CA2264830C - Solid electrolyte composite for electrochemical reaction apparatus - Google Patents

Abstract

A solid polymer electrolyte composite for an electrochemical reaction apparatus that possesses satisfactory ion conduction properties and has excellent mechanical strength and heat resistance, is provided. The solid polymer electrolyte composite is characterized in that a solid polymer electrolyte is contained in the continuous pores of an expanded porous polytetrafluoroethylene sheet which has continuous pores and in which the inner surfaces defining the pores are covered with a functional material such as a metal oxide. An electrochemical reaction apparatus containing an electrolyte, wherein said electrochemical reaction apparatus is characterized in that the aforementioned solid polymer electrolyte composite is used as this electrolyte is also provided.

Description

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W O 98/11614 PCTrUS97/16178 TITLE OF THE INVENTION
SOLID ELECTROLYTE COMPOSITE FOR
ELECTROCHEMICAL REACTION APPARATUS

FIELD OF THE INVENTION
This invention relates to composite membranes for use in electrochemical apparatus and processes. More particularly, the invention relates to microporous membranes that contain electrolytes in the pores.

BACKGROUND OF THE INVENTION
Solid polymer electrolytes have recently attracted attention as electrolytes for lithium cells and the like because of the following advantages (1) the energy density of a cell can be increased because the material can double as a separator, (2) leakage-free, high-reliability cells can be obtained by providing1~ an all-solid construction, (3) it is easier to reduce the thickness or weight of a cell or to obtain an irregular shape, and the like.
There are two types of conventional solid polymer electrolytes: (1) polymers containing metal salts and (2) polymeric gels containing electrolyte solutions. With the first type, complexes of metal salts and polar polymers such as PEO (polyethylene oxide) form, and transport of lithium and other such ions accompanies the molecular motion of polymer chains. Such solid polymer electrolytes have high mechanical strength, but their ionic conductivity at roomtemperature has a limit on the order of 10-4 S/cm. It is therefore necessary to lower the mo'ccul~r weight or to soften the polymers in order to intensify the molecular motion of the polymer chains, but this approach ultimately leads to a reduction in mechanical strength. With the second type, the contained electrolyte functions as an ionic conductor and preserves the polymers as solids. The ionic conductivity of such solid polymer electrolytes is on the order of 10-3 S/cm, that is, falls within a practicable range, but a disadvantage is that the polymers are plasticized by the electrolyte, and their mechanical strength is lowered.
Demand has existed for some time for solid polymer electrolytes whose ionic conductivity is on the order of 10-3 S/cm, whose thickness is on a par with that of con\/enLional separators, and which have :il,enyll~ that does not present CA 02264830 1999-03-0~

W O 98tll614 PCTrUS97/16178 problems in terms of handling. Heat resistance is another consideration that has come into play in recent years as the performance of electrochemical reaction apparatuses has improved. In other words, a solid polymeric electrolyte composite for an electrochemical reaction apparatus should be able 5 to preserve its diaphragm functions even when the apparatus heats up.
Composite solid polymeric electrolytes obtained by packing a solid polymer electrolyte into the pores of a polymeric porous film have been proposed as products satisfying both the ionic conductivity and mechanical strength requirements for solid polymer electrolytes (Japanese Laid-Open Patent Applications 1-158051, 2-230662, and 2-291607), but a satisfactory electrolyte has yet to be obtained.
Therefore, one object of the present invention is to provide a composite that utilizes a solid polymeric electrolyte for an electrochemical reaction apparatus that possesses satisfactory ion conduction properties and has 15 excellent mechanical strength and heat resistance, and to provide an electrochemical reaction apparatus in which this electrolyte is used.
Ion exchange membranes are well known. Ion exchange membranes which utili~e a microporous media have previously been disclosed (U.S. Patent Nos. 5,547,551 and 5,599,614). Hitherto, the use of a microporous media was 20 proposed primarily as a means of providing a "mechanical reinforcement function" only of the ion exchange media. This mechanical reinforcement provided improved dimensional stability as well as the capability to provide thinner overall membranes which in turn improved overall transport properties of the film (as measured through ionic conductance cr moisture vapor

2~ transmission).
Also dLle:lllpl~ to enhance ion exchange membrane properties have been attempted in the past by adding an additional component. U.S. Patent 5,547,911 to Grot relates to a method to apply a layer of catalytically active pa,licles to the surface of a membrane. U.S. Patent 4,568,441 relates to the 30 application of non-conductive inorganic particle to the surface of a membrane to improve it's gas release properties. Neither of these teach that the dispersion of an additive within the membrane results in higher performance.

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W O 98/11614 PCTrUS97/16178 U.S. Patent 5,322,602 to Razaq relates to improving the performance of an ion exchange polymer membrane by treating it with an acid which diffuses into the membrane.
WO 96/29752 to Grot et al reiates to the incor~or~lion of various 5 inorganic fillers into a membrane to decrease fuel crossover. The ability to make thin very high conductance membranes is not ad~llessed.
U.S. Patent 5,523,181 ( and Japanese patents 6-1 1 1827 and 6-11 1834) to Stonehart et al relates to an ion exchange membrane in which silica is dispersed throughout the membrane. No indication is made to a microporous 1 0 substrate.
U.S. Patent 5,472,799 to Watanabe relates to an ion exchange membrane which incorporates a catalyst layer. While a thin membrane is mentioned as desirable, no mention is made of a microporous support.
U.S. Patent Nos. 5,547,551 and 5,599,614 relate to the use of a 15 microporous support where the function is to improve strength and mechanical properties, allowing the use of thin high conductance membranes. The addition of fillers within the microporous support is not addressed; however, the use of additives with the ion exchange medium to enhance specific functional properties is disclosed. But it is difficult to distribute additive particles 20 adequately since the microporous reinforcement also acts as a filtration medium impeding the flow of finely divided particulates.
There remains a need for thin high conductance membranes which have enhanced properties through the use of a functional support with the car~bility to provide multiple functions uniformly.
SUMMARY OF THE INVENTION
The shortcomings of the art are overcome by this invention which is:
a composite membrane co",prisi"g:
a) a microporous polymeric sheet having its pores extending from 30 one side to the other, b) the structure defining the pores being at least partially covered with a functional material selected from:
i) inorganicparticulate;
ii) metal; and CA 02264830 1999-03-0~

iii) an organic polymer;
c) the pores of the sheet being at least partially filled with polymer electrolyte selected from:
i) polymer compositions that contains metal salts;
ii) polymeric gels that contain electrolyte, and iii) an ion exchange resin.

BRIEF DESCRIPTION OF Tl IE DRAWINGS
The operation of the present invention should become apparent from the following description when considered in conjunction with the accompanying drawings, in which:
Figure 1 depicts a structural cross-sectional diagram of a lithium secondary cell pertaining to the present invention;
tigure 2 depicts a plan view of a positive electrode terminal film doubling as a positive electrode collector made of aluminum;
Figure 3 depicts a plan view of a negative electrode terminal film doubling as a negative eleGtrode collector made of copper; and Figure 4 depicts a porous microstructure having additives and polymer electrolyte.
DETAILED DESCRIPTION OF THE INVENTION
An important feature of the invention is the functional material b). By "functional" is meant that the material has some feature which affects the properties and function of the composites.
The MicroPorous Sheet Suitable microporous polymer films include those made from polyolefins, polyamides, polycarbonates, ~ellu'os ~s, polyurethanes, polyesters, polyethers, polyacrylates, copolyether esters, copolyether amides, chitosan, and fluoropolymers. Suitable fluoropolymers include membranes of porous polytetrafluoroethylene, more preferably a membrane of expanded porous PTFE (sometimes referred to as ePTFE) produced by the process taught in U.S. Patent No. 3,953,566 (to Gore).

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Porous polytetrafluoroethylene sheet or film suitable for use in the invention can be made by processes known in the art, for example, by stretching or drawing processes, by papermaking processes, by processes in which filler materials are incorporated with the PTFE resin which are 5 subsequently removed to leave a porous structure, or by powder sintering processes. Preferably the porous polytetrafluoroethylene film is porous expanded polytetrafluoroethylene film having a structure of interconnected nodes and fibrils, as described in U.S. Patent Nos. 3,953,566 and 4,187,390 which describe the preferred material and processes for making them. The 10 nodes and fibrils define an internal structure having a three-dimensional network of interconnected passages and pathways which extend vertically, from surface to surface, and laterally, from edge to edge, throughout the membrane. The porous polytetrafluoroethylene membrane should have a thickness in the range 3 to 1,000 micrometers, preferably in the range 5 to 100 15 micrometers; a pore volume in the range 20 to 98 percent, preferably in the range 50 to 90 percent; and a nominal pore size in the range 0.05 to 15 micrometers, preferably in the range 0.1 to 2 micrometers.
Microporous films of other polymers such as thermoplastic polymers are described in U.S. Patent No. 4,539,256 to Sherman, incorporated herein by 20 reference. Preparation of microporous polyurethanes is described in U.S.
Patent No. 4,429,000. Preparation of microporous polymeric films, especially microporous polyolehns (polyethylene, polypropylene, polybutenes, polypentenes, etc.) is described in British Patent 1339207. Preparation of microporous films by stretching is described in U.S. Patent No. 4,726,989 25 where use of polyamides, polyolefins, polystyrenes, polyvinylidene fluoride, and polycaprolactanes are described. Preparation of microporous films by liquid extraction is described in U.K. Publication No. GB 2,026,381. Stretching is described in U.S. Patent No. 4,100,238. Preparation by film fracture, hot stretching is described in U.S. Patent No. 3,679,540. All these patents are 30 incorporated by reference for their description of the polymers.
GB 2,026,381 discloses the preparation of membranes having a porous surface by blending polymer with a liquid component to form a binary two-phase system which, in the liquid aggregate state, has a region of miscibility and a region with miscibility gaps, forming a sheet of the blend, casting the film . .

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W O 98/11614 PCT~US97/16178 into a bath of the liquid component and removing the liquid component to provide porosity. The resultant non-oriented porous sheet has a relatively low tensile strength.
U.S. Patent Nos. 3,953,566, 3,962,153, 4,096,227, 4,110,392, 4,187,390 and 4,194,041, all incorporated by reference, describe the preparations of porous articles, including microporous sheets, formed of polytetrafluoroethylene(PTFE), a non-thermoplastic polymer, which is characterized by having a microstructure of nodes connected by fibrils. Such articles are produced by extruding a paste comprised of PTFE particles and a lubricant, removing the lubricant and ~etching and annealing the resultant product. The resultant product is a sintered, oriented porous film of PTFE.
U.S. Patent Nos. 4,100,238 and 4,197,148, incorporated by reference, describe the preparation of microporous films by extruding a two component blend, solvent leaching one dispersed component and stretching the resultant leached film to obtain a desired porosity. The blend consists of polymer and a leachable, non-miscible substance. Once the leachable dispersed polymer phase is removed and the film oriented, a porous film results.
U.S. Patent No. 3,679,540, incorporated by reference, discloses a method for making a microporous polymer film by cold stretching an elastic polymer film until porous surface regions are formed by film failure, hot stretching the cold stretched film until fibrils and pores or open cells are formed and then heat setting the resultant film. Controlled porosity is generally not attained in such films because they do not always uniformly fibrillate to a specific pore size.
Certain U.S. patents disclose the preparation of porous polymer film by blending into the polymer non-miscible leachable particulate substance such as starch, salts, etc., forming a sheet and leaching the particulate substance fromthe polymer sheet. Such U.S. Patents, incorporated by reference, include:
U.S. Patent Nos. 3,214,501 and 3,640,829, U.S. Patent No. 3,870,593 discloses the preparation of a microporous polymer sheet by blending non-miscible, non-leachable filler into the polymer, forming a sheet of the blend and stretching the sheet to form pores which are initiated at the sites of the filler particles.

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W O 98/11614 PCTnUS97/16178 U.S. Patent No. 4,539,256 which patent is hereby incorporated by reference, teaches a method of making a microporous sheet which comprises the steps of melt blending a cryst~";7~h'~ thermoplastic polymer with a compound which is miscible with the thermoplastic polymer at the polymer 5 melting temperature but immiscible on cooling below the polymer melting temperature, forming a sheet of the melt blend, cooling the sheet to a temperature at which the compound becomes immiscible with the polymer to cause phase separation between the thermoplastic polymer and the compound to provide a sheet.
Such porous polymer films or sheets will preferably have a porosity of greater than 35%. More preferably, the porosity should be between 40-95%
preferably 70%. The thickness of the film is preferably less than 2 mil (0.05 mm, 50 micrometers). Preferably the thickness is between 0.06 mils (1.5 m) and 1.6 mils, and most preferably the thickness is between 0.50 mils (0.013 mm) and 1.50 mils (0.038 mm).
A preferred film is expanded porous PTFE commercially available in a variety of forms from W. L. Gore & Associates, Inc., under the trademark GORE-TEX membrane. The porous microstructure of such expanded porous PTFE films either comprises nodes interconnected by fibrils, or comprises 20 substantially fibrils with substantially no nodes present. Preferred porous expanded PTFE films can be characterized as having a bubble point between 10 and 60 psi; and an air flow between 20 Frazier and 10 Gurley seconds. It may also have a pore size distribution value between 1.0~ and 1.20; and a ball burst sllenylh between 0.9 and 17 pounds/force.
The Functional Material The material covering the structure defining the pores can be a metal oxide. The metal oxides endow the composite with improved mecl1an ~. ' s~ nylll sustainable over a long period of time. ePTFE has good inherent 30 mechan.~" I strength, but this mechanical strength must be further enhanced by the metal oxide.
The metal oxide also acts as a matrix to stably retain the solid polymer electrolyte in the pores at a high content. Because of its high porosity, the ePTFE is capz~'e of accepting and holding large amounts of solid polymer CA 02264830 1999-03-0~

electrolytes. In addition, the solid polymer electrolyte that fills the pores cannot be desorbed easily because it is retained by the fine fibrils and minute nodes of ePTFE. Furthermore, the oxides, improve the wettability of the microporous sheet, making it easier for the solid polymer electrolyte to pack the pores.
In addition, the metal oxide is stable at elevated temperatures. The performance of lithium cells and other electrochemical reaction apparatuses is gradually improving, and it is believed that heating is caused by the repeated charging and discharging occurring at a high current density, by short circuits,and by other undesirable phenomena. If the solid polymer electrolyte lacks heat resistance or is incapable of preserving its shape at high temperatures, the functions are lost and an extensive short circuit occurs, creating the danger of a malfunction. A composite acts to prevent a short circuit from forming between electrodes.
In the present invention, an expanded porous polytetrafluoroethylene which has continuous pores and in which the inner surfaces of the pores are covered with a metal oxide is used in order to retain the aforementioned solid polymer electrolyte. Examples of the metal oxides used in this case include oxides of the following elements: lithium, beryllium, boron, sodium, magnesium, aluminum, Ai [sic], phosphorus, potassium, calcium, cerium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, gallium, germanium, selenium, rubidium, strontium, yttrium, zirconium, niobium, molybdenum, ruthenium, rhodium, palladium, cadmium, indium, tin, antimony, tellurium, cesium, barium, lanthanum, cerium, praseodymium, neodymium, samarium, europium, cadmium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, thorium, protactinium, hafnium, tantalum, tungsten, platinum, titanium, lead, bismuth, and the like.
Functional additives can be, for example, an inorganic filler, or a catalyst or a com~ ~alion of such materials. Examples include, but are not limited to, silica, platinum, titanium dioxide, platinum supported on silica, platinum supported on titania, carbon, boron nitride, barium titanate, or a blend of materials, or a polymer such as a fluorocarbon, or a polyolefin, etc. - different to the original microporous substrate and the ion exchange material utilized such as for example perflouro sulfonic acid resin.

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W O98/11614 PCT~US97/16178 One application is an improved self humidified membrane for a PEM
fuel cell where the filler is silica or titanium dioxide which serves to aid in the back ."ig,dlion of product water from the cathode to the anode.
A second application is a self humidified low gas cross over PEM fuel 5 cell membrane where the filler is platinum, or platinum supported on silica ortitania, which serves to react and produce water in the membrane from any reactant which might otherwise diffuse through the membrane and degrade open circuit performance.
A third application is where the filler is boron nitride which serves to aid 10 in heat conduction through the membrane.
A fourth application is a super capacitor where the filler is boron titanate which serves to increase the dielectric capability of the membrane.
A fifth application is where the filler is electrically conductive and serves to transport electrons through the membrane as well as protons for the 15 production of H202 in a shorted fuel cell arrangement. This allows a much simpler cell design since it is no longer necessary to provide an external path for the electrons to flow.
A sixth - FF' s;ltion is where the filler is an ion exchange material which serves to improve the bond between the support and an ion exchange material 20 in the polymer electrolyte.
A seventh application is where the filler is a material which lowers the surface energy of the substrate thus improving or allowing wetting and easier prucessing of ion exchange material into the microporous structure.

25 The Polvmeric Electrolvte (1) Polymer compositions that contain metal salts.
Examples of polymer compositions include polyethers, polyesters, polyimides, cross-linked polyethers, polymers containing polyether segments, polymers of vinyl silane having alkoxy groups, polymethyl siloxanes having 30 ethylene oxy (EO) groups, polyphosphazenes having EO groups, polymethacrylic acid esters having EO groups, polyacrylic acid, polyaziridine, polyethylene sulfide, and other polar polymer subslances. Examples of electrolytes in the polymers include various metal salts such as LiCI04, LiCF3SO3, LiF, Nal, Lil, NaSCN, LiBF4, LiPF6, LiBPh4 (Ph: phenyl group), and CA 02264830 1999-03-0~
Wo 98/11614 PCT/US97t16178 other alkali metal salts, as well as sulfuric acid, phosphoric acid, trifluoromethanesulfonic acid, tetrafluoroethylenesulfonic acid, and other proton acids.

5 (2) Polymeric gels that include electrolytes.
These polymers absorb and gel an electrolyte. Examples of such electrolyte solutions include solutions obtained by dissolving electrolytes and other necessary soluble polymers in organic solvents such as propylene carbonate, ~-butyrolactone, dimethoxyethane, dioxane, tetrahydrofuran, 10 acetonitrile, dimethyl sulfoxide, methyl tetrahydrofuran, and sulfolane. The polymers are not subject to any particular limitations as long as they are polymers that have cross-linked structures and are capable of absorbing and gelling the aforementioned electrolyte solutions, and any of the various conventionally known products can be used.

(3) lon-Exchange Resins The ion-exchange polymeric materials used can be any ion-exchange materials that will provide the desired result. The materials are preferably fluorinated because the material should be substantially inert to chemical 20 activity and should be heat resistant.
The ion-exchange polymeric material will of course contain ionic functionality, preferably sulfonic moieties, carboxylic moieties or phosphonic moieties. The functional groups are present in an amount sufficient to impart ion-exchange properties to the polymer. An equivalent weight too high results 25 in the electrical resistivity being too high. But if the equivalent weight is too low, mechanical sl,enylh becomes poor. The ionic functionality will usually be provided by carboxylic, sulfonic or phosphonic ~roups present either on the polymer backbone or present on pendant groups that extend from the polymer backbone in a recurring fashion. The polymer backbone will preferably be a 30 fluorinated hydrocarbon backbone chain. The functional group preferably will have the structure -COOM,--SO~M or PO3M2, where M is hydrogen, a metallic cation or NH+4. If a metallic cation, it will preferably be an alkali metal or an alkaline earth metal, such as Na+, K+ or the like.

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W O 98/11614 PCTrUS97/16178 For carboxylic functionality, the pendant side chains which carry the above functional groups may have at the terminal end of the side chain a group of the formula:

~F-- V or -0 ~F-- V

Z / I \ Z T

where V is -COOM, Z is -F or -CF3 and T iS an integer of 1-12, preferably 1 or 2, as described in U.S. Patent 4,437,951 to DuPont, all of which is incorporatedby reference for its disclosure of both carboxylic and sulfonic functionality.
The sulfonyl polymers with which the present invention is concerned are typically polymers having a fluorinated hydrocarbon backbone chain to which are attached the sulfonic containing functional groups as pendant side chains.
For sulfonic polymers, terminal portion of the side chains can be:

-CFRSO3M, -CF2CFRSO3M, or -OCF2CF2-SO3M, or the like where R is F, Cl, or perfluoroalkyl and M is as described earlier.
For phosphoric polymers, the same sort of pendant groups are present.
Other ion-exchange resins useful herein, in addition to the fluorinated 25 carboxylic resins and the fluorinated sulphonic and phosphoric resins described above, include, but are not limited to, polyvinyl alcohol (PVA), divinyl benzene/styrene copolymers, provided they have the requisite functional groups pendant chains. The polymers can be mixed with a metal salt to obtain the desired functionality. A sulfonated polymer of trifluorostyrene, such as 30 homopolymer or a copolymer with tetrafluoroethylene, can be used.
It is understood that the foregoing description of ion-exchange resins is not limited and is representative. It is understood that the invention can employ any polymer type of ion-exchange material. Thus, as seen above, not only do the resins include ones with the functional group as a part of the polymer, but . . .

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W O 98/11614 PCT~US97/16178 also ones where the functional groups are provided by an additive to the polymer.
The ion-exchange resins used in the invention can be prepared by general polymerization techniques developed for homo and copolymerizations of fluorinated ethylenes, particularly those employed for tetrafluoroethylene whichare described in the literature. Nonaqueous techniques for preparing the copolymers include that of U.S. Patent No. 3,041,317, that is, by the polymerization of a mixture of the major monomer therein, such as tetrafluoroethylene, and a fluorinated ethylene containing a sulfonyl fluoride group in the presence of a free radical initiator, preferably a perfluorocarbon peroxide or azo compound, at a temperature in the range 0-200~C. and at pressures in the range of 105 to 2 x 107 Pascals (1-200 Atm.) or higher. The nonaqueous polymerization may, if desired, be carried out in the presence of a fluorinated solvent. Suitable fluorinated solvents are inert, liquid, perfluorinated hydrocarbons, such as perfluoromethylcyclohexane, perfluorodimethylcyclobutane, perfluorooctane, perfluorobenzene and the like, and inert, liquid chloro-fluorocarbons such as 1,1,2-trichloro-1,2-2-trifluoroethane, and the like. Aqueous techniques for preparing such copolymers include contacting the monomers with an aqueous medium containing a free-radical initiator to obtain a slurry of polymer particles in non-water-wet or granular form, as disclosed in U.S. Patent No. 2,393,967, or contacting the monomers with an aqueous medium containing both a free -radical initiator and a telogenically inactive dispersing agent, to obtain an aqueous colloidal dispersion of polymer particles, and coagulating the dispersion, as disclosed, for example, in U.S. Patent No. 2,559,752 and U.S.
Patent No. 2,593,583.
In addition, ion-exchange polymer resins described and prepared as in U.S. Patent Nos. 4,267,364 to DuPont; 4,544,458 to DuPont; 4,178,218 to Asahi; 4,255,523 to Asahi; 5,082,472 to Mallouk, et al.; and 5,422,411 to Wei, et al., all incorporated by reference, can be used.
Other exar"r'es of lon exchange materials include, such as polyvinyl alcohol, divinyl benzene, styrene based polymers, alpha beta triflurostyrene, ora ketone based ionomer such as sulfonated polyetherketone ether ketone (PEKEK) and metal salts with or without a polymer. The ion exchange CA 02264830 1999-03-0~

W O 98/11614 PCT~US97/16178 material may also be comprised of at least in part a powder such as but not limited to carbon black, graphite, nickel, silica, titanium dioxide, platinum, boron nitrate, barium titanate or a non-ionic polymer such as poyvinylidene fluoride or a co-polymer of TFE, etc.

Preparation where metal oxide is the functional material.
An ePTFE in which the inner surfaces of the pores are covered with a metal oxide can be manufactured by a method comprising the following steps:
a step in which the ePTFE is impregnated with a gelation product in the form of 10 a solution obtained by allowing water to react with a hydrolyzable metal-containing organic compound, a step in which the gelation product in the form of a solution absorbed by the pores is allowed to react with water and converted to a gelation product in the form of a soiid, and a step in which the gelation product in the form of a solid thus formed is heated and dried.
A metal alkoxide or metal complex is formed as the aforementioned hydrolyzable metal-containing organic compound (also referred to as the "metal oxide precursor").
Specific examples of metal alkoxides include tetramethoxytitanium, tetraethoxytitanium, tetraisopropoxytitanium, tetrabutoxytitanium, zirconium isopropylate, zirconium butyrate, tetramethoxysilane, tetraethoxysilane, tetraisopropoxysilane, and tetra-t-butoxysilane. Specific examples of metal complexes include titanium tetraacetyl acetonate, zirconium acetylacetonate, and other metal acetylacetonates. In the present invention, a silicone-based alkoxide such as tetraethoxysilane is particularly suitable for use.
The aforementioned metal oxide precursor is brought into contact with water, partially gelled, and made into a gelation product in the form of a solution before being complexed with the ePTFE. The gelation reaction can be a reaction well-known in the past, including a hydrolysis/polycondensation reaction.
Water can be added to the metal oxide precursor, and agitation and mixing can be performed, in order to partially gel the metal oxide precursor. A
water-miscible organic solvent such as methanol, ethanol, propanol, butanol, or another alcohol can be added to the water in this case, and an acid (hydrochloric acid, sulfuric acid, nitric acid, acetic acid, hydrofluoric acid, or the .. .

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4 PCT/US97/16178 like) or a base (sodium hydroxide, potassium hydroxide, ammonia, or the like) can also be added as needed. The partial gelation reaction of the metal oxide precursor can also be performed by adding water to the solution of the metal oxide precursor in an organic solvent, and agitating and mixing the system. In

5 this case, any solvent can be used as the organic solvent as long as it is capable of dissolving the metal oxide. Aliphatic and aromatic hydrocarbons can be used in addition to alcohols. The gelation reaction is performed at a temperature that is generally 0 to 100~C and preferably 60 to 80~C.
The proportion in which water is used should be 0.1 to 100 mol, and 10 preferably 1 to 10mol, per mole of the metal oxide precursor. Although it is preferable for the gelation reaction to be performed in a sealed system or in a flow of inert gas, it is also possible to promote the gelation reaction by the moisture contained in the outside air.
A partially gelled product in the form of a solution of the metal oxide 15 precursor is thus obtained. As used herein, the term "partially gelled product of a metal oxide precursor" refers to a product used under conditions corresponding to the use of a metal oxide hydrous gel in the form of a solid that is a completely gelled product and that lacks fluidity.
To allow the partially gelled product of a metal oxide precursor to form a 20 complex with the microporous sheet, it is possible to adopt a method in whichthe sheet is immersed in the partially gelled product in the form of a solution or a method in which the partially gelled product in the form of a solution is applied to the sheet with a spray or a roll, and any method can be used as long as it allows the partially gelled product to fill the pores of the surface portion and the 25 interior of the sheet.
The sheet that has been complexed with the partially gelled product of a metal oxide precursor in such a manner is brought into contact with an excess amount of contained water in order to further promote the gelation reaction of the metal oxide precursor and to form a metal oxide hydrous gel in the form of 30 a solid (completely gelled product). It is preferable for a method in which the sheet cor"r'-xed with the partially gelled product of a metal oxide precursor isimmersed in water to be used for such complete gelation, but it is also possibleto use methods in which sprayed water is blown, steam is blown, or the like. In this case, the water used may contain acids or alkalis because it is used to CA 02264830 1999-03-0~

promote the gelation reaction. A metal oxide hydrous gel is produced in the form of a film on the inner surfaces of the pores of the molding after the gelation reaction has been completed, and a monolithically deposited metal oxide forming a thin, uniform layer on the inner surfaces of the pores can be obtained by drying the gel at 300~C or lower, and preferably 200~C or lower.
The thickness of the metal oxide layer is 0.01 to 0.2~m, and preferably 0.02 to 0.1 ~m. Because it is formed from a metal oxide hydrous gel obtained in such a manner, the metal oxide forms a monolithic, continuous film and has excellent adhesion that impairs its separation from the porous body. The metal oxide composite molding has a high void volume, which is at least 50%, and preferably at least 70%, of the void volume of the initial molding.
Alternatively, the functional material can be introduced into the micropores of the polymeric sheet by imbibing the material into the pores and then heating to remove the imbibing solvent. When the microporous polymeric sheet is polytetrafluoroethylene (PTFE), the functional material can be added by mixing a particulate filler with a PTFE aqueous dispersion; cocoagulating thefiller and the PTFE; lubricating the filled PTFE with lubricant; paste extrudingand optionally calendering to form a film; and expanding the film by stretching it so as to form a porous PTFE membrane having the filler distributed therein.
Alternatively, the microporous ePTFE can be plated with a metal described in US Patent 4,720,400 (Manniso).
Alternatively, a microporous article such as catalyst filled ePTFE
described in part by US Patent 5,602,669 may be used as the substrate.
The solid polymer electrolyte can be placed into the pores by roll a~p' G~tion, spraying, dipping, or another technique with a solution or dispersion containing the solid polymer electrolyte, and the solvent is then removed. The pores can be filled with a polymerization solution comprising an electrolyte anda monomer, and the ingredients polymerized inside the pores. The pores can be filled with a polymerization solution comprising an electrolyte, a monomer, and a solvent, the ingredients polymerized inside the pores, and the solvent is suhseqLIently removed. The pores can be filled with an electrolyte-containing partially gelled solution of a polymer, and the ingredients are gelled inside the pores. Specific methods for introducing a solid polymer electrolyte into the CA 02264830 1999-03-0~

pores of a molding are appropriately selected in accordance with the type of solid polymer electrolyte.
The pores can be either partially or fully imbibed with ion exchange medium such as an ionomer in an alcohol solution such as is commercially 5 available from Ashai Glass such as Flemion~ solution in ethanol. The ion exchange medium may subsequently be dried or re-dissolved as the case may require.
A product of the invention is depicted in Figure 4. A composite membrane 10 is provided which is made up of a microporous polymeric sheet 10 comprised of nodes 11 and fibrils 12. In some embodiments, the sheet can be comprised of only fibrils. The nodes and fibrils are covered, at least in part by functional material 13. The space between the nodes and fibrils is then filled, preferably, completely (i.e., no air flow through) with the polymer electrolyte.Preferably the interior volume of the sheet is substantially occluded by the 1 5 electrolyte.
The composite membranes of the present invention may be employed in various ~FF'irations, including but not limited to polarity based chemical separations, electrolysis, fuel celis, batteries, pervaporation, gas separation,dialysis, industrial electrochemistry, super acid catalyst, medium for enzyme 20 immobilization and the like.
Examples of use in some electrochemical applications include lithium primary cells, magnesium cells, and other primary cells, lithum secondary cells;polymer cells and other secondary cells; and fuel cells.

25 ExamPle 1 100 parts of tetraethoxysilane (manufactured by Sinetsu Silicone), 52 parts of water, and 133 parts of ethanol were allowed to react for 24 hours at 80~C under reflux conditions in which the supply of moisture contained in the outside air was shut off with the aid of a calcium chloride tube, yielding a 30 partially gelated solution of a metal oxide precursor. An expanded porous polytetrafluoroethylene film (manufactured by Japan Gore-Tex Inc.; thickness:
25 llm; pore diameter: 0.5 ~ m; thickness: 40 ~m; porosity: 92%) was impregnated with this solution and immersed in warm water (60~C) for 5 hours to complete the gelation. The gelled product was dried for 30 minutes at CA 02264830 1999-03-0~

150~C, yielding a silica gel complex extended porous polytetrafluoroethylene film in which the exposed surfaces, including the inner surfaces, of the porous body were covered with the silica gel. This composite film retained at least 80% of the voids of the original porous film and was highly porous.
An acrylonitrile-methacrylate copolymer powder obtained from Japan Exlan Co. Ltd (molar ratio: 90/10) was subsequently added at a rate of 1.5 9/10 ml, and acetonitrile was added at the same time at a rate of 1.5 g/10ml, to an organic electrolyte solution obtained by dissolving LiPF6, an electrolyte liquidmixed with propylenecarbonate and ethyl carbonate obtained from Tomiyama Pure Chemical Industry, in a mixed solvent (organic solvent) of propylene carbonate and ethylene carbonate (volume ratio: 1/1) in such a way that the concentration was 1M, yielding an acetonitrile-diluted polymeric gel molecule/electrolyte mixture.
The acetonitrile-diluted polymer gel/electrolyte mixture was subsequently absorbed by the pores (cavities) of the aforementioned silica gel composite extended porous polytetrafluoroethylene film, then vacuum-dried for at least 5 hours at 60~C to remove the acetonitrile, and finally cooled to -20~C, yielding a solid polymer electrolyte composite with a thickness of about 25 ~lm.
The ionic conductivity (20~C; complex impedance technique) and the tensile strength as tested by JIS K 7113, of this polymer solid electrolyte composite were measured. The results are shown in Table 1.

Compal~Live ExamPle 1 An acetonitrile-diluted polymeric gel/electrolyte mixture prepared in the same manner as in Example 1 was cast, yielding a solid polymer electrolyte (simple substance) with a thickness of 25 llm. In this case, the simple solid polymer electrolyte had insufficient mechanical strength, was difficult to handle, and was impractical as a film.
For the sake of comparison, a solid polymer electrolyte film (simple substance) composed of a polymer/electrolyte with a thickness of 1 OO~lm was fabricated, and the ionic conductivity (20~C; complex impedance technique) and tensile strength of the film were measured. The results are shown in Table 1.

CA 02264830 1999-03-0~

W O 98/11614 PCTrUS97/16178 It follows from Table 1 that the solid polymer electrolyte composite of the present invention is a solid polymer electrolyte in which the mechanical strength is significantly improved while the ionic conductivity is maintained atthe level of a conventional solid polymer electrolyte. The composite of the 5 present invention can be easily made into a thin film and stably fabricated into a solid polymer electrolyte film of about 25 tlm, making it possible to reduce theresistance of the solid polymer electrolyte portion.

Item Example 1 Comparative Example lonic conductivity 1.5 x 10-~ 1.5 x 10-~
(slcm2) Tensile strength 150 8 (kg/cm2) Example 2 A lithium secondary cell will now be described as an embodiment 15 example of an electrochemical reaction apparatus obtained using the aforementioned solid polymer electrolyte composite.
Figure 1 is a structural cross-sectional diagram of the lithium secondary cell of the present invention. In Figure 1, 1 is the solid polymer electrolyte composite film pertaining to the present invention; 2 is a positive electrode 20 terminal film doubling as a positive electrode collector made of aluminum; 3 is a positive electrode film consisting of LiCoO2 (obtained from Nippon Chemical Ind.), acetylene black (obtained from Denki Kagaku as Denka Black), and a polymeric gel/electrolyte mixture (corresponds to a product obtained by removing acetonitrile from the aforementioned acetonitrile solution); 4 is a 25 negative electrode terminal film doubling as a negative electrode collector made of copper; 5 is a negative electrode film consisting of graphite and a polymeric gel/electrolyte mixture (corresponds to a product obtained by removing acetonitrile from the aforementioned acetonitrile solution); 6 is a seal;
and 7 is a casing. Figure 2 is a plan view of the positive electrode terminal film 30 doubling as a positive electrode collector made of aluminum. In Figure 2, A is a positive electrode terminal, and B is a positive electrode collector.

CA 02264830 1999-03-0~

W O 98/11614 PCTrUS97/16178 Figure 3 is a plan view of the negative electrode terminai film doubling as a negative electrode collector made of copper. In Figure 3, C is a negative electrode terminal, and D is a negative electrode collector.
The method for manufacturing the aforementioned cell will now be 5 described.

(1 ) Manufacture of Laminate L of Positive Electrode Film and Positive Electrode Terminal Film Doublin~ as Positive Electrode Collector Made of Aluminum 15 g of an acrylonitrile-methacrylate copolymer powder (molar ratio:
90/10) and 12 g of acetonitrile were simultaneously added to 100 ml of an organic electrolyte solution obtained by dissolving LiPF6 in a mixed solvent (organic solvent) of propylene carbonate and ethylene carbonate (volume ratio:
1/1 ) in such a way that the concentration was 1 M, yielding an acetonitrile-diluted polymer gel/electrolyte mixture.
4 g of an LiCoO2 powder with a mean grain diameter of about 20 ~m and 0.2 g of acetylene black were subsequently added to 7.3 g of the aforementioned acetonitrile-diluted polymer gel/electrolyte mixture, and the ingredients were uniformly agitated, yielding a starting solution for the positive electrode. This starting solution was spread over the entire surface (with the exception of the terminal A) of the flat aluminum positive electrode collector 2(thickness: 20 ~lm) shown in Figure 2, the collector was vacuum-dried for over 5 hours at 60~C to remove the acetonitrile, and the dried collector was cooled to -20~C.
A laminate L of the positive electrode film 3 and the positive electrode terminal film 2 doubling as a positive electrode collector made of aluminum was thus obtained. In this laminate L, the terminal (A in Figure 2) measured 1 cm x 2 cm and had a thickness of 20 ~lm, and the positive electrode collector (B in Figure 2) measured 5.8 cm x 5.8 cm and had a thickness of 220 ~m.

CA 02264830 1999-03-0~

WO 98/11614 PCTtUS97116178 (2) Manufacture of Laminate M of Ne~ative Electrode Film and Ne~ative Electrode Terminal Film Doublinq as Ne~ative Electrode Collector Made of Copper 4 g of a partially graphitized carbon material (obtained from Kureha Chemical Co. Ltd) with a mean grain diameter of about 10 ~m was added to 7.3 g of the aforementioned acetonitrile-diluted polymer gel/electrolyte mixture, and the ingredients were uniformly agitated, yielding a starting solution for the negative electrode. This starting solution was spread over the entire surface (with the exception of the terminal C) of the flat copper negative electrode collector 4 (thickness: 20 ~m) shown in Figure 3, the collector was vacuum-dried for over 5 hours at 60~C to remove the acetonitrile, and the dried collector was cooled to -20~C.
A laminate M of the negative electrode film 5 and the negative electrode terminal film 4 doubling as a negative electrode collector made of copper was thus obtained. In this laminate M, the terminal (C in Figure 3) measured 1 cm x 2 cm and had a thickness of 20 ,um, and the negative electrode collector (D in Figure 3) measured 5.8 cm x 5.8 cm and had a thickness of 520 ~m.

(3) Manufacture of Solid Polvmer Electrolyte Composite Film A film 1 measuring 5.8 cm x 5.8 cm was manufactured from the solid polymer electrolyte composite film (thickness: 25 ~lm) of Practical Example 1.

(4) Cell Manufacture The aforementioned laminate L was superposed on one side of the solid polymer electrolyte composite film 1, the aforementioned laminate M was superposed on the other side, and the resulting assembly was kept at a pressure of 1 kglcm2 for 1 minute, yielding a laminate.
The laminate was subsequently introduced into a casing (7 in Figure 1) that consisled of polypropylene, was open at one end, and had a thickness of 1 mm. The open end was sealed with polypropylene resin film, yielding a seal (6 in Figure 1).
The lithium secondary cell thus obtained was subjected to chargeldischarge cycle tests at a temperature of 20~C, an upper limit of 4.3 V, CA 02264830 1999-03-0~

WO 9$/11614 PCT/US97/16178 and a lower limit of 3.0 V, with the discharge being conducted at a constant current of 8 mA. The results are shown in Table 2.

Comparative ExamPle 2 A lithium secondary cell was manufactured using, as an electrolyte film, the solid polymer electrolyte (simple substance; thickness: 25 ~m) of Comparative Example 1 instead of the solid polymer electrolyte composite film in Practical Example 2, but the components were difficult to handle and could not be made into a cell.
In view of this, a lithium secondary cell was fabricated in the same manner as in Practical Example 2, except that the solid polymer electrolyte film(simple substance; thickness: 100 11m) of Comparative Example 1 was used instead of the solid polymer electrolyte composite film.
The resulting cell was subjected to charge/discharge cycle tests at a temperature of 20~C, an upper limit of 4.3 V, and a lower limit of 3.0 V, with the discharge being conducted at a constant current of 8 mA. The results are shown in Table 2.
It can be seen in Table 2 that the lithium secondary cell of the present invention remains stable over a large number of cycles and that the cell capacity deteriorates only slightly even when the number of cycles exceeds 200.
By contrast, the lithium secondary cell of Comparative Example 2 iS
configured in such a way that the solid polymer electrolyte portion (simple substance) of the cell is four times thicker than the corresponding portion of the cell obtained in Practical Example 2, quadrupling the resistance of the solid polymer electrolyte portion (simple subsl~nce). As a result, the capacity deteriorates only slightly even when the number of cycles exceeds 200, but the discharge capacity is low. These results indicate that the present invention allows a compact, high-performance cell to be obtained.

.. . , . , . .. ~

CA 02264830 l999-03-0~

W O 98/11614 PCTrUS97/16178 Tabie 2 Number of Discharge capacity (mAh) charge/
discharge cycles Productof present Cor"paris~n invention product 1 46.5 40.0 56.3 43.2 100 56.2 43.1 150 - 56.2 42.9 200 56.1 42.8 250 56.0 42.7 ExamPle 3 A multi-functional membrane was made by a) mixing a particulate filler with PTFE aqueous dispersion, b) cocoagulating the filler and the PTFE
c) lubricating the filled PTFE with lubricant d) paste extruding and optionally calendering to form a film e) expanding said film by stretching it so as to form a porous PTFE having said filler distributed therein.
An aqueous dispersion of PTFE resin (20-36% solids) was obtained. Into the aqueous dispersion, particulate filler of Fumed Silica, Cabosil~ M5, from Cabot Corp. was added to produce a 20% by weight silica final dried mixture.
This mixture was cocoagulated by rapid shearing of the aqueous dispersion. A
c-oagulum of fine powder PTFE resin and silica filler was subsequently formed and dried into cakes. When dry, the cakes were carefully crumbled and lubricated with an odorless mineral spirit. The amount of mineral spirits used was 0.52 grams per gram of PTFE/SiO2 dry powder.
This mixture was aged below room temperature to allow for the mineral spirits to become uniformly distributed within the PTFE/SiO2 powder resin. This mixture was compressed into a billet and extruded at 1200 psi through a 0.045 inch by 6 inch gap die attached to a ram type extruder to form a coherent extrudate. A reduction ratio of 44:1 was used.
Two layers of extrudate were stacked together to form 100 mil assembly and subsequently rolled down between two metal rolls which were heated to between 50~C. The final thickness after roll down was 0.014 inch. The material CA 02264830 1999-03-0~

W O98/11614 PCT~US97116178 23 was transversely expanded at a ratio of 3:1 and then the mineral spirits were removed from the extrudate by heating the mass to 250~C (i.e. a temperature where the mineral spirits were highly volatile). The dried extrudate was transversely expanded at 150~C at a ratio of 3.5:1 and a rate of 2300% per second. After expansion, the sheet was amorphously locked at greater than 340~C and cooled to room temperature.
This membrane was subsequently imbibed with ion exchange resin solution as in example 5 to create a ion exchange composite membrane.
Electrodes loaded at 0.3 mg /cm2 platinum were attached to both sides of the membrane and the membrane electrode assembly was placed in a single cell fuel cell test apparatus.
Air and H2, both at 40 psig and 25~C, were fed to the cell. A steady state current of 1.178 amps/cm2 was produced at 0.5 volts with no humidification of the incoming reactants. Cell temperature was 50"C. A microreinforced membrane with no filler yielded only 0.975 amps at the same test conditions.

Example 4 An aqueous dispersion of PTFE resin was obtained. Into the aqueous dispersion, a particulate carbon black (Ketjen Black) filler was added to produce a 20% by weight final dried mixture. This mixture was cocoagulated by rapid shearing of the aqueous dispersion. A coagulum of fine powder PTFE
resin and carbon filler was subsequently formed and dried into cakes. When dry, the cakes were carefully crumbled and lubricated with an odorless mineral spirit. The amount of mineral spirits used was 0.20 grams per gram of PTFE /
carbon black dry powder.
This mixture was compressed into a billet and extruded at 1500 psi through a 0.045 inch by 6 inch gap die attached to a ram type extruder to form a coherent extrudate. A reduction ratio of 84:1 was used.
The extrudate was then rolled down between two metal rolls which were heated to between 50~C. The final thickness after roll down was 0.010 inch.
The mineral spirits were removed from the extrudate by heating the mass to 250~C (i.e. a temperature where the mineral spirits were highly volatile). The dried extrudate was transversely expanded at 150~C at a ratio of 3.5:1. After CA 02264830 1999-03-0~

expansion, the sheet was heated to amorphously locked at greater than 340~C
and cooled to room temperature.
This membrane was subsequently imbibed with Flemion~ (Asahi Glass) ion exchange resin solution (9 % by weight resin in ethanol) and dried 3 times.
The final composite thickness was 27 microns.

Example 5 An aqueous dispersion of PTFE resin is obtained. Into the aqueous dispersion, a particulate titania filler was added to produce a 20% by weight final dried mixture. This mixture was cocoagulated by rapid shearing of the aqueous dispersion. A coagulum of fine powder PTFE resin and titania filler was subsequently formed and dried into cakes. When dry, the cakes were carefully crumbled and lubricated with an odorless mineral spirit. The amount ofmineral spirits used was 0.20 grams per gram of PTFE / titania dry powder.
This mixture was compressed into a billet and extruded at 1500 psi through a 0.045 inch by 6 inch gap die attached to a ram type extruder to form a coherent extrudate. A reduction ratio of 84:1 was used.
The extrudate was then rolled down between two metal rolls which were heated to between 50~C. The final thickness after roll down was 0.008 inch.
The mineral spirits were removed from the extrudate by heating the mass to 250~C (i.e. a temperature where the mineral spirits were highly volatile). The dried extrudate was transversely expanded at 1 50~C at a ratio of 3.5:1 and at arate of 440% per second. After expansion, the sheet was amorphously locked at greater than 340~C and cooled to room temperature.
2~ It was subsequently imbibed with ion exchange media by brushing both sides with a solution of PFSA in ethanol (Flemion~9 9% by weight).

Example 6 An aqueous dispersion of PTFE resin was obtained. Into the aqueous 30 disper~iont a platinum coated titania catalyst was added to produce a 10% by weight final dried mixture. This mixture was cocoagulated by rapid shearing of the ~queous dispersion. A coagulum of fine powder PTFE resin and catalyst filler was subsequently formed and dried into cakes. When dry, the cakes were CA 02264830 1999-03-0~

W O 98111614 PCT~US97tl6178 carefully crumbled and lubricated with an odorless mineral spirit. The amount of mineral spirits used was 0.26 grams per gram of PTFE/catalyst dry powder.
This mixture was compressed into a billet and extruded at 3000 psi through a 0.045 inch by 6 inch gap die attached to a ram type extruder to form a coherent extrudate. A reduction ratio of 44:1 was used.
The extrudate was then rolled down between two metal rolls which were heated to 50~C. The final thickness after roll down was 0.016 inch. The mineral spirits were removed from the extrudate by heating the mass to 250~C (i.e. a temperature where the mineral spirits were highly volatile).
A portion of this roll was then placed within a batch film expansion machine and expanded at an expansion rate of 500% per second to a ratio of 12:1 in both the machine and transverse direction.
This microporous membrane was subsequently imbibed with a fluorinated sulfonic acid resin composition as in example 5. The final thickness of the 15 composite membrane was 15 microns. Electrodes with a total of 0.6 mg Pt/cm2 were attached and the membrane tested in a single cell fuel cell test apparatus.Air and H2, both at 40 PSIG. and 25~C, were fed to the cell. A steady state current of 0.47 amps/cm2 was produced at 0.8 volts with no humidification of the incoming gasses. Cell temperature was 50~C. A 15 micron 20 micro~einforced membrane with no filler yielded only 0.36 amps at 0.8 volts under the same conditions.

Voltage for Voltage for CurrentExample 5 Example 7 DensityMembrane Membrane 300 mA/cm20.835 0.810 600 mA/cm20.775 0.750 900 mA/cm20.705 0.670 While particular embodiments of the present invention have been illustrated and described herein, the present invention should not be limited tosuch illu:,l,alions and descriptions. It should be apparent that changes and modific~tions may be incorporated and embodied as part of the present invention within the scope of the following claims.

, ~ , . . ... . . .

Claims (55)

We claim:

1. A composite membrane for use in an electrochemical apparatus or process comprising:
a) at least one polymeric sheet having pores and inner surface area, b) wherein inner surface area of the polymeric sheet is covered with at least one metal oxide; and c) said pores being at least partially filled with at least one polymer electrolyte so that the composite membrane can be used in the electrochemical apparatus or process.

2. The membrane of claim 1 wherein said polymeric sheet is expanded porous PTFE.

3. The membrane of claim 1 wherein said polymeric sheet is ultra high molecular weight polyethylene.

4. The membrane of claim 1 wherein said polymer electrolyte is a polymer composition that contains metal salt.

5. The membrane of claim 1 wherein said polymer electrolyte is an ion-exchange resin.

6. The membrane of claim 1 wherein said polymeric sheet is expanded porous PTFE, and the polymer electrolyte is an ion-exchange resin that fills substantially all pores of the expanded porous PTFE.

7. The membrane of claim 6 wherein the expanded porous PTFE comprises nodes, and said metal oxide covers the nodes of the expanded porous PTFE.

8. The membrane of claim 6 wherein the expanded porous PTFE comprises fibrils, and said metal oxide covers the fibrils of the expanded porous PTFE.

9. The membrane of claim 6 wherein the expanded porous PTFE comprises nodes and fibrils, and said metal oxide covers the nodes and fibrils of the expanded porous PTFE.

10. An electrochemical reaction apparatus containing an electrolyte, wherein said electrochemical reaction apparatus is characterized in that the composite membrane of claim 1 is used as the electrolyte.

11. The membrane of claim 1 wherein the polymer electrolyte is a polymeric gel that contains an electrolyte.

12. The membrane of claim 1 wherein said metal oxide is an oxide of an element selected from the group consisting of: lithium, beryllium, boron, sodium, magnesium, aluminum, silicon, phosphorous, potassium, calcium, cerium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, gallium, germanium, selenium, rubidium, strontium, yttrium, zirconium, niobium, molybdenum, ruthenium, rhodium, palladium, cadmium, indium, tin, antimony, tellurium, cesium, barium, lanthanum,praseodymium, neodymium, samarium, europium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, thorium, protactinium, hafnium, tantalum, tungsten, platinum, lead, bismuth.

13. The membrane of claim 1 wherein said metal oxide is an oxide of silicon.

14. An electrolyte for use in an electrochemical reaction apparatus comprising solid polymer electrolyte which is contained in continuous pores of an expanded polytetrafluoroethylene film to provide the electrolyte with ionic conductance for use in the electrochemical reaction apparatus or process in which inner surface area of the film is covered with metal oxide layer.

15. An electrolyte according to claim 14, wherein the solid polymer electrolyte comprises at least one polar polymer complexed with at least one metal salt.

16. An electrolyte according to claim 14, wherein the solid polymer electrolyte comprises at least one polymeric gel comprising an electrolyte solution.

17. An electrolyte according to claim 14, wherein the solidpolymer electrolyte comprises at least one ion exchange resin.

18. An electrolyte according to claim 14, wherein the expanded polytetrafluoroethylene film has a porosity of 40% to 95%.

19. An electrolyte according to claim 14, wherein the expanded polytetrafluoroethylene film has a porosity of 70% to 95%.

20. An electrolyte according to claim 14, wherein the expanded polytetrafluoroethylene film has a thickness of three microns to 1,000 microns.

21. An electrolyte according to claim 14, wherein the expanded polytetrafluoroethylene film has a thickness of five microns to 100 microns.

22. An electrolyte according to claim 14, wherein the expanded polytetrafluoroethylene film has a thickness of thirteen microns to 38 microns.

23. An electrolyte according to claim 14, wherein the electrolyte is prepared by:
(a) providing the expanded polytetrafluoroethylene film, (b) impregnating the film with a precursor to the metal oxide, (c) heating the precursor-impregnated film to form the metal oxide from the precursor to the metal oxide.

24. An electrolyte according to claim 23, wherein the precursor to the metal oxide is a gel.

25. An electrolyte according to claim 23, wherein the heating is carried out at a temperature of 300°C or lower.

26. An electrolyte according to claim 23, wherein the heating is carried out at a temperature of 200°C or lower.

27. An electrolyte according to claim 14, wherein the thickness of the metal oxide layer is 0.01 microns to 0.2 microns.

28. An electrolyte according to claim 14, wherein the thickness of the metal oxide layer is 0.02 microns to 0.1 microns.

29. An electrolyte according to claim 14, wherein the metal oxide layer is a monolithic, continuous layer.

30. An electrolyte according to claim 14, wherein:
the film of expanded polytetrafluoroethylene with the metal oxide layer but without polymer electrolyte has a first void volume, and the film of expanded polytetrafluoroethylene without the metal oxide layer and without polymer electrolyte has a second void volume, and the first void volume is at least 50% of the second void volume.

31. An electrolyte according to claim 30, wherein the first void volume is at least 70% of the second void volume.

32. An electrolyte according to claim 30, wherein the first void volume is at least 80% of the second void volume.

33. A composite membrane for use in an electrochemical apparatus or process comprising:
a) a polymeric sheet comprising polymer and having a porous structure:
b) said polymeric sheet having distributed in the polymer:
i) inorganic particulate;
ii) metal;
iii) an organic polymer; or a combination thereof, and c) said porous structure being at least partially filled with an ion-exchange resin to provide ionic conductance for use in the electrochemical apparatus or process.

34. The membrane of claim 33 wherein the polymeric sheet has distributed therein an inorganic finely divided powder.

35. The membrane of claim 33 wherein the polymeric sheet has distributed therein a precious metal.

36. The membrane of claim 33 wherein the polymeric sheet has distributed therein silica.

37. The membrane of claim 33 wherein the polymeric sheet has distributed therein fumed silica.

38. The membrane of claim 33 wherein the polymeric sheet has distributed therein titania.

39. The membrane of claim 33 wherein the polymeric sheet has distributed therein carbon.

40. The membrane of claim 33 wherein the polymeric sheet has distributed therein platinum.

41. The membrane of claim 33 wherein the polymeric sheet has distributed therein platinum supported on a substrate.

42. The membrane of claim 33 wherein said polymeric sheet is expanded porous PTFE, and said ion-exchange resin fills substantially all pores of the expanded porous PTFE.

43. The membrane of claim 33, wherein the polymeric sheet has inorganic particulate distributed therein.

44. The membrane of claim 33, wherein the polymeric sheet has metal distributed therein.

45. The membrane of claim 33, wherein the polymeric sheet has an organic polymer distributed therein.

46. The membrane of claim 33, wherein the polymeric sheet has a thickness of less than 50 microns.

47. The membrane of claim 33, wherein the membrane is disposed between two fuel cell electrodes.

48. The membrane of claim 47, wherein the membrane disposed between two fuel cell electrodes provides a steady state current of at least 1.178 amps/cm 2 at 0.5 volts, with no humidification of incoming fuel cell air and hydrogen reactants, with air and hydrogen feed both at 40 psig and 25°C, and the fuel cell temperature at 50°C.

49. The membrane of claim 48, wherein the polymeric sheet has a thickness of less than 38 microns.

50. A composite membrane for use in an electrochemical apparatus or process comprising:
a) a polymeric sheet comprising polymer and having a porous structure and a thickness of less than 50 microns, b) said polymeric sheet having distributed in the polymer inorganic particulate, metal, or a combination thereof;
c) said porous structure being at least partially filled with polymeric gel that contains electrolyte to provide ionic conductance for use in the electrochemical apparatus or process.

51. The composite membrane of claim 50, wherein said porous structure is substantially filled with polymeric gel than contains electrolyte.

52. A composite membrane for use in an electrochemical apparatus or process comprising:

a) a polymeric sheet comprising polymer and having a porous structure, b) said polymeric sheet having distributed in the polymer inorganic particulate, metal, or a combination thereof, c) said porous structure being at least partially filled with a polymer composition that contains metal salts to provide ionic conductance for use in the electrochemical apparatus or process.

53. The composite membrane of claim 52, wherein said porous structure is substantially filled with a polymer composition that contains metal salts.

54. The composite membrane of claim 52, wherein the polymeric sheet has a thickness less than 50 microns.

55. The composite membrane of claim 54, wherein the polymeric sheet has a porosity of 40% to 95%.