2. Background Art Various devices have been utilized for dispensing fluids, where the fluids are dispensed over an extended period of time at a predictable substantially constant rate. One such device for dispensing fluid, as shown in Fig. 1, is based on using an electrochemical gas generating cell in which hydrogen gas is electrochemically generated to pressurize a gas chamber which, in turn, dispenses the fluid from the device.

A prior art construction of a hydrogen-generating cell is of a Zn-air type cell, shown in Fig. 2. A Zn-air cell typically utilizes zinc as the anode, a carbon based cathode and an alkaline solution as the electrolyte. The anode cap subassembly is comprised of a Zn alloy, an electrolyte, and the cap. The cathode can subassembly is comprised of a carbon-based porous electrode, a separator, and the can, all of which are crimped together using a plastic grommet as an insulator.

Various prior art patents describe the construction of such cells. For example, U. S.

Patent No. 3,894, 538, issued to Richter and U. S. Patent No. 4,023, 648, issued to Orlitzky disclose metal-air cells for generating hydrogen as a motive force. Similarly, Winsel, U. S.

Patent No. 5,242, 565 and Winsel EP 1013296 both disclose use of a conventional Zn-Air cell for generating hydrogen or oxygen as a motive force. However, none of these references utilize a cathode structure which is hydrogen permeable and, substantially impermeable to preclude ingress of oxygen, carbon dioxide And water (moisture) into and out of the associated cell. Although such prior art cells can be utilized as hydrogen generative cells, they are very inefficient and have short storage life in their active state mainly due to interference of 02 and C02 as well as loss of moisture through the cathode.

Accordingly, it is an object of the present invention to provide for an improved cell construction, which overcomes the shortcomings of the prior art. It is also an object of the present invention to convert commercially available Zn-air cells and prior art hydrogen generative cells into storage stable and efficient hydrogen gas generative cells by attaching a non-porous membrane to the cathodic side of the outer housing so that °2 and C02 are prevented from entering the cathode while water vapor is simultaneously prevented from escaping the cell through the cathode. Furthermore, it is an object of the present invention to provide a device in which hydrogen is permitted to escape from the cell.

SUMMARY OF THE INVENTION One embodiment of the invention comprises a galvanic cell, which includes an anode cap subassembly comprising a metal anode, electrolyte, a cathode can subassembly, a micro- porous separator, and a sealing grommet. The anode may comprise zinc, lead, iron, magnesium, aluminum and mixtures and alloys thereof.

The cathode can subassembly is further comprised of a cathode that is permeable to hydrogen, but substantially impermeable to 02, H20 and CO2. In a preferred embodiment, the cathode comprises at least one of a non-porous dense electrically conducting polypropylene, a non-porous composite of carbon, Teflon, and FEP foil; a palladium foil, an iron titanium foil, an iron magnesium foil, as well as metallic membranes of one or more of palladium, nickel, titanium, and, non-porous polymers, and composites of ceramics and palladium. The cathode materials will not allow 02, moisture and C02 to permeate in and out of the cell but will allow hydrogen to escape the cell.

In another preferred embodiment, the cathode includes a graded porosity. In such an embodiment, the cathode comprises a graded porosity from a highly porous structure (50% pores with a pore size of 1 micron or greater) to a non-porous structure along its thickness. In this case, a carbon Teflon composite with graded porosity is cladded to non-porous FEP foil.

This cathode structure exhibits the required properties for highly efficient hydrogen generative systems that warrant that the cathode is hydrogen-permeable but impermeable to 02, CO2, and H20.

In another preferred embodiment, the cathode comprises a nonporous conductive cathode.

In a preferred embodiment, the cathode comprises a non-porous conductive polymer.

In one such preferred embodiment, the polymer comprises at least one of conductive Teflon and conductive polypropylene or conductive polyethylene.

In a preferred embodiment, the at least one aperture of the outer shell comprises a plurality of apertures, each of which has a diameter of less than about 5 microns.

In another aspect of the invention, the invention comprises a system comprising a commercial Zn-air cell or prior art galvanic electrochemical H2 gas generating cell and a membrane. The galvanic electrochemical H2 gas-generating cell includes at least one aperture for releasing gas. The membrane is associated with the at least one aperture. The membrane is hydrogen permeable and substantially impermeable to 02, C02 and water, to, in turn, preclude the passage of 02, COs and water into and out of the cell, and to facilitate the permeation of hydrogen through the at least one aperture.

The commercial Zn-air cells as well as prior art hydrogen generating electrochemical cells use a gas permeable porous cathode through which all the gases including 02, H20, and CO2 can permeate. This permeation results in 02 and C02 interference and water loss during operation, and in turn, low efficiency and short storage life during the hydrogen generating mode. The present embodiment of the invention describes the construction and method of converting commercial Zn-air cells and prior art hydrogen cells to more efficient hydrogen generating cells by incorporating such cells so that the cathode is not exposed to outside Oz, H2O, and C02, but allows generated hydrogen to escape.

In one preferred embodiment, the membrane is electrically conductive. In one such preferred embodiment, the membrane is selected from the group consisting of : electrically conductive non-porous polypropylene ; sintered composite of carbon, Teflon, and FEP foil ; palladium foil, iron titanium foil, iron magnesium foil, as well as metallic membranes of one or more of palladium, nickel, titanium, and, non-porous polymers, and composites of ceramics and palladium.

In another preferred embodiment, the membrane is electrically insulative. In one such preferred embodiment, the membrane comprises at least one of polypropylene and Teflon.

In a preferred embodiment, the system further includes an outer casing assembly encircling a portion of the membrane and at least a portion of the cell. In one such preferred embodiment, the outer casing assembly further comprises a cap, a can and an isolation grommet positioned between the can and the cap.

The present invention is also directed to a method for generating hydrogen using a zinc anode-based electrochemical cell comprising the steps of associating an electrically conductive circuit with a storage-stable hydrogen generating cell, with one end of the circuit connected to a anode subassembly of the cell, and the other end of the circuit connected to a cathode subassembly of the cell having a non-porous cathode, generating hydrogen within the cell electrochemically, and selectively releasing hydrogen from the cell through the non-porous cathode, while simultaneously preventing the passage of oxygen and water into or out of the cell.

BREIF DESCRIPTI ON OF THE DRAWINGS Fig. 1 is a prior art fluid delivery device using a gas-generating cell; Fig. 2 is a cross-sectional view of typical prior art hydrogen generating cell; Fig. 3 is a cross-sectional view of an H2 generating cell of the present invention; Fig. 4 is a cross-sectional view of a cathode with graded porosity of present invention; Figs. 5-8 are cross-sectional views of various structures related to conversion of Zn-air cells to hydrogen generating cells of the present invention; Fig. 9 shows a fluid delivery device of the present invention wherein the commercial Zn-air cell is converted into an H2 generating cell; Fig. 10 (a) shows the total volume of a fragrance dispensed as a function of time; Fig. 10 (b) shows the rate of dispensing as a function of time; Fig. 11 (a) shows the total volume of a fragrance dispensed as a function of time; and Fig. 11 (b) shows the rate of dispensing as a function of time.

DETAILED DESCRIPTION OF THE DRAWINGS While this invention is susceptible of embodiment in many different forms, there is shown in the drawings and will herein be described in detail several specific embodiments with the understanding that the present disclosure is to be considered as an exemplification of the principles of the invention and is not intended to limit the invention to the embodiments illustrated.

Zinc anode-based electrochemical cell, or"button cell"10 is shown in Fig. 3, as comprising zinc-based anode subassembly 20, non-porous cathode-based cathode subassembly 30, and grommet 40. Zinc based anode subassembly 20 comprises metal cap 22 containing a Zn alloy, and alkaline electrolyte 24. Non-porous cathode-based cathode subassembly 30 comprises can 32, and at least one aperture 34. Cathode subassembly 30 is further comprised of non-porous cathode structure 36 and separator 38. Although the present description will be with respect to a zinc based anode, it will be understood to those having ordinary skill in the art that other metals, such as zinc, lead, iron, magnesium, aluminum and mixtures and alloys thereof, can likewise be used. Accordingly, the present invention should not be limited to a zinc air cell.

Non-porous cathode structure 36 comprises several possible embodiments, as illustrated in Figs. 4-8. The various non-porous cathode structures shown include standard cathode structures of commercial Zn-air cells with additional outside enclosures so as to render the cathodes hydrogen-permeable, but impermeable with respect to oxygen, C02 and water.

Such cathode structures may take many forms, but preferably include membranes formed from materials such as non-porous, dense polypropylene, palladium foil, iron titanium foil, iron magnesium foil, and sintered composites of carbon, Teflon, and FEP foil. Of course, other structures and materials which exhibit the foregoing properties of permeation are likewise contemplated for use, including, but not limited to other metallic membranes of palladium, nickel, titanium, non-porous polymers, composites of ceramics and palladium, as well as combinations and mixtures thereof.

One particularly useful embodiment involves a conductive non-porous polypropylene or Teflon cathode (or other non-porous conductive polymer cathode). In that embodiment, the polypropylene or Teflon cathode is permeable to hydrogen, but impermeable to 02 and to water/moisture. In operation of such an embodiment, hydrogen is generated on the conductive portion of the conductive polymer and then permeated through the polymer material.

One of the possible structures of cathode 36 is shown in Fig. 4 as comprising a graded cathode 50. Graded cathode 50 comprises an electrode having a graded porosity such that it is most porous at the side facing the electrolyte 22 and substantially non-porous at the side facing the gas side 26. Such a graded electrode can be achieved by varying the catalyst material to density material ratio throughout the thickness in order to increase/decrease permeation of materials accordingly. The density material to catalyst material ratio may then eventually be increased so that at least a portion of graded cathode 50 is non-porous.

Additionally, it may be desirable to clad a non-porous film 28 to the porous cathode composite, as can also be seen in Fig. 4. The catalyst material of such an embodiment generally comprises graphite, active carbon, Reney nickel or other metals suitable for hydrogen generation such as for instance platinum or palladium. Of course, other materials are contemplated for the catalyst. In addition, materials such as Teflon and polypropylene, among others, are contemplated for use as the density material.

In another embodiment of the invention, the cathode may comprise a completely non- porous cathode. Such a cathode is preferably a sintered composite of polymer and conductive material. The thickness of such a non-porous composite cathode is at least about 0.001 inches.

Such a cathode is obtained by way of sintering the composite of polymer and conductive material under pressure and heat. For example, polypropylene powder or Teflon powder is mixed with metals or carbon and then sintered under pressure.

Referring again to Fig. 3, a grommet 40 (preferably of nylon) electrically isolates the anode cap 22 from the cathode can 32. The cathode can 32 is then crimped around the grommet assembly forming a seal. The cathode can 32 is comprised of nickel-plated steel, and is in direct electrical contact with the cathode 36. The can 32 has at least one aperture 34 to permit passage of gasses in or out of the cell. In one embodiment, aperture 34 may comprise a plurality of apertures.

As shown in Fig. 5, the advantages of the above-described cathode structure may be provided to commercially available Zn-air cells by including membrane 60 to Zn-air cell 62 so as to provide a storage stable H2 gas generating system. Membrane 60 includes the above- described properties of being hydrogen permeable while being substantially impermeable to 02, C02 and water. The membrane may be either conductive or insulative. The materials for membrane 60 may comprise those materials identified above and, in addition, non-conductive non-porous polypropylene and Teflon. By way of example, as shown in Fig. 5, membrane 60 may be positioned in a gas-tight engagement with a lower surface 64 of the Zn-air cell 62 (i. e., the cathode can).

The embodiments of Figs. 6-8 are all capable of use in association with conventional Zn-air cells, so as to provide the advantages of membrane 60 thereto. Specifically, as shown in Fig. 6, the Zn-air cell 62 may further be supplemented with outer casing assembly 70, which includes metal casing can 72. Metal casing can 72 includes lower opening 74 and may comprise a conductive metal material. In such an embodiment, membrane 60 may be positioned in a gas-tight engagement with lower surface 64 of the conventional cell 62.

Subsequently, the entire cell 62 with membrane 60 may be positioned within metal casing can 72 such that electrical connectivity is achieved between the conventional cell and metal casing can 72. In addition, a portion of membrane 60 remains exposed within lower opening 74.

Once properly assembled, the metal casing can 72 is crimped much like cathode can 10 of Fig.

3.

In another embodiment of the invention, as shown in Fig. 7, the conventional cell may be further supplemented with another embodiment of outer casing assembly 70. In this embodiment, assembly 70 includes cap 80, can 82 and isolation grommet 84. In such an assembly, a standard zinc-air cell 62 is first positioned within cap 80. Thereafter, isolation grommet 84 is extended around cap 80. Next, membrane 60 is positioned such that membrane 60 contacts both the isolation grommet 84 and the cathode can 32 of the cell. The cell 62 is positioned within can 80, wherein the can 82 is crimped to the isolation grommet 84 and the cap 80. Can 82 includes lower opening 74 so as to expose at least a portion of the membrane 60. In such an embodiment, membrane 60 comprises a conductive membrane such as palladium foil, iron titanium foil and iron magnesium foil, among others.

Alternatively, Fig. 8 illustrates a similar embodiment of the present invention as that shown in Fig. 7, configured so that membrane 60 is not required to be conductive.

Specifically, Fig. 8 shows the same embodiment as in Fig. 7, with outer casing assembly 70 having cap 80, can 82 and isolation grommet 84, along with having cell 62 enclosed inside assembly 70, and membrane 60 associated just below lower opening 74. However, the device in Fig. 8 additionally includes conductive ring 86 associated between bottom of cell 62 and membrane 60. As can be seen, ring 86 connects the bottom of cell 62 with can 82, providing a conductive connection. Therefore, even if membrane 60 is not conductive, ring 86 provides a conductive path to complete a circuit for operation.

In operation, the above-described device may be placed into any of a number of devices requiring hydrogen evolution for operation. These devices, including several that will be described further herein, connect the anode 20 and the cathode 30 subassemblies of the present invention electrically, activating the zinc-air cell 62 contained within. Once activated, zinc-air cell begins producing hydrogen at a measured rate, which then passes out of the cell 62 through the non-porous cathode 36 and separator 38, if necessary, and then through the at least one aperture 34, to the outside device. Simultaneous to this process, cathode 36 and/or separator 38 help to prevent the influx and efflux of oxygen, CO2, and/or water moisture to/from the cell 62.

Two working examples are described below.

Example I Commercial Zn-air cells were used as hydrogen generating cells by incorporating an hydrogen permeable but 02, moisture, and CO2 impermeable shield or membrane so that under shunt resistance of 4.3 kilo-ohms and 11.3 kilo-ohms, these cells generated hydrogen. Zn-air cells obtained from ENERGIZES were used in cartridges as shown in Fig. 9. The cartridges were filled with fragrances, while the Zn-air cells were sealed in a dense non-porous polypropylene shield or membrane. A total of eight cartridges were fabricated. Four cartridges were shunted with 4.3 Kilo-ohms while four remaining cartridges were shunted with 11.3 Kilo-ohms. Fig. 10 (a) shows the total volume of fragrance dispensed as a function of time, while Fig. 10 (b) shows the rate of dispensing as a function of time. As one can see, the present invention, when integrated into the above device, increased the total life of cell operation, while allowing for more consistent and controlled fragrance flow.

Example II Graded cathode based zinc electrochemical cells were used where the cathode is non- porous. The cathode in the cell is permeable to hydrogen substantially impermeable to 02, H20 and CO2. The cathode is a composite of sintered Teflon and carbon sheet attached to a non-porous FEP disc. The cells were packaged in a fluid delivery cartridge with fragrance as the fluid. A total of nine cartridges were tested. Fig. 11 (a) shows the total volume of fragrance dispensed as a function of time, while Fig. 1 l (b) shows the rate of dispensing as a function of time. The use of the graded cathode structures of the present invention enabled producible results to be obtained for both the rate of delivery and the total volume delivered over time.

The foregoing description merely explains and illustrates the invention and the invention is not limited thereto except insofar as the appended claims are so limited, as those skilled in the art who have the disclosure before them will be able to make modifications without departing the scope of the invention.