Direct isopropanol fuel cell
11677090 · 2023-06-13
Assignee
Inventors
- Heiner Ophardt (Arisdorf, CH)
- Volker Loos (Sankt Wendel, DE)
- Gregor Hoogers (Trier, DE)
- Albrecht Lang (Niederbipp, CH)
Cpc classification
H01M8/04634
ELECTRICITY
H01M8/04216
ELECTRICITY
H01M8/1025
ELECTRICITY
Y02E60/50
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
H01M8/04082
ELECTRICITY
H01M8/1011
ELECTRICITY
Abstract
A direct isopropanol fuel cell adapted for use in ambient conditions and utilizing as fuel isopropanol and water preferably with isopropanol at relatively high concentrations representing 30% to 90% isopropanol.
Claims
1. A method of use of a direct isopropanol fuel cell, comprising: providing a direct fuel cell comprising: a proton conducting or exchange membrane with a cathode side and an anode side, a cathode having a cathode catalyst on the cathode side of the membrane and an anode having an anode catalyst on the anode side of the membrane such that the membrane is arranged between the cathode and the anode, operating the direct fuel cell to generate electricity by supplying the anode with a liquid fuel and supplying the cathode with atmospheric air from the atmosphere containing oxygen; characterized by: the cathode is open to the atmosphere placing the cathode side of the membrane passively in communication with the atmosphere, the anode catalyst is selected from the group of a platinum and ruthenium catalyst, a platinum and nickel catalyst, a platinum and gold catalyst, and mixtures thereof, the cathode catalyst comprises a platinum catalyst, the liquid fuel consisting of 10% to 90% by volume isopropanol, 90% to 10% by volume water and 0% to 30% by volume acetone in contact with the anode catalyst on the anode side of the membrane, operating the fuel cell at electrical potentials between the anode and cathode such that a reaction at the anode catalyst to oxidize a molecule of isopropanol into a molecule of acetone releasing two electrons is a principal reaction, and the membrane selected to permit the acetone at the anode catalyst to pass through the membrane to the cathode side of the membrane into communication with the atmosphere, the acetone at the anode catalyst passing through the membrane to the cathode side of the membrane into communication with the atmosphere and evaporating into the atmosphere at the cathode side of the membrane.
2. A method as claimed in claim 1 including operating the fuel cell at ambient temperatures, and providing the atmospheric air at ambient temperature to the cathode, and storing the liquid fuel at ambient temperatures and supplying the liquid fuel at ambient temperatures to the anode.
3. A method as claimed in claim 2 wherein the anode catalyst consists of the platinum and ruthenium catalyst, including operating the fuel cell at ambient temperatures in the range of plus 5 degrees Celsius to plus 40 degrees Celsius, the fuel cell comprises a membrane electrode assembly, the membrane electrode assembly comprising a layered assembly of an anode gas diffusion layer, an anode catalyst layer including the anode catalyst, the membrane, a cathode catalyst layer including the cathode catalyst, and a cathode gas diffusion layer in that order, and the membrane electrode assembly is between a cathode current collector on the cathode side of the membrane and an anode current collector on the anode side of the membrane, the cathode diffusion layer open to the atmosphere, the oxygen from the atmospheric air passing through the cathode diffusion layer to the cathode catalyst layer into contact with the cathode catalyst, the acetone at the anode catalyst passing through the anode catalyst layer to the anode side of the membrane, through the membrane from the anode side of the membrane to the cathode side of the membrane, from the cathode side of the membrane through the cathode catalyst layer to the cathode gas diffusion layer, and through the cathode gas diffusion layer into communication with the atmosphere with the acetone evaporating into the atmosphere, the acetone at the anode catalyst passing successively through the anode catalyst layer, membrane, and the cathode gas diffusion layer into communication with the atmosphere with the acetone evaporating into the atmosphere.
4. A method as claimed in claim 2 including: providing the fuel cell in a dispenser of a hand cleaning fluid that has a dispensing pump to dispense a cleaning fluid onto a hand of a person, supplying the electricity generated by the fuel cell to the dispenser for operation of the dispenser, and operating the dispensing pump to dispense the hand cleaning fluid onto a person's hands, wherein the hand cleaning fluid includes the liquid fuel selected from the group consisting of: (a) the liquid fuel which has not been supplied to the anode, and (b) the liquid fuel after having been supplied to the anode.
5. A method as claimed in claim 1 including operating the fuel cell at electrical potentials between the anode and cathode greater than 200 mV.
6. A method as claimed in claim 5 wherein the liquid fuel having 40% to 90% by volume isopropanol, and 60% to 10% by volume water.
7. A method as claimed in claim 5 wherein the liquid fuel having of 65% to 75% by volume isopropanol, and 35% to 25% by volume water.
8. A method as claimed in claim 1 wherein the liquid fuel having 0% to 5% by volume acetone.
9. A method as claimed in claim 1 wherein: the fuel cell comprises a membrane electrode assembly, the membrane electrode assembly comprising a layered assembly of an anode gas diffusion layer, an anode catalyst layer including the anode catalyst, the membrane, a cathode catalyst layer including the cathode catalyst, and a cathode gas diffusion layer in that order, and the membrane electrode assembly is between a cathode current collector on the cathode side of the membrane and an anode current collector on the anode side of the membrane, the cathode diffusion layer passively open to the atmosphere, the oxygen from the atmospheric air passing through the cathode diffusion layer to the cathode catalyst, the anode diffusion layer in contact with the fuel, the fuel passing through the anode diffusion layer to the anode catalyst, the acetone evaporating from the cathode gas diffusion layer to the atmosphere.
10. A method as claimed in claim 1 including: providing the fuel cell in a dispenser of a hand cleaning fluid that has a dispensing pump to dispense a cleaning fluid onto a hand of a person, supplying the electricity generated by the fuel cell to the dispenser for operation of the dispenser, and operating the dispensing pump to dispense the hand cleaning fluid onto a person's hands, wherein the hand cleaning fluid includes the liquid fuel selected from the group consisting of: (a) the liquid fuel which has not been supplied to the anode, and (b) the liquid fuel after having been supplied to the anode.
11. A method as claimed in claim 10 wherein the hand cleaning fluid consists of the liquid fuel selected from the group consisting of: (a) the liquid fuel which has not been supplied to the anode, and (b) the liquid fuel after having been supplied to the fuel cell.
12. A method as claimed in claim 4 wherein liquid fuel after having been supplied to the anode includes acetone produced by the oxidization of isopropanol in the fuel cell.
13. A method as claimed in claim 11 wherein the hand cleaning fluid includes less than 5% by volume of acetone.
14. A method as claimed in claim 1 wherein the supplying the cathode with atmospheric air from the atmosphere containing oxygen is by the cathode side of the membrane being passively open to the atmosphere.
15. A method as claimed in claim 1 wherein the supplying the anode with the liquid fuel includes providing the liquid fuel to the anode within a closed fuel system whereby the acetone created at the anode catalyst becomes part of the liquid fuel, and the acetone evaporating at the cathode side of the membrane into the atmosphere reduces the acetone in the liquid fuel.
16. A method as claimed in claim 1 wherein the liquid fuel having 40% to 90% by volume isopropanol, and 60% to 10% by volume water.
17. A method as claimed in claim 16 wherein the liquid fuel having 0% to 5% by volume acetone.
18. A method as claimed in claim 5 wherein: the fuel cell comprises a membrane electrode assembly, the membrane electrode assembly comprising a layered assembly of an anode gas diffusion layer, an anode catalyst layer including the anode catalyst, the membrane, a cathode catalyst layer including the cathode catalyst, and a cathode gas diffusion layer in that order, and the membrane electrode assembly is between a cathode current collector on the cathode side of the membrane and an anode current collector on the anode side of the membrane, the cathode diffusion layer passively open to the atmosphere, the oxygen from the atmospheric air passing through the cathode diffusion layer to the cathode catalyst, the anode diffusion layer in contact with the fuel, the fuel passing through the anode diffusion layer to the anode catalyst, the acetone evaporating from the cathode gas diffusion layer to the atmosphere, providing the fuel cell in a dispenser of a hand cleaning fluid that has a dispensing pump to dispense a cleaning fluid onto a hand of a person, wherein the hand cleaning fluid includes the liquid fuel selected from the group consisting of: (a) the liquid fuel which has not been supplied to the anode, and (b) the liquid fuel after having been supplied to the anode.
19. A method as claimed in claim 18 including operating the fuel cell at electrical potentials between the anode and the cathode not below 300 mV.
20. A method as claimed in claim 18 including operating the fuel cell at electrical potentials between the anode and the cathode in the range of 300 mV and 400 mV.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) Further aspects and advantages of the present invention will appear from the following description taken together with the accompanying drawings in which:
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DETAILED DESCRIPTION OF THE DRAWINGS
(25) Reference is made to
(26) The MEA 16 comprises five layers of which the center layer is a proton exchange membrane 20. On the right side of the proton conducting or exchange membrane 20 an anode catalyst 22 is provided. To the right of the anode catalyst 22, an anode gas diffusion layer (GDL) 24 is provided beside the anode current collector 26. On the left hand side of the proton electrode membrane 20, a cathode catalyst 23 is provided. To the left of the cathode catalyst 23 a cathode gas diffusion layer (GDL) 25 is provided beside the cathode current collector 27.
(27) To the left laterally outwardly of the cathode current collector 27, an air chamber 29 is defined within the cathode end plate 15. The air chamber 29 is open outwardly to the atmosphere via air openings 31 through the cathode end plate 15. On the right hand side the anode end plate 14 defines therein an anode fuel chamber 28 opening inwardly through the anode current collector 26 to the anode GDL 24. The anode fuel chamber 28 closed otherwise other than at a fuel chamber inlet 30 at an upper end of the anode fuel chamber 28 and a fuel chamber outlet 32 at a lower end of the anode fuel chamber 28.
(28) A fuel reservoir 34 is provided at a height below the anode fuel chamber 28. The fuel reservoir 34 is shown as an enclosed vessel with an enclosing wall 35. An air vent tube 289 provides an air vent passageway 36 through the wall 35 to the atmosphere so as to provide for equalization of the pressure inside the fuel reservoir 34 with the atmospheric air as, for example, to relieve any vacuum which may be developed within the fuel reservoir 34 as fuel is consumed by the fuel cell. A fuel chamber drain tube 290 provides a drain passageway 37 from fuel chamber outlet 32 to a drain tube outlet 291 in the fuel reservoir 34 to permit fluid within the anode fuel chamber 28 to flow, as under gravity, from the anode fuel chamber 28 into the fuel reservoir 34. A reservoir outlet 38 is provided connected via a fuel pump feed tube 293 providing a feed passageway 39 to a fuel pump 40. The fuel pump 40 is connected via a fuel pump discharge tube 294 providing a discharge passageway 41 to the fuel chamber inlet 30. The fuel pump 40 when operating draws fluid from the reservoir 34 via the feed passageway 39 and discharges it via the discharge passageway 44 into the anode fuel chamber 28.
(29) The anode current collector 26 comprises a conductive wire mesh or screen. An anode lead wire 42 is electrically connected to the anode collector 26 and extends upwardly therefrom. The cathode current collector 27 comprises a conductive wire mesh or screen. A cathode lead wire 43 is electronically connected to the cathode current collector 27.
(30) The anode lead wire 42 and the cathode lead wire 43 are schematically illustrated as connected so as to have an electronic load L therebetween as with electrons moving in the wires 42 and 43 in a direction indicated by the arrows 45 when the fuel cell arrangement is operational to create electrical energy. The load L is schematically illustrated as being electrically interconnected via a controller 47 to an electrical power storage device 46. The controller 47 is also electrically interconnected with an electric motor 48 to drive the fuel pump 40. In operation of the fuel cell arrangement 10 electrical power is generated by the cell 12 as schematically illustrated by the load L which power is under the control of the controller 47 directed as to be stored in electrical power storage device 46 and/or the delivered to the pump motor 48 to drive the fuel pump 40. The controller 47 preferably includes various sensing devices and capability to sense various aspects the operation of the fuel cell arrangement 10 the load L and the open circuit potential preferably over time. The electrical power storage device 46 may comprise rechargeable batteries, capacitors and the like.
(31) Reference is made to
(32) As a first addition, an air closure cover 50 is provided mounted for pivoting about a pivot axis 51 from an open position as shown in
(33) As a second addition, a fuel supply container 54 is provided which may, for example, comprise a bottle. The container 54 has a container outlet 55. The container 54 supplies the liquid fuel to the fuel reservoir 34 to maintain the fuel reservoir 34 substantially full of fuel. In
(34) In
(35) Reference is made to
(36) In
(37) The air closure cover 50 has a face plate 63 which in the closed position is disposed to closely overly and engage an outer face 64 of the cathode end plate 15 to prevent air communication between the atmosphere and the air chamber 29.
(38) Reference is made to
(39) Reference is made to
(40) Outwardly of the anode current collector 26 and the cathode current collector 27 are provided an anode seal 68 and a cathode seal 69, respectively. Each of the seals 68 and 69 is also shown as a rectangular sheet, however, of a size both in width and height larger than the rectangular sheets forming the MEA 16, the anode current collector 26 and the cathode current collector 27. On each of the seals 68 and 69, there is a border portion 70 between their circumferential edges and a dashed line. The border portion 70 of the anode seal 68 is adapted to engage and seal to the border portion 70 the cathode seal 69 forming an impermeable seal circumferentially thereabout. A central portion 71 of each of the seals 68 and 69 inside the border portion 70 is provided so as to suitably permit air and fuel and other materials to pass there through as between the air chamber 29 and the MEA 16 on the anode side 72 of the MEA 16 and as between the anode fuel chamber 28 and the MEA 16 on the cathode side 73 of the MEA 16. The joined border portions 70 of the seals 68 and 69 are sized to be complementary to the circumferential extent of a cell cavity 175 in the inner face 75 of the cathode end plate 15 shown on
(41) Referring to
(42) Referring to
(43) Proximate the upper end of the anode end plate 14, the fuel cavity 76 is provided. The fuel cavity 76 has a rectangular configuration having a rectangular outer wall 201, a top wall 202 a bottom wall 203, a right side wall 204 and left side wall 205. The fuel cavity 76 defines an enclosed cavity open at an opening 200 through the inner face 74 of the anode end plate 14 as seen in
(44) The anode end plate 14 carries the reservoir cavity 77 below the fuel cavity 76. The reservoir cavity 77 has an outer wall 206 and a top wall 207, bottom wall 208, left side wall 209 and a right side wall including portions 210, 211 and 212 of which portion 211 is horizontal as shown. The reservoir cavity 77 opens outwardly as an opening 214 through the inner face 74 of the anode end plate 14. A sealing bead 215 is provided in the inner face 74 of the anode end plate extending circumferentially about the opening 214 of the reservoir cavity 77. The sealing bead 215 assists in engagement with the inner face 75 of the cathode end plate 15 when the cathode end plate 15 and the anode end plate 14 are drawn together so as to provide a fluid impermeable seal therebetween. With the anode end plate 14 and the cathode end plate 15 secured together, the opening 214 of the reservoir cavity 77 is enclosed by the inner face 75 of the cathode end plate 15 is forming the reservoir 34 cavity therebetween.
(45) As can be seen in
(46) As can be seen from
(47) Reference is made to
(48) In a top wall 80 of the anode end plate 14 the upper ends of four vertically extending bores are shown.
(49) A vertical pump bore 240 extends from the top wall 80 through pump cavity 78 to the horizontal portion 210 of the side wall of the reservoir cavity 77. The vertical pump bore 240 opens at the top wall 80 as a pump bore upper opening 241. A horizontal pump bore 242 is cut from the fuel cavity 76 right side 204 horizontally to the vertical pump bore 240. A separate element, a pump bore plug 243, is engaged within the upper end of the vertical pump bore 240 after the vertical pump bore 240 is formed to sealably close the vertical pump bore 240 against fluid flow. The vertical pump bore 240 above the pump cavity 78 and the horizontal pump bore 242 form the discharge passageway 41. The vertical pump bore 240 below the pump cavity 78 forms the feed passageway 39. When the fuel pump 40 is received within the pump cavity 78, operation of the fuel pump 40 draws fluid from the reservoir cavity 77 and discharges fuel into the fuel cavity 76 by flow through the vertical pump bore 240 and the horizontal pump bore 242.
(50) A vertical drain bore 246 extends vertically downwardly from the top wall 80 through the top wall 207 into the reservoir cavity 77. The vertical drain bore 246 opens at an upper opening 248 in the top wall 80 of the anode end plate 14. A separate element, a drain bore plug 249, is received and closes the opening 248 to fluid flow after the vertical drain bore 246 is formed to sealably close the vertical drain bore 246 against fluid flow. A horizontal drain bore 247 extends from the left side wall 205 of the fuel cavity 76 horizontally into the vertical drain bore 246. The vertical drain bore 246 and the horizontal drain bore 247 define the drain passageway 37 for communication between the fuel cavity 76 and the reservoir cavity 77. The drain bore 244 is disposed laterally to the left side of the fuel cavity 76 and does not interfere with the fuel cavity 76.
(51) A vent bore 244 extends vertically downwardly from the top wall 80 through the top wall 207 into the reservoir cavity 77 providing the air vent passageway 36 therein. The vent bore 244 opens through the top wall 207 of the reservoir cavity 77 as an opening 245. The vent bore 244 is disposed laterally to the left side of the fuel cavity 76 and does not interfere with the fuel cavity 76.
(52) A supply bore 252 extends vertically downwardly from the top wall 80 through the top wall 207 into the reservoir cavity 77 providing the supply passageway 56 therein. The supply bore 252 is disposed laterally to the left side of the fuel cavity 76 and does not interfere with the fuel cavity 76. The supply bore 252 opens through the top wall 207 of the reservoir cavity 77 as an opening 254. The top wall 207 of the reservoir cavity 77 has about the opening 247 four short blind bores 255. A separate element, a sump box member 250 is shown by itself in
(53) The particular nature of the fuel level controlling inlet valve 57 is not limited and various other valve arrangements may be provided for controlling the supply of fuel from the fuel supply container 54 to the fuel reservoir 34 under gravity. It is considered preferred to provide for the fuel supply container 54 so as to provide a larger supply of fuel than the capacity of fuel reservoir 34 to increase the energy and duration that the fuel cell may operate. A separate fuel supply container 54 is not necessary and is for example not provided in the embodiment of
(54) Providing for flow of fuel from the fuel supply container 54 into the fuel reservoir 34 by gravity as controlled by the fuel level controlling inlet valve 57 shown as a mechanical valve is preferred so as to not require any expenditure of the energy generated by the fuel cell as to deliver fuel from the fuel supply container 54 to the fuel reservoir 34. Alternately, with the fuel supply container 54 above the fuel reservoir 34, an electrical solenoid valve may form the fuel level controlling inlet valve 35 as controlled by the controller and with a fuel level sensor provided within the fuel reservoir 34 to determine when fuel from the fuel supply container 54 may be permitted to flow under gravity to the fuel reservoir 34, as another alternative, a supply pump may be provided to pump fuel from the fuel supply container 54 into the fuel reservoir 34 as controlled by the controller with a fuel level sensor within the fuel reservoir 34.
(55) In an assembled fuel cell, as seen in
(56) Reference is made to
(57) The pump motor 48 is fixedly secured to the outer face 65 of the anode end plate 14 and carries an axle 198 with a coupling 100 which extends into engagement with the extension rod 180 rotate the extension rod on rotation of the motor 48.
(58) When the motor 180 rotates the driver impeller 146 clockwise in a direction of the arrow 188 shown in
(59) The particular nature of the pump motor showing is but one form of a pump which can be conveniently adapted. Rather than coupling the motor to the driven impeller via shaft that extends through the anode end plate 14 and requires a seal, a magnetic coupling may be provided. Various other motors and various other fluid pump arrangements can be provided without departing from the scope of the invention.
(60) In accordance with a preferred operation of the fuel cell 10 of the first and second embodiments the present invention, the liquid fuel is recirculated by the fuel pump 40 through the anode fuel chamber 28 and back to the fuel reservoir 34. This effectively is a closed circuit but for any additional fuel which may be supplied from the fuel supply container 54 in the second embodiment to maintain the fuel reservoir 34 substantially filled with fluid. In the second embodiment, the fuel which may be received from the fuel supply container 54 will replace fuel which may be consumed in or evaporate from the fuel cell.
Experimental Results
(61) A fuel cell as shown in
(62) In a first preferred configuration:
(63) (a) The active surface area of the air and the fuel compartment were 50 cm.sup.2 each.
(64) (b) The volume of the anode fuel chamber 28 was approximately 2 cm.sup.3.
(65) (c) The volume of the fuel reservoir 34 was approximately 2 cm.sup.3. The fuel was supplied from the fuel reservoir (approximately 2 cm.sup.3) and the spent fuel was discarded.
(66) (d) The pumping capacity of the fuel pump was approximately 1000 ml per minute. Pumping was controlled by a timer, and approximately 5 cm.sup.3 were pumped every twenty minutes.
(67) (e) The fuel cell was operated at ambient room temperatures of about 20 degrees Celsius.
(68) (f) The liquid fuel consisting of 70% by volume isopropanol and 30% by volume water was used the following operational.
(69) (g) The fuel cell was operated to produce electricity provided the open circuit potential was above approximately 380 mV.
(70) (h) The fuel cell was operated in intervals with load on for 60 seconds and load off for 60 seconds.
(71) (i) In a second series of experiments, the intervals were modified as follows: load on for 30 seconds and load off for 60 seconds.
(72) (j) The fuel cell was connected to a dc/dc converter in order to recharge a buffer battery (consisting of four NiMH cells).
(73) (k) The fuel cell was operated so as to maintain a stable battery voltage of approximately 5V.
(74) (1) This fuel cell was operated in excess of five months.
(75) (m)
(76) (n)
(77) In a second preferred configuration:
(78) (a) The active surface area of the air and the fuel compartment were 50 cm.sup.3.
(79) (b) The volume of the anode fuel chamber 28 was approximately 2 cm.sup.3.
(80) (c) The liquid fuel consisting of 70% by volume isopropanol and 30% by volume water was used the following operational.
(81) (d) The fuel was supplied from a reservoir 34 with approximately 300 cm.sup.3 volume and the spent fuel was recycled to this reservoir.
(82) (e) A feeder 57 was used to refill the reservoir 34 automatically from a fuel tank 54 with a volume of 300 cm.sup.3.
(83) (f) The pumping capacity of the fuel pump was approximately 1000 ml per minute. Pumping was controlled by a timer, and approximately 5 cm.sup.3 were pumped every ten minutes.
(84) (g) The fuel cell was operated at ambient room temperatures of about 20 degrees Celsius.
(85) (h) The fuel cell was operated to produce electricity provided the potential under load was above approximately 380 mV.
(86) (i) The fuel cell was operated in intervals with load on for 30 seconds and load off for 30 seconds.
(87) (j) The fuel cell was connected to a dc/dc converter in order to recharge a buffer battery (consisting of four NiMH cells).
(88) (k) The fuel cell was operated so as to maintain a stable battery voltage of approximately 5V.
(89) (l) This fuel cell was operated in excess of six weeks.
(90) (m)
(91) (n)
(92) Reference is made to
(93) The dispenser 300 includes a fluid container 54 and, in this regard, the fuel cell arrangement 10 in
(94) The dispenser 300 includes a housing 310 adapted to be mounted vertically as to a wall. The housing 310 includes a front plate 390 and a rear plate 391 secured together. The front plate 390 and includes a motor casing 392 which carries internally a dispensing motor 382. The motor casing 392 carries a forwardly open socket 308. The dispenser 300 has a replaceable unit 312 which comprises both the supply container 54 and a pump 320. The replaceable unit 312 is adapted to be removably coupled to the housing 310 by forward and rearward movement with the container 54 removably supported on a support shelf 332 of the front plate and the dispensing pump 320 removably engaged within the socket 308. A feed tube 340 connects the dispensing outlet 338 of the supply container 54 with the pump 320. A one-way inlet valve 336 permits flow from the container 54 to the pump 320. When the replaceable unit 312 is coupled to the housing 310, the pump 320 is operatively connected to the electrical motor 382 such that operation of the dispensing motor 382 drives the dispensing pump 320 to dispense liquid as from an outlet 344 onto a person's hand disposed underneath the outlet 344 but not shown. Below the motor casing 392, the front plate 390 carries a sensing mechanism 336 to sense the presence of a user's hand underneath the outlet 344 and to thereby as suitably controlled by the controller 47 to dispense the cleaning fluid from the container 54 onto a person's hand.
(95) Between the front plate 390 and the rear plate 391, a cavity 393 is schematically shown which extends downwardly past the lower end of the front plate 390 where the cavity 393 opens forwardly. A protective rigid wire screen 394 extends between the rear plate 391 and the front plate 390 below the front plate 390 in front of the cavity 393 to permit air flow into and out of the cavity 393. Within the cavity 393 below the front plate 390, the fuel cell arrangement 10 is provided with the anode end plate 14 fixedly secured to the rear plate 291 and carrying the cathode end plate 15 forwardly thereof. The cavity 393 is sized so as to accommodate all of the components of the fuel cell arrangement 10 providing sufficient room for the components such as those indicated in
(96) The fuel cell arrangement 10 generates electrical power which is stored in the electrical power storage device 46 and is hence used by the controller 47 to operate the dispenser 300 as by sensing the presence of a user's hand with the sensing mechanism 336 and, when a user's hand is sensed, to operate the motor 382 to dispense a predetermined dose of fluid. When fluid within the supply container 54 is exhausted, the replaceable unit 312 may be removed and replaced by another unit. In such replacement, a quick connect and disconnect arrangement may be provided between the supply tube 295 and the container outlet 55.
(97) In
(98) Reference is made to
(99) In the embodiments of
(100) The particular nature of the dispenser into which a fuel cell arrangement 10 in accordance with the present invention may be incorporated is not limited. Such fluid dispensers may serve many purposes. In the context of the dispenser being a dispenser of cleaning fluids, it is particularly advantageous if the fuel may serve a dual purpose of acting, on one hand, as a cleaning liquid for use in cleaning and, on the other hand, for use as a fuel in the fuel cell, however, this is not necessary.
(101) In accordance with the embodiments of the dispensers illustrated in
(102) In accordance with the embodiment of the dispenser illustrated in
(103) The dispenser of
(104) In accordance with the present invention, fuel within the fuel cell may be discharged from the outlet 344 of the dispenser 300 with the various mechanisms being provided for transferring of the fuel within the fuel cell back to the supply container 54, the dispensing container 316 or otherwise to the dispenser 16 for discharge out the discharge outlet 344 or the dispenser 16.
(105) In accordance with the present invention, with a fuel comprising a mixture of isopropanol and water, a reaction product of acetone will, with operation of fuel cells, come to be present with the isopropanol and water within the anode fuel chamber 28 and the fuel reservoir 34. The presence of acetone in relatively minor concentrations, for example, less than 30% by volume and, more preferably, less than 5% by volume, does not have a negative effect on a person's skin and thus can be tolerated in many applications where the dispensing fluid is to be used to clean a person's hand. Of course, when the liquid fuel is delivered from the fuel cell arrangement 10 into the dispensing fluid container 316, the acetone will be diluted with the fluid within the dispensing container 316. As well, the presence of acetone as, for example, up to 30% by volume is not detrimental for many other cleaning uses or other purposes.
(106) While the invention has been described with reference to preferred embodiments, many modifications and variations will now occur to persons skilled in the art. For a definition of the invention, reference is made to the following claims.