substances 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 229910021641 deionized water Inorganic materials 0.000 claims description 2
- 238000010790 dilution Methods 0.000 claims description 2
- 239000012895 dilution Substances 0.000 claims description 2
- 239000000446 fuel Substances 0.000 abstract description 24
- 230000005540 biological transmission Effects 0.000 abstract description 4
- 230000005611 electricity Effects 0.000 abstract description 4
- 238000010248 power generation Methods 0.000 abstract description 4
- 238000012546 transfer Methods 0.000 abstract description 4
- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 2
- 239000013078 crystal Substances 0.000 abstract 2
- 150000004677 hydrates Chemical class 0.000 abstract 2
- 238000005266 casting Methods 0.000 abstract 1
- 230000002349 favourable effect Effects 0.000 abstract 1
- 239000010970 precious metal Substances 0.000 abstract 1
- 239000000463 material Substances 0.000 description 14
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 13
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 12
- 239000006185 dispersion Substances 0.000 description 12
- 239000012153 distilled water Substances 0.000 description 10
- 239000007789 gas Substances 0.000 description 10
- 238000009835 boiling Methods 0.000 description 9
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 8
- 239000000956 alloy Substances 0.000 description 8
- 229910045601 alloy Inorganic materials 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 235000019441 ethanol Nutrition 0.000 description 8
- 238000002156 mixing Methods 0.000 description 8
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 7
- 229920000491 Polyphenylsulfone Polymers 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 238000004140 cleaning Methods 0.000 description 6
- 229920006389 polyphenyl polymer Polymers 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000012544 monitoring process Methods 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229920000557 Nafion® Polymers 0.000 description 4
- 150000001298 alcohols Chemical class 0.000 description 4
- 229910052786 argon Inorganic materials 0.000 description 4
- 238000009792 diffusion process Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 239000004020 conductor Substances 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000002105 nanoparticle Substances 0.000 description 3
- 229910000510 noble metal Inorganic materials 0.000 description 3
- 229910052697 platinum Inorganic materials 0.000 description 3
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- 229910010413 TiO 2 Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 238000007600 charging Methods 0.000 description 2
- 239000000805 composite resin Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 230000008595 infiltration Effects 0.000 description 2
- 238000001764 infiltration Methods 0.000 description 2
- 150000002484 inorganic compounds Chemical class 0.000 description 2
- 229910010272 inorganic material Inorganic materials 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000000615 nonconductor Substances 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 2
- 239000011973 solid acid Substances 0.000 description 2
- HBGPNLPABVUVKZ-POTXQNELSA-N (1r,3as,4s,5ar,5br,7r,7ar,11ar,11br,13as,13br)-4,7-dihydroxy-3a,5a,5b,8,8,11a-hexamethyl-1-prop-1-en-2-yl-2,3,4,5,6,7,7a,10,11,11b,12,13,13a,13b-tetradecahydro-1h-cyclopenta[a]chrysen-9-one Chemical compound C([C@@]12C)CC(=O)C(C)(C)[C@@H]1[C@H](O)C[C@]([C@]1(C)C[C@@H]3O)(C)[C@@H]2CC[C@H]1[C@@H]1[C@]3(C)CC[C@H]1C(=C)C HBGPNLPABVUVKZ-POTXQNELSA-N 0.000 description 1
- PFRGGOIBYLYVKM-UHFFFAOYSA-N 15alpha-hydroxylup-20(29)-en-3-one Natural products CC(=C)C1CCC2(C)CC(O)C3(C)C(CCC4C5(C)CCC(=O)C(C)(C)C5CCC34C)C12 PFRGGOIBYLYVKM-UHFFFAOYSA-N 0.000 description 1
- 229920003934 Aciplex® Polymers 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229920003935 Flemion® Polymers 0.000 description 1
- SOKRNBGSNZXYIO-UHFFFAOYSA-N Resinone Natural products CC(=C)C1CCC2(C)C(O)CC3(C)C(CCC4C5(C)CCC(=O)C(C)(C)C5CCC34C)C12 SOKRNBGSNZXYIO-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 230000020411 cell activation Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000002772 conduction electron Substances 0.000 description 1
- 239000008358 core component Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000002019 doping agent Substances 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 239000011532 electronic conductor Substances 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000010416 ion conductor Substances 0.000 description 1
- 150000002500 ions Chemical group 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000010355 oscillation Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000013112 stability test Methods 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- 125000001273 sulfonato group Chemical group [O-]S(*)(=O)=O 0.000 description 1
- 125000000472 sulfonyl group Chemical group *S(*)(=O)=O 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
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
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- Fuel Cell (AREA)
Abstract
The present invention relates to a self-humidifying solid electrolyte composite membrane and a manufacturing process thereof, particularly to a solid electrolyte composite membrane of a fuel battery and a preparation process thereof. Sulfonation resin is used as substrates mixed with crystal hydrates, and then, the crystal hydrates are dissolved at high temperature and high pressure, and the solid electrolyte composite membrane is formed by a flow casting method. The composite membrane does not contain precious metals, can carry out the transfer of protons and water, and can not carry out the transfer of electrons and gas, and the manufacturing cost is low; a proton exchanging membrane fuel battery can generate electricity in a self-humidification mode without the need for a humidifier, so the specific power of the power generation system is increased; the proton transmission capability of the composite membrane is strong, electric conductivity can exceed 0.08S. cm-1, and the power density of the fuel battery assembled by using the composite membrane can exceed 2.0 W/cm 2; the discharge performance of the battery is stable, and the service life of the battery can reach more that 10000 hours; the composite membrane is prepared by the original preparation process, so the area of the formed composite membrane can exceed 1m2; the composite membrane is suitable for large-scale production, and is favorable to pushing the industrialization of proton exchanging membrane fuel batteries.
Description
Technical field
The present invention relates to a proton exchanging film fuel battery from humidification electrolyte compound film for solid and preparation technology thereof, belong to the fuel cell material science and technology field.
Background technology
Proton Exchange Membrane Fuel Cells, be after alkaline fuel cell, phosphoric acid fuel cell, melting carbonate fuel battery and Solid Oxide Fuel Cell the 5th generation fuel cell.Proton Exchange Membrane Fuel Cells (PEMFC) has high power density, high-energy conversion efficiency, and cold-starting, advantages of environment protection promises to be the power source of zero disposal of pollutants electric automobile most.Research has become a focus in present electrochemistry and the energy science field to PEMFC, and many developed countries are all investing heavily in this technology.
Proton exchange membrane is the core component of PEMFC, it with general chemical power source in the barrier film that uses be very different, be a kind of ion conductor.Proton exchange membrane uses phenolic resins sulfonic acid type film, polystyrolsulfon acid type film, polytrifluorostyrene sulfonic acid type film and perfluorinated sulfonic acid type film etc. several usually, and perfluorinated sulfonic acid type film is the electrolyte that is suitable for Proton Exchange Membrane Fuel Cells at present most.Perfluorinated sulfonic acid type film comprises following several types: the Nafion series membranes that (1) U.S. DuPont company produces comprises Nafion117, Nafion115, Nafion112, Nafion111 etc.; (2) the XUS-B204 film of U.S. Dow chemical company development; (3) Aciplex series membranes and the Flemion film produced of Japanese Asahi company; (4) the C film of Japanese chlorine engineering (ChlorineEngineers) company; (5) BAM type film of Canadian Ba Lade company etc.
The conductivity of proton exchange membrane depends on its water content consumingly.When film was in dry state, conductivity was almost nil; When the film complete wetting, has good proton electrical conductance.The service behaviour that is to say Proton Exchange Membrane Fuel Cells relies on the water content in the film to a great extent.Therefore in order to guarantee the normal power generation of Proton Exchange Membrane Fuel Cells, just must make proton exchange membrane be in moisture state, fuel cell is carried out water management.Usual way is reacting gas to be carried out humidification prevent that film is dry, especially makes the anode-side and the not dehydration of entrance point of proton exchange membrane, increases the water content of proton exchange membrane.Reacting gas humidifying equipment commonly used has bubbling humidifier, membrane humidifier, dew point humidifier, direct work of water sprinkling for better material moisture device etc.Yet these humidifying equipments make the whole generating system become complicated, have increased system cost, and have been unfavorable for portable use.The self-humidification that removes the humidification subsystem then helps promoting the industrialization of Proton Exchange Membrane Fuel Cells.Also claim passive humidification from humidification, promptly need not extraneous water source and thermal source and come the humidification reacting gas that Proton Exchange Membrane Fuel Cells also can keep moistening preferably degree, keep the good proton conductivity of film.Therefore many scholars have done from aspects such as fuel cell structure, electrode, films manyly to explore from humidification.Japan scholar Watanabe is in the phase earlier 1990s self-humidification [US Patent number:5766787,1998] that begins one's study, with noble metal granules such as platinum, SiO
2, TiO
2Making composite membrane etc. in the nano level particle adding perfluor sulfoacid resin solution, realized from humidification, mainly is the O that relies on from the infiltration of yin, yang the two poles of the earth
2And H
2Pt catalyst surface chemical catalysis water generation reaction in proton exchange membrane, with the two common humidifying proton exchange film of water that the electrochemical cathode reaction generates, the oxide particle in the film plays the effect that keeps moisture.Another key property of this method is to stop reacting gas to be penetrated into electrode, has reduced the polarization of electrode overpotential, can improve the performance of battery.But this Pt, Pt/SiO
2, Pt/TiO
2The complicated process of preparation of perfluorinated sulfonic acid composite membrane, the cost height; And the Pt distribution of particles is inhomogeneous in the composite membrane, also can generate focus, and composite membrane is degenerated; In addition, the Pt particle also might make the solid electrolyte conducting, and self-discharge phenomenon takes place.Scholars such as Korea S Tae-Hyun Yang, Chang-Soo Kin adopt the method for the three-in-one combination of sputter Pt particulate between the two-layer dielectric film to realize from humidification composite membrane [Tae-Hyun Yang recently, Young-Gi Yoon, Chang-Soo Kim, et al..Journal of power Source, 2002,106:328-332.], principle is to make the hydrogen or oxygen gas of cross-diffusion in the film on the Pt catalyst combination reaction take place, and generates the water-wet solid electrolyte.But this method cost height, and increased the internal resistance of cell.Above as can be seen self-humidification all is conceived to use Pt to come catalysis cross-diffusion gas to generate water, and does not adopt the composite membrane technology of the conductivity of reinforcing membrane under low moistening degree.United States Patent (USP) [Patent number 6468684,1999] adopted the method that in solid acid, adds construction adhesive to make novel solid electrolyte, this solid electrolyte adds mechanical performance or chemical stability that construction adhesive strengthens solid electrolyte based on solid acid.The construction adhesive of admixture is non-conductor or conductor material, and the non-conductor material is polymer and glass; And conductor material is an electronic conductor, like this, with the electron conductor material be the solid electrolyte that makes of matrix can conduction electron again can proton conducting.Yet this solid electrolyte can not infiltration water, electrical property is lower, and there is weak point in its preparation technology, as the direct hot binding of many employings, this can increase unsteadiness and inhomogeneities that alloy combines with polymeric substrates, and the thickness of composite membrane is difficult to reach ultra-thin level.
Summary of the invention
The objective of the invention is provides a kind of novel from humidification electrolyte compound film for solid and preparation technology thereof for Proton Exchange Membrane Fuel Cells, this electrolyte compound film for solid cost of manufacture is low, do not contain noble metal, when cell power generation, can not produce focus, do not have self-discharge phenomenon yet, and can strengthen its conductivity under low moistening degree effectively.
The present invention is achieved through the following technical solutions: a kind of from the humidification electrolyte compound film for solid, it is characterized in that: it is substrate doping crystalline hydrate that described composite membrane adopts sulfate resin, and is prepared from as follows:
(1) the crystalline hydrate liquid stream that mixes is broken into the nano particle that is of a size of between 5～100nm;
(2) making in sulfate resin and the absolute alcohol kind solvent one or more is that 0.5～8MPa, temperature are to dissolve in 200～650 ℃ the autoclave in pressure under inert gas shielding, makes A solution;
(3) with one or more of crystalline hydrate and absolute alcohol kind solvent being that 0.5～8MPa, temperature are to dissolve in 110～300 ℃ the autoclave in pressure under the inert gas shielding, make B solution;
(4) getting described B solution and A solution, is 0.5～30% batching by crystalline hydrate and sulfate resin mass percent, and is that 0.5～8MPa, temperature are 200～650 ℃ and mix down evenly at pressure, makes even mixed solution;
(5) solution that mixes in the step (4) is cooled to 150～580 ℃ under normal pressure, adopts the The tape casting film forming;
(6) at room temperature after the drying, place under 80～550 ℃ of temperature and inert environments under heat-treat.
Sulfate resin described in the present invention adopts as shown in the formula the perfluorinated sulfonic acid polymer of (I) or contains the sulfonated polymer or the PBI[poly-(2,2-m-(phenylene)-5,5-bisbenzimidazole) of aromatic ring structure shown in the formula (II)] in the resin one or more.
Crystalline hydrate of the present invention adopts M.nH
2O, wherein M is an inorganic compound.For example crystalline hydrate is H
3PW
12O
40NH
2O, H
3PMo
12O
40NH
2O, H
4SiW
12O
40NH
2O, H
1+xZr
2Si
xP
3-xO
12NH
2O, H
1+xY
xZr
2-x(PO
4)
3NH
2O, H
xZr
1+xNb
1-x(PO
4) 3nH
2O, H
1.28Zn
0.36SO
4NH
2O, H
1.6Mg
0.2SO
4NH
2O, H
1.72Mg
0.14SO
4NH
2O, ZrHPO
4NH
2O or CaHPO
4.nH
2Among the O any.
The present invention also provides a kind of preparation technology from the humidification electrolyte compound film for solid, and this technology prepares as follows:
(1) uses the nanometer crush method under 100Mpa～600MPa dynamic load amount, the crystalline hydrate liquid stream that mixes is broken into the nano particle that is of a size of 5～100nm;
(2) one or more in sulfate resin and the absolute alcohol kind solvent are that 0.5～8MPa, temperature are to dissolve in 200～650 ℃ the autoclave in pressure under inert gas shielding, make A solution;
(3) with one or more of crystalline hydrate and absolute alcohol kind solvent being that 0.5～8MPa, temperature are to dissolve in 110～300 ℃ the autoclave in pressure under the inert gas shielding, make B solution;
(4) get described B solution and A solution, by crystalline hydrate and sulfate resin mass percent is 0.5～30% batching, and be that 0.5～8MPa, temperature are 200～650 ℃ and mix down at pressure, and under ultrasonic wave cumulative peptizaiton, evenly mix, make homogeneous mixture solotion;
(5) solution that mixes in the step (4) is cooled to 150～580 ℃ under normal pressure, adopts the The tape casting film forming;
(6) under the room temperature after the drying, place under 80～550 ℃ of temperature and inert environments under heat-treat;
(7) proton exchange membrane places the H of 1.0～10.0vol%
2O
2Boiled in the aqueous solution 30～120 minutes, and removed organic impurities, take out the back washed with de-ionized water, place the dilution heat of sulfuric acid of 0.1～1.0M to boil again 30～240 minutes, to remove inorganic metal ion, take out the back and clean up with deionized water, can make from the humidification electrolyte compound film for solid.
Provided by the present inventionly have the following advantages and the high-lighting effect from the humidification electrolyte compound film for solid: this composite membrane does not contain noble metal, can carry out the transmission of proton and water, can not carry out the transmission of electronics and gas, and is cheap for manufacturing cost; Can make Proton Exchange Membrane Fuel Cells need not humidifier and just can generate electricity, improve the specific power of electricity generation system from humidification; Can operate by high temperature (above 100 ℃), strengthened ability and electrochemical reaction dynamics that CO is poisoned; Also can normal power generation at low temperature (below 0 ℃).And the proton conductivity of this composite membrane is very strong, and conductivity can surpass 0.08S.cm
-1, its fuel battery assembled power density can surpass 2.0W/cm
2Cell discharge performance is stable, and the life-span can reach up to ten thousand hours; And the present invention adopts the preparation technology of original creation: high temperature, high pressure dissolving are also adopted the The tape casting film forming, make the film forming area can surpass 1m
2, be suitable for large-scale production, help promoting the industrialization of Proton Exchange Membrane Fuel Cells.
Description of drawings
Fig. 1 is the outline drawing from the humidification electrolyte compound film for solid provided by the invention.
Fig. 2 is for adopting the I-V characteristic curve of cell figure from the humidification electrolyte compound film for solid provided by the invention.
Fig. 3 is provided by the invention from humidification electrolyte compound film for solid stability test energy curve for adopting.
Embodiment
Provided by the invention is a kind of solid electrolyte that is used for PEMFC from the humidification electrolyte compound film for solid, and the conductivity of composite membrane depends on the conductivity of basis material polymer and dopant material and the interaction between them; In order to strengthen solid electrolyte moisture holding capacity and the conductivity under low humidity, the present invention adopts the method for doping crystalline hydrate in having the sulfate resin matrix of proton conduction function, makes composite membrane, and it has conductivity preferably.The sulfate resin that adopts among the present invention is meant through sulfonated polymers, comprise the above-mentioned perfluorinated sulfonic acid polymer of structural formula (I), the sulfonated polymer that contains aromatic ring structure shown in the structural formula (II), the sulfonation PBI[poly-(2 of containing, 2-m-(phenylene)-5, the 5-bisbenzimidazole)] polymer.Here the sulfonation of indication is meant to introduce and has the group that contains the S element that the group that contains the S element refers to sulfonate group (SO on some C atom of polymer molecular structure
3H) and the metal ion group as (SO
3M, M representation metal ion), sulfonyl group (SO
2X, X represents nonmetalloid).
In the perfluorinated sulfonic acid polymer in the formula (I), x, y, m, n is the different degree of polymerization, as Nafion, the Dow film.The X of aromatic ring structure polymer representative: X ≠ aliphat C-H group (Aliphatic C-H groups) in the formula (II); X=-S-: polyphenylene sulfides (Polyphenylene sulfide); X=-O-: polyphenylene oxide (Polyphenyleneoxide); X=-SO
2-: polysulfones (Polysulfone); X=-NHCO-: polyamide (Polyamides); X=-COO-: polyester (Polyesters); X=-CO-: polyketone (Polyketones).
The general formula of the crystalline hydrate that mixes is: M.nH
2O, wherein M is an inorganic compound.Crystalline hydrate the typical case be represented as: H
3PW
12O
40NH
2O, H
3PMo
12O
40NH
2O, H
4SiW
12O
40NH
2O, H
1+xZr
2Si
xP
3-xO
12NH
2O, H
1+xY
xZr
2-x(PO
4)
3NH
2O, H
xZr
1+xNb
1-x(PO
4)
3NH
2O, H
1.28Zn
0.36SO
4NH
2O, H
1.6Mg
0.2SO
4NH
2O, H
1.72Mg
0.14SO
4NH
2O, ZrHPO
4NH
2O, CaHPO
4NH
2O.
Above crystalline hydrate has strong water-wet behavior and proton conductivity.The crystalline hydrate molecule can not only attract bond electron pair consumingly, and also has lone electron pair, and negative electrical charge is very concentrated, makes this compounds have the proton transfer ability.Hydrone is a polar molecule, when water molecules is around these crystalline hydrate molecules, the dipole of hydrone will and proton between produces and attracts each other, so aquation takes place, the formation hydrogen bond is very beneficial for the transmission of proton like this.Therefore, the crystalline hydrate with water of coordination molecule of some can strengthen the water content of proton exchange membrane under low humidity, improves the proton transfer ability.
The manufacture method of composite membrane has influenced its performance largely, and the present invention has specifically adopted following method preparation: crystalline hydrate can prepare by chemical reaction methods such as sol-gels, also can buy by market, and is cheap.Before mixing, need alloy is pulverized and purified treatment, can adopt the nanometer crush method under 100MPa～600MPa dynamic load amount, doping crystalline hydrate liquid stream to be broken into the particle that is of a size of 5～100nm.Being used the absolute alcohol kind solvent makes at inert gas (as N
2, Ar
2) protection or vacuum under dissolve, temperature should not be too high, in order to avoid polymer unwinds is damaged, generally between 200～650 ℃.Be that 0.5～8MPa, temperature are to dissolve in 110～300 ℃ the autoclave with one or more of crystalline hydrate and absolute alcohol kind solvent in pressure again; Both doping ratios are key parameters, and crystalline hydrate can not mix too much, otherwise the mechanical strength variation of composite membrane breaks easily, and the mass ratio of general crystalline hydrate and sulfate resin is between 0.5～30%; The crystalline hydrate composition granule is littler, distributes also just better, and it is more effectively to disperse means that the ultrasonic wave cumulative disperses.Because nano particle Showed Very Brisk; interaction between its individuality is also very strong; Shi Changhui makes several aggregation of particles together; and formed bigger (cluster) particle; this phenomenon can greatly be cut down the effect that crystalline hydrate should be brought into play in polymer; therefore the composite membrane dispersion technology is very important; adopt ultrasonic cumulative dispersion technology can make that alloy is uniformly dispersed among the preparation technology of the present invention; after waiting to be uniformly dispersed; be cooled to 150～580 ℃; adopt the The tape casting moulding again, controllable film thickness is in 10～300 mu m ranges, and is dry sliced then.Also need use hydrogen peroxide, sulfuric acid treatment at last, remove the proton conductivity of impurity and reinforced composite membrane.
Embodiment 1
With sulfonation PBI[poly-(2,2-m-(phenylene)-5,5-bisbenzimidazole)] resin and H
3PW
12O
40NH
2It is as follows in detail that the O crystalline hydrate prepares the embodiment of composite membrane:
Use the broken dispersion machine of compound high shear with crystalline hydrate H
3PW
12O
40NH
2It is standby that O powder liquid stream under 600MPa is broken into the particle of 100 nano-scales.Adopt the base material of sulfonation PBI dried resin as composite membrane; use the solvent of alcohols mixture (5vol% methyl alcohol, 50vol% ethanol, 45vol% propyl alcohol) as sulfonation PBI dried resin; under argon shield, in autoclave, be pressurized to 8MPa, and be heated to 530 ℃ and dissolve and obtain sulfonation PBI solution for standby.With H
3PW
12O
40NH
2O crystalline hydrate and absolute ethyl alcohol are inserted and are pressurized to 8MPa in the autoclave, and are heated to 110 ℃ and dissolve, and obtain alloy solution.By sulfonation PBI dried resin: H
3PW
12O
40NH
2O=100: 30 (mass ratioes) batchings, obtain composite membrane solution, in autoclave, be pressurized to 8MPa, and be heated to 530 ℃ and dissolve, and under the effect of the ultrasonic cumulative dispersion machine of 600W, till mixing.Then the composite membrane mixture is cooled under 480 ℃, the The tape casting film forming, film thickness monitoring is at 50 microns.Under 430 ℃, composite membrane is carried out drying at last, be cut into a certain size composite membrane after to be dried the finishing, the hydrogen peroxide solution through 1vol% boils processing 2 hours respectively, uses the distilled water boiling washing afterwards, boil with the dilute sulfuric acid of 0.1M again and handled 4 hours, promptly make H after boiling cleaning with distilled water
3PW
12O
40NH
2O composite membrane/sulfonation PBI composite membrane.
Embodiment 2
With sulfonation PPSU (PS) resin and ZrHPO
4NH
2It is as follows in detail that the O crystalline hydrate prepares the embodiment of composite membrane:
Use the broken dispersion machine of compound high shear with crystalline hydrate ZrHPO
4NH
2It is standby that O powder liquid stream under 400MPa is broken into the particle of 50 nano-scales.Adopt the base material of sulfonation PPSU dried resin as composite membrane; use the solvent of absolute ethyl alcohol as sulfonation PPSU dried resin; under nitrogen protection, in autoclave, be pressurized to 0.5MPa, and be heated to 650 ℃ and dissolve and obtain sulfonation PPSU solution for standby.With ZrHPO
4NH
2O crystalline hydrate and anhydrous amylalcohol are inserted and are pressurized to 1MPa in the autoclave, and are heated to 300 ℃ and dissolve, and obtain alloy solution.By sulfonation PPSU dried resin: ZrHPO
4NH
2O=100: 1 (mass ratio) batching, obtain composite membrane solution, in autoclave, be pressurized to 1MPa, and be heated to 650 ℃ and dissolve, and under the effect of the ultrasonic cumulative dispersion machine of 500W, till mixing.Then the composite membrane mixture is cooled under 580 ℃, the The tape casting film forming, film thickness monitoring is at 50 microns.Under 550 ℃, composite membrane is carried out drying at last, be cut into a certain size composite membrane after to be dried the finishing, the hydrogen peroxide solution of process 10vol% boils and handles half an hour respectively, use the distilled water boiling washing afterwards, boil with the dilute sulfuric acid of 1M again and handle half an hour, promptly make ZrHPO after boiling cleaning with distilled water
4NH
2O/ sulfonation PPSU composite membrane.
Embodiment 3
With sulfonated polyphenyl oxygen base resin (PPO) resin and H
1.28Zn
0.36SO
4NH
2It is as follows in detail that the O crystalline hydrate prepares the embodiment of composite membrane:
Use the broken dispersion machine of compound high shear with crystalline hydrate H
1.28Zn
0.36SO
4NH
2It is standby that O powder liquid stream under 300MPa is broken into the particle of 10 nano-scales.Adopt the base material of sulfonated polyphenyl oxygen base resin as composite membrane; use the solvent of alcohols mixture (45vol% methyl alcohol, 35vol% amylalcohol, 20vol% octanol) as sulfonated polyphenyl oxygen base resin; under argon shield, in autoclave, be pressurized to 4MPa, and be heated to 200 ℃ and dissolve that to obtain sulfonated polyphenyl oxygen base resin solution standby.With H
1.28Zn
0.36SO
4NH
2O crystalline hydrate and absolute ethyl alcohol are inserted and are pressurized to 0.5MPa in the autoclave, and are heated to 200 ℃ and dissolve, and obtain alloy solution.Press sulfonated polyphenyl oxygen base portions of resin H
1.28Zn
0.36SO
4NH
2O=100: 0.5 (mass ratio) batching, obtain composite membrane solution, in autoclave, be pressurized to 0.5MPa, and be heated to 200 ℃ and dissolve, and under the effect of the ultrasonic cumulative dispersion machine of 500W, till mixing.Then the composite membrane mixture is cooled under 150 ℃, the The tape casting film forming, film thickness monitoring is at 50 microns.Under 80 ℃, composite membrane is carried out drying at last, be cut into a certain size composite membrane after to be dried the finishing, the hydrogen peroxide solution through 4vol% boils processing 3 hours respectively, uses the distilled water boiling washing afterwards, boil with the dilute sulfuric acid of 1M again and handled 2 hours, promptly make H after boiling cleaning with distilled water
1.28Zn
0.36SO
4NH
2O composite membrane/sulfonated polyphenyl oxygen base resin.
Embodiment 4
With sulfonated polysulfone resin (PSF) and H
3PMo
12O
40NH
2It is as follows in detail that the O crystalline hydrate prepares the embodiment of composite membrane:
Use the broken dispersion machine of compound high shear with crystalline hydrate H
3PMo
12O
40NH
2It is standby that O powder liquid stream under 450MPa is broken into the particle of 15 nano-scales.Adopt the base material of SPSF dried resin, use the solvent of absolute ethyl alcohol, under nitrogen protection, in autoclave, be pressurized to 1.5MPa, and be heated to 550 ℃ and dissolve and obtain the SPSF solution for standby as the polysulfones dried resin as composite membrane.With H
3PMo
12O
40NH
2O crystalline hydrate and anhydrous amylalcohol are inserted and are pressurized to 1MPa in the autoclave, and are heated to 250 ℃ and dissolve, and obtain alloy solution.By SPSF dried resin: H
3PMo
12O
40NH
2O=100: 1 (mass ratio) batching, obtain composite membrane solution, in autoclave, be pressurized to 1MPa, and be heated to 450 ℃ and dissolve, and under the effect of the ultrasonic cumulative dispersion machine of 500W, till mixing.Then the composite membrane mixture is cooled under 520 ℃, the The tape casting film forming, film thickness monitoring is at 50 microns.Under 160 ℃, composite membrane is carried out drying at last, be cut into a certain size composite membrane after to be dried the finishing, the hydrogen peroxide solution of process 10vol% boils and handles half an hour respectively, use the distilled water boiling washing afterwards, boil with the dilute sulfuric acid of 1M again and handle half an hour, promptly make H after boiling cleaning with distilled water
3PMo
12O
40NH
2O/ sulfonated polysulfone resin composite membrane.
Embodiment 5
With Nafion perfluorinated sulfonic resin and crystalline hydrate CaHPO
4NH
2It is as follows in detail that O prepares the embodiment of composite membrane:
Use the broken dispersion machine of compound high shear with crystalline hydrate CaHPO
4NH
2It is standby that O powder liquid stream under 100MPa is broken into the particle of 5 nano-scales.Adopt the base material of perfluorinated sulfonic acid dried resin as composite membrane; use the solvent of alcohols mixture (10vol% methyl alcohol, 30vol% ethanol, 60vol% isopropyl alcohol) as the perfluorinated sulfonic acid dried resin; under argon shield, in autoclave, be pressurized to 3.5MPa, and be heated to 280 ℃ and dissolve and obtain the sulfonate resin solution for standby.With crystalline hydrate CaHPO
4NH
2O and alcohols mixture (10vol% methyl alcohol, 90vol% ethanol) are inserted and are pressurized to 2.5MPa in the autoclave, and are heated to 150 ℃ and dissolve, and obtain alloy solution.Press perfluorinated sulfonic acid dried resin: CaHPO
4NH
2O=100: 3 (mass ratioes) batchings, obtain composite membrane solution, in autoclave, be pressurized to 3.5MPa, and be heated to 280 ℃ and dissolve, and under the effect of the ultrasonic cumulative dispersion machine of 400W, till mixing.Then the composite membrane mixture is cooled under 170 ℃, adopts the The tape casting film forming, film thickness monitoring is at 50 microns.Under 135 ℃, composite membrane is carried out drying at last, be cut into a certain size composite membrane after to be dried the finishing, the hydrogen peroxide solution through 3wt% boils processing 1 hour respectively, uses the distilled water boiling washing afterwards, boil with the dilute sulfuric acid of 0.3M again and handled 1 hour, boil with distilled water that to clean the back standby.Fig. 1 is for making CaHPO
4NH
2O/ perfluorinated sulfonic resin composite membrane pattern, surface distributed is more even.The look (PFSA is a water white transparency) that is translucent, stretch modulus is 290MPa, the mechanical performance all Nafion112 film with Dupont company is suitable.
Above composite membrane is made into membrane electrode, is assembled into PEMFC and carries out from the moisturization evaluation.At first will at room temperature dry after the oven dry as the carbon paper of gas diffusion layers substrate (Japanese Toray company) through ultrasonic waves for cleaning 30 minutes, high-temperature process is 30 minutes under 340 ℃ high temperature.With a certain proportion of water and ethanol is solvent, and activated carbon (Vulcan XC-72,150 orders) is mixed with polytetrafluoroethylene PTFE (U.S. Dupont company) emulsion, uses supersonic oscillations.After mixing, with the mixture carbon paper surface of smooth above-mentioned processing equably, sintering forms gas diffusion layers under 340 ℃ high temperature, as the substrate of pole catalyze layer.Then with a certain amount of Pt/C (20%; Johnson-Matthey company), Nafion (10%; U.S. Dupont company) and redistilled water add in the beaker; place in the ultrasonic waves for cleaning pond; after fully mixing, form Catalytic Layer ink shape material, evenly be sprayed in the pole catalyze layer substrate; 90 ℃ of following vacuumizes, heat treatment 30 minutes under 120 ℃ and argon shield afterwards.Last Catalytic Layer surface makes hydrophilic thin layer hydrogen electrode through special disposal, and the Pt carrying capacity is 0.4mg/cm
2
It is 5cm that MEA is assembled into active area
2Monocell.Fuel gas adopts dry hydrogen gas respectively, and directly by 1.5 times of stoichiometry chargings, oxidizing gas adopts dried oxygen without humidification, directly presses 2 times of stoichiometry chargings without humidification; The battery internal gas pressure is controlled at 0.3MPa, and battery operated temperature is at 70 ℃.When cell activation after 5 hours, under steady state operation, battery is estimated from moisturization.The voltage-current characteristic of battery as shown in Figure 2, discharge stability is as shown in Figure 3 under the constant voltage.
Very excellent with the battery performance that the composite membrane of manufacturing of the present invention is assembled into, under the humidification mode, generating electricity, maximum power density has surpassed 2.0W/cm
2Battery performance is stable, worked 200 hours during in, performance is undamped, and is slightly on the rise.
Claims (3)
1. one kind from the humidification electrolyte compound film for solid, it is characterized in that: described composite membrane is that to adopt with the sulfate resin be that substrate doping crystalline hydrate is prepared from, and its preparation process is as follows:
(1) the crystalline hydrate liquid stream that mixes being broken into particle size is between 5～100nm; Described crystalline hydrate is H
3PW
12O
40NH
2O, H
3PMo
12O
40NH
2O, H
4SiW
12O
40NH
2O, H
1+xZr
2Si
xP
3-xO
12NH
2O, H
1+xY
xZr
2-x(PO
4)
3NH
2O, H
xZr
1+xNb
1-x(PO
4)
3NH
2O, H
1.28Zn
0.36SO
4NH
2O, H
1.6Mg
0.2SO
4NH
2O, H
1.72Mg
0.14SO
4NH
2O, ZrHPO
4NH
2O or CaHPO
4NH
2Among the O any;
(2) making sulfate resin and absolute alcohol kind solvent is that 0.5～8MPa, temperature are to dissolve in 200～650 ℃ the autoclave in pressure under inert gas shielding, makes A solution; Described sulfate resin adopts as shown in the formula the perfluorinated sulfonic acid polymer of I or sulfonated polymer that contains aromatic ring structure or the sulfonation PBI polymer of formula II;
The X of aromatic ring structure polymer representative among the formula II: X ≠ aliphat C-H group; X=-S-: polyphenylene sulfides; X=-O-: polyphenylene oxide; X=-SO
2-: polysulfones; X=-NHCO-: polyamide; X=-COO-: polyester; X=-CO-: polyketone;
(3) with described crystalline hydrate and absolute alcohol kind solvent being that 0.5～8MPa, temperature are to dissolve in 110～300 ℃ the autoclave in pressure under the inert gas shielding, make B solution;
(4) getting described B solution and A solution, is 0.5～30% batching by crystalline hydrate and sulfate resin mass percent, and is that 0.5～8MPa, temperature are 200～650 ℃ and mix down evenly at pressure; Make homogeneous mixture solotion;
(5) solution that mixes in the step (4) is cooled to 150～580 ℃ under normal pressure, adopts the The tape casting film forming;
(6) at room temperature after the drying, place under 80～550 ℃ of temperature and inert environments under heat-treat.
2. one kind according to claim 1 from the preparation technology of humidification electrolyte compound film for solid, and this technology prepares as follows:
(1) adopting the nanometer crush method under 100MPa～600MPa dynamic load amount the crystalline hydrate liquid stream that mixes to be broken into particle size is 0.005～0.1 μ m; Described crystalline hydrate is H
3PW
12O
40NH
2O, H
3PMo
12O
40NH
2O, H
4SiW
12O
40NH
2O, H
1+xZr
2Si
xP
3-xO
12NH
2O, H
1+xY
xZr
2-x(PO
4)
3NH
2O, H
xZr
1+xNb
1-x(PO
4)
3NH
2O, H
1.28Zn
0.36SO
4NH
2O, H
1.6Mg
0.2SO
4NH
2O, H
1.72Mg
0.14SO
4NH
2O, ZrHPO
4NH
2O or CaHPO
4NH
2Among the O any;
(2) making sulfate resin and absolute alcohol kind solvent is that 0.5～8MPa, temperature are to dissolve in 200～650 ℃ the autoclave in pressure under inert gas shielding, makes A solution; Described sulfate resin adopts as shown in the formula the perfluorinated sulfonic acid polymer of I or sulfonated polymer that contains aromatic ring structure or the sulfonation PBI polymer of formula II;
The X of aromatic ring structure polymer representative among the formula II: X ≠ aliphat C-H group; X=-S-: polyphenylene sulfides; X=-O-: polyphenylene oxide; X=-SO
2-: polysulfones; X=-NHCO-: polyamide; X=-COO-: polyester; X=-CO-: polyketone;
(3) with crystalline hydrate and absolute alcohol kind solvent being that 0.5～8MPa, temperature are to dissolve in 110～300 ℃ the autoclave in pressure under the inert gas shielding, make B solution;
(4) get described B solution and A solution, by crystalline hydrate and sulfate resin mass percent is 0.5～30% batching, and be that 0.5～8MPa, temperature are 200～650 ℃ and mix down at pressure, and under ultrasonic wave cumulative peptizaiton, evenly mix, make homogeneous mixture solotion;
(5) solution that mixes in the step (4) is cooled to 150～580 ℃ under normal pressure, adopts the The tape casting film forming;
(6) at room temperature after the drying, place under 80～550 ℃ of temperature and inert environments under heat-treat;
(7) proton exchange membrane is placed the H of 1.0～10.0vol%
2O
2Boiled in the aqueous solution 30～120 minutes, and removed organic impurities, take out the back and use washed with de-ionized water, place the dilution heat of sulfuric acid of 0.1～1.0M to boil again 30～240 minutes,, take out the back and clean up with deionized water to remove inorganic metal ion.
3. according to the described preparation technology from the humidification electrolyte compound film for solid of claim 2, it is characterized in that: the absolute alcohol kind solvent described in the step (2) is to contain the following absolute alcohol solvent of 8 C atoms; Absolute alcohol kind solvent described in the step (3) adopts and contains the following absolute alcohol solvent of 5 C atoms.
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| CN102142574A (en) * | 2011-02-25 | 2011-08-03 | 江苏冰城电材股份有限公司 | Practical proton exchange membrane fuel cell generator |
| CN103887518B (en) * | 2014-03-26 | 2016-08-17 | 清华大学 | A kind of ordered polymer membrane electrode from humidification |
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