Membrane module mold

Abstract

A membrane module and method of making are provided, including a mold therefor. Exemplarily, the module, which comprises a membrane around which is formed a frame, is adapted for use with an electrochemical apparatus. The membrane comprises a fabric made from a synthetic fiber such as nylon, where the nylon is woven into ripstop nylon fabric. The frame, which comprises, exemplarily, high-density polyethylene (HDPE) or polypropylene, includes a wedge-shaped portion to facilitate collection of evolved gases and which provides support to the membrane as well as support to internal electrodes. The mold is adapted to suspend and secure the membrane during formation of the module and to provide a module which secures the membrane within the frame after formation of the module.

Claims

1. A process of creating a manufacture, the manufacture comprising: a frame, the frame comprising: a frame outer edge, the frame outer edge comprising a frame outer edge top portion; a ledge, the ledge in a spaced-apart relation to the frame outer edge, the ledge comprising a ledge inner edge, the ledge inner edge comprising a ledge inner edge top portion, the ledge inner edge top portion defining a gas slope, the gas slope positioned and adapted to facilitate the upward passage of evolved gas; a wedge-shaped curtain, the curtain extending from the ledge inner edge top portion and extending away from the frame outer edge top portion, the curtain comprising: a curtain top portion, the curtain top portion beginning at the ledge inner edge top portion; a curtain lower edge, the curtain lower edge thinner than the curtain top portion; and at least one curtain protrusion, the at least one curtain protrusion proximate the curtain lower edge; and an aperture, the aperture defined by: the curtain lower edge; and a portion of the ledge not including the ledge inner edge top portion; and a membrane, the membrane suspended and secured within the aperture; the process comprising the steps of: (a) placing a membrane onto at least two of a plurality of membrane hangers of a first portion mold section, the first portion mold section further comprising at least one pinch hole protrusion; (b) mating the first portion mold section with a second portion mold section, thereby creating a mold cavity, the mold cavity formed to define the frame, the second mold portion section comprising at least one pinch hole protrusion in juxtaposition to the first mold portion at least one pinch hole protrusion, thereby securing the membrane between the first portion mold section at least one pinch hole protrusion and the second portion mold section at least one pinch hole protrusion; and (c) injecting a plastic into the mold cavity, whereby the manufacture is created.

2. A process, the process comprising the steps of: (a) placing a membrane onto at least two of a plurality of membrane hangers of a first portion mold section, the first portion mold section further comprising at least one pinch hole protrusion; (b) mating the first portion mold section with a second portion mold section, thereby creating a mold cavity, the second portion mold section comprising at least one pinch hole protrusion in juxtaposition to the first mold portion at least one pinch hole protrusion, thereby securing the membrane between the first mold portion at least one pinch hole protrusion and the second mold portion at least one pinch hole protrusion; and (c) injecting plastic into the mold cavity.

3. The process of claim 2, wherein at least one of the first portion mold section and the second portion mold section further includes at least one curtain protrusion indent, whereby at least one curtain protrusion is formed.

4. The process of claim 2, wherein the mold cavity is formed to define a gas slope, whereby a gas slope is formed.

5. The process of claim 2, wherein the mold cavity is formed to define a wedge-shaped curtain, whereby a wedge-shaped curtain is formed.

Description

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWING

(1) The accompanying drawings, which are incorporated in, and constitute a part of, this specification, illustrate several embodiments consistent with the invention and, together with the description, serve to explain the principles of the invention.

(2) FIG. 1 is a block diagram illustrating a hydrogen system.

(3) FIG. 2 is a partial cutaway view illustrating an electrolyzer and associated collection towers along with enclosures.

(4) FIGS. 3 and 4 combine to give an exploded view illustrating components of an electrolyzer.

(5) FIG. 5 illustrates the detail of a channel.

(6) FIG. 6 illustrates the detail of a membrane fabric.

(7) FIG. 7 is a process diagram illustrating an electrolyzer and associated ancillary equipment and controls.

(8) FIGS. 8 and 9 are circuit diagrams illustrating monitoring and control circuits for an electrolyzer and associated ancillary equipment.

(9) FIG. 10 is a circuit diagram illustrating an oxygen sensor and associated control circuit.

(10) FIG. 11 is an exploded view of a framed electrode.

(11) FIG. 12 is an exploded view of a framed membrane.

(12) FIG. 13 is an exploded view of a membrane module and including an electrode.

(13) FIG. 14 is an enlarged view of the section noted as FIG. 14 in FIG. 13.

(14) FIG. 15 is a view of the membrane module noted as FIG. 15 in FIG. 13.

(15) FIG. 16 is an enlarged view of the section noted as FIG. 16 in FIG. 13.

(16) FIG. 17 illustrates the section of a mold used to form the portion of the membrane module noted as FIG. 17 in FIG. 13 of the membrane module of FIGS. 13-16.

(17) FIG. 18 is an enlarged view of the section noted as FIG. 18 in FIG. 17.

(18) FIG. 19 illustrates the section of a mold used to form the portion of the membrane module noted as FIG. 19 in FIG. 15 of the membrane module of FIGS. 13-16.

(19) FIG. 20 is an enlarged view of the section noted as FIG. 20 in FIG. 19.

DETAILED DESCRIPTION

(20) Referring to FIG. 1, a hydrogen system 10 includes an electrolyzer process 100 (shown also in FIGS. 2 and 7) adapted to produce hydrogen 32 from water 34 using electricity 28. The electrolyzer process 100 converts water 34 into its component parts of hydrogen 32 and oxygen 30. An electrolyte 36 is combined with the water 34 in a feedwater tank 38 and introduced into the electrolyzer process 100 as feedwater 40. Typically, the electrolyte 36 is sodium hydroxide (NaOH) or potassium hydroxide (KOH), but cations such as, but not limited to, lithium (Li.sup.+), rubidium (Rb.sup.+), potassium (K.sup.+), cesium (Cs), barium (Ba.sup.2+), strontium (Sr.sup.2+), calcium (Ca.sup.2+), sodium (Na.sup.+), and magnesium (Mg.sup.2+) may also be used. Those skilled in the relevant art will recognize that other compounds are suitable for providing an electrolyte 36 to the electrolyzer process 100. Direct current (DC) electricity 28 fed to the electrolyzer process 100 provides the necessary electricity 28 for producing hydrogen 32. Makeup water 34 is added as required. Electrolyte 36 is added as needed to maintain proper concentration.

(21) An electrical power selection and conditioning module 14 enables the hydrogen system 10 to provide DC electricity 28 from a variety of sources which are appropriately connected thereto. By way of example only, such sources include solar panels 22, wind turbines 24, batteries 26, and the conventional power grid 16, which alternating current (AC) electricity 18 may be converted to DC by an AC-DC rectifier which may be included in the power selection and conditioning module 14. It will be appreciated by those skilled in the relevant art that sources other than those shown and discussed may also provide the necessary electric power 28. Advantageously, excess power from, for example, solar panels 22 or wind turbines 24, not required to operate the electrolyzer process 100, may be fed back into the grid 16 for credit or utilized in a residence, business, or other property.

(22) As shown in FIG. 1, oxygen 30 may be vented to the atmosphere or further processed for other uses. Hydrogen 32 produced by the electrolyzer process 100 may be sent to storage 12 for further use and may be compressed (not shown) for storage at higher pressures as required. In a residential setting, for example, the hydrogen 32 may be used to fill an onboard supply vessel, for example, with a vehicle 42. Conventional stationary appliances 44 such a furnace, water heater, stove or oven, an absorption air conditioner or refrigerator, electrical generator, or fuel cell may be powered by the hydrogen 32. Finally, excess heat from the electrolyzer 102 or a hydrogen or oxygen collector 104, 106 (described more fully below) may help further reduce heat demands.

(23) The electrolyzer 102 and selected ancillary components are shown in FIG. 2. An electrolyzer 102 (described more fully below) receives water via the hydrogen collector 104 and the oxygen collector 106 (both described more fully below). The hydrogen collector 104 collects hydrogen 32 generated by the electrolyzer 102 and the oxygen collector 106 collects oxygen 30 generated by the electrolyzer 102.

(24) In an exemplary embodiment as shown in FIG. 2, the electrolyzer 102 is enclosed within a sealed electrolyzer enclosure 108 and the hydrogen and oxygen collectors 104, 106 are enclosed within a sealed collector enclosure 110. Water or other suitable heat transfer fluid may be circulated through the electrolyzer enclosure 108 and around the electrolyzer 102 as indicated by electrolyzer enclosure circulating heat transfer fluid in 112 and electrolyzer enclosure circulating heat transfer fluid out 114. The electrolyzer enclosure circulating heat transfer fluid circulating through the electrolyzer enclosure 108 may be heated by the electrolyzer 102 to, for example, 115 deg. F. and may be subsequently used for space heating or for heating hot water, especially in a residence. Air or other suitable heat transfer fluid may be circulated through the collector enclosure 110 and around the hydrogen and oxygen collectors 104, 106 as indicated by collector enclosure circulating heat transfer fluid in 116 and collector enclosure circulating heat transfer fluid out 118. The collector enclosure circulating heat transfer fluid circulating through the collector enclosure 110 is heated by the hydrogen and oxygen collectors 104, 106 to, for example, 130 deg. F. and may subsequently be used for space heating, heating hot water, or for powering an absorption air conditioner or refrigerator. In an exemplary embodiment, the electrolyzer enclosure 108 and the collector enclosure 110 are constructed with -inch high density polyethylene (HDPE) panels and appropriately sealed to contain the circulating heat transfer fluid.

(25) FIGS. 3 and 4 combine to illustrate an exemplary embodiment of a multi-cell electrolyzer 102. Going through in order, first is a stack closed end compression plate 200. In the illustrated embodiment, the stack closed end compression plate 200 has no means for allowing process streams in or out. Such connections are at the far end of the stack 102. In an exemplary embodiment, the stack closed end compression plate 200 is -inch hot-rolled steel. The stack closed end compression plate 200 may also comprise a material such as cold-rolled steel, composite, or other material with sufficient strength. The stack closed end compression plate 200 includes a plurality of stack compression bolt holes 202. In the illustrated embodiment, there are 16 stack compression bolt holes 202 which receive a like number of stack compression bolts (not shown). The stack closed end compression plate 200 cooperates with a stack open end compression plate 290 (FIG. 4) and the plurality of stack compression bolts (not shown) to hold together and compress the electrolyzer 102. Also, in an exemplary embodiment, the stack closed end compression plate 200 includes an electrical stud hole 204 to receive, and to allow for protrusion of, an electrical stud 232 attached to an anode 230. The electrical stud 232 enables electrical current to be applied to the electrolyzer 102. As will be appreciated by those skilled in the relevant art, the anode 230 and the cathode 231 (FIG. 4) may be reversed and the ancillary collection equipment modified accordingly. In the illustrated embodiment, the stack closed end compression plate 200 further includes a stack lift tongue 206 including a stack lift hole 208 for facilitating lifting and transporting the electrolyzer 102. In an exemplary embodiment, the surface of the stack closed end compression plate 200 facing the stack closed end insulator plate 220 is treated with blanchard grinding.

(26) Adjacent the stack closed end compression plate 200 is a stack closed end insulator plate 220. In an exemplary embodiment, the stack closed end insulator plate 220 is -inch HDPE. Other non-conductive materials with sufficient strength and heat resistant properties, such as low density polyethylene (LDPE), polyurethane, nylon, and ceramic materials could be satisfactory. The stack closed end insulator plate 220 includes a series of stack compression bolt holes 202. In the illustrated embodiment, there are 16 stack compression bolt holes 202 which receive a like number of stack compression bolts (not shown). Also, in an exemplary embodiment, the stack closed end insulator plate 220 includes an electrical stud hole 204 to receive, and to allow for protrusion of, the electrical stud 232 attached to the anode 230. The stack closed end insulator plate 220 may further include a set of seals (not shown) such as O-rings seated in a like set of seal grooves (not shown) formed to seal one or more water inlets 234 an oxygen outlet 236 and a hydrogen outlet 238 formed in the anode 230.

(27) Adjacent to the stack closed end insulator plate 220 is the anode 230. The anode 230 includes the electrical stud 232 attached thereto which may be threaded for ease of connection to DC electrical power. As will be appreciated by those skilled in the relevant art, the anode 230 may be connected to DC electrical power in a number of ways, including, but not limited to, one or more tabs along the side edges of the anode 230. In an exemplary embodiment, the anode 230 is constructed of 11-gauge 316 stainless steel. In the illustrated embodiment, the anode 230 includes 16 stack compression bolt holes 202 which receive a like number of stack compression bolts (not shown). As assembled, the anode 230 is placed so its electrical stud 232 protrudes through the electrical stud holes 204 formed in the stack closed end insulator plate 220 and the stack closed end compression plate 200 and is connected to DC electrical power. In an exemplary embodiment, the anode 230 is formed with an oxygen outlet 236, a hydrogen outlet 238, and one or more water inlets 234.

(28) Adjacent to the anode 230 is a first end frame 240. Shown in FIG. 3 is the anode side of the first end frame 240. In an exemplary embodiment, the first end frame 240 is HDPE. As with the insulator plates 220, 280 (FIG. 4), and the interior frames 260 (FIGS. 3 and 4), the end frames 240 could comprise LDPE, polyurethane, nylon, or ceramic material. The first end frame 240 includes a chamber aperture 248 and, in the illustrated embodiment, 16 stack compression bolt holes 202 which receive a like number of stack compression bolts (not shown). The first end frame 240 further includes at least one water inlet 234. In the illustrated embodiment, the anode side of the first end frame 240 includes at least one channel 244 formed between the at least one water inlet 234 and the chamber aperture 248 and, thus, provides fluid connectivity between the water inlet 234 and the chamber aperture 248. In the illustrated embodiment, the anode side of the first end frame 240 includes at least one channel support 246. (Shown in analogous fashion in FIG. 5.) The at least one channel support 246 helps maintain the integrity of the channel 244 when the electrolyzer 102 is under compression.

(29) The first end frame 240 further includes an oxygen outlet 236 and a hydrogen outlet 238. In the illustrated embodiment, the anode side of the first end frame 240 includes a channel 244 formed between the oxygen outlet 238 and the chamber aperture 248. In the illustrated embodiment, the anode side of the first end frame 240 includes at least one channel support 246 (FIG. 5). The reverse side of the first end frame 240, which faces, and is adjacent to, a first membrane assembly 250, is described herein below when describing a membrane assembly side of a first interior frame 260.

(30) Referring again to FIG. 3, adjacent to the first end frame is the first membrane assembly 250. In an exemplary embodiment, the first membrane assembly 250 comprises a membrane 256 and an associated membrane gasket 254. In a further exemplary embodiment, the membrane 256 is ripstop nylon with a thread count per square inch of 11892 and with a weight per square yard of about two ounces. Ripstop nylon is durable and less-expensive than alternative materials and it is resistant to chemical attack by caustic feedwater 40. In an exemplary embodiment, the nylon used in the membrane material is nylon 6,6. In a further exemplary embodiment, the nylon used in the membrane material is nylon 6. In an exemplary embodiment, the ripstop nylon membrane 256 is treated with a fluorocarbon-based water-repellent. In a further exemplary embodiment the ripstop nylon membrane 256 is not so treated. When wet, the membrane 256 enables electrons to selectively pass through. Additionally, and although not wishing to be bound by any particular theory, it is believed that the structure of the ripstop nylon material, with its interwoven ripstop reinforcement threads in a crosshatch pattern, may effect a concentration of current density and improve cell efficiency.

(31) In an exemplary embodiment, the membrane may also comprise other synthetic fabric materials. Polyamides, of which nylon is at type, also include aramids, a class of strong, heat-resistant fibers comprising aromatics.

(32) The membrane gasket 254 effects a seal of the membrane 256 when included in the electrolyzer 102. In an exemplary embodiment, the membrane gasket 254 comprises plastisol bonded to a border of the membrane 256. The plastisol may be applied via a silkscreen process. The border of one side of the membrane 256 is coated with plastisol and heated, typically in an oven, sufficiently to bond the plastisol to the membrane 256, in one exemplary embodiment, generally between about 140 deg. C. and about 170 deg. C. for between about 45 seconds and about 60 seconds. In another exemplary embodiment, about 175 deg. C. for about 90 seconds. The membrane 256 is then turned over and the border of the other side of the membrane 256 is coated with plastisol and heated as before. The bonds are complete after about 72 hours. Before treating with plastisol to form the membrane gasket 254, the original dimensions of the membrane 256 are larger to accommodate shrinkage in the heating process.

(33) The membrane gasket 254 comprises at least one water inlet 234, an oxygen outlet 236, a hydrogen outlet 238, and a series of stack compression bolt holes 202. A die punch may be used to form these holes, inlets, and outlets and may include a series of alignment jig posts (not shown). A series of alignment marks or holes 252 may be included on the membrane assembly 250 which cooperate with the die punch alignment jig posts to enable the membrane assembly 250 to be properly aligned on the die punch.

(34) Plastisols are used to print textiles and are composed primarily of polyvinyl chloride (PVC) resin, typically a white powder, and a plasticizer, typically a thick, clear liquid. Optionally, a colorant may be added. The inks must be heated to cure, generally at temperatures in the range of 140-170 deg. C., as discussed above. The porosity of the textile permits good plastisol penetration and, therefore, good adhesion of the plastisol to the textile. When used with tightly-woven ripstop nylon, however, the plastisol may be combined with a nylon binding agent such as Nylobond Bonding Agent (NYBD-9120) (Union Ink Co., Ridgefield, N.J.). In an exemplary embodiment, the ink is Ultrasoft PLUS (PLUS-6000) (Union Ink Co.) and is formulated.

(35) In a further exemplary embodiment, the plastisol is 900-series, such as 902LF, from International Coatings Co. (Cerritos, Calif.). These plastisol formulations include a premixed bonding agent catalyst. Exemplary curing is about 175 deg. C. for about 90 seconds.

(36) In an exemplary embodiment, the membrane assembly 250 is about 0.009 inches thick at the membrane gasket 254. Under compression in the electrolyzer 102, the membrane gasket 254 compresses and the membrane assembly 250 compresses to about 0.005 inches.

(37) Referring again to FIG. 3, adjacent to the first membrane assembly 250 is a first interior frame 260. Shown in FIG. 3 is the first membrane side of the first interior frame 260. In an exemplary embodiment, the first interior frame 260 is HDPE. The first interior frame includes a chamber aperture 248 and, in the illustrated embodiment, 16 stack compression bolt holes 202 which receive a like number of stack compression bolts (not shown). The first interior frame 260 also includes at least one water inlet 234, an oxygen outlet 236, and a hydrogen outlet 238.

(38) The side of the first interior frame 260 which faces an interior electrode 270 is further described herein below with the second interior frame 260. On the interior electrode side of the first interior frame 260 is an electrode ledge 272 formed around the chamber aperture 248 into which the interior electrode 270 may nest. In an exemplary embodiment, the electrode ledge 272 has a depth of one-half the thickness of the interior electrode 270. As will be appreciated by those skilled in the art, the interior electrode side of the first interior frame 260, discussed below with the second interior frame 260, and shown in detail in FIG. 4, includes a channel 244 (not shown, but illustrated analogously with the second interior frame 260 of FIG. 4), analogous to the channel 244, formed between the hydrogen outlet 238 (not shown, but illustrated analogously with the second interior frame 260 in FIG. 4) and the chamber aperture 248. The channel 244 may further include at least one channel support 246 (FIG. 5).

(39) Turning now to FIG. 4, adjacent to the first interior frame 260 is an interior electrode 270. As will be appreciated by one skilled in the relevant art, the interior electrode 270 operates as a bi-polar electrode. In an exemplary embodiment, the interior electrode 270 is sized to nest within the electrode side of each interior frame 260. In an exemplary embodiment, the interior electrode 270 is 18-gauge 316 stainless steel.

(40) Adjacent to the interior electrode 270 is a second interior frame 260. As shown in FIG. 4, the interior electrode side of the second interior frame 260 faces the interior electrode 270. In an exemplary embodiment, the second interior frame 260 is HDPE. The second interior frame 260 includes a chamber aperture 248 and, in the illustrated embodiment, 16 stack compression bolt holes 202, which receive a like number of stack compression bolts (not shown). The second interior frame 260 also includes at least one water inlet 234, and oxygen outlet 236, and a hydrogen outlet 238.

(41) The side of the second interior frame 260 which faces the interior electrode 270 includes an electrode ledge 272 formed around the chamber aperture 248 into which the interior electrode 270 may nest. In an exemplary embodiment, the electrode ledge 272 has a depth of one-half the thickness of the interior electrode 270. The interior electrode side of the second interior frame 260 includes a channel 244 formed between the oxygen outlet 236 and the chamber aperture 248. The channel 244 may further include at least one channel support 246 (FIG. 5).

(42) The side of the second interior frame 260 which is adjacent to, and faces, a second membrane assembly 250 is analogously shown in detail and described with the side facing the first membrane assembly 250 of the first interior frame 260 (FIG. 3).

(43) Adjacent to the second membrane assembly side of the second interior frame 260 is a second membrane assembly 250, which has been described herein above with the first membrane assembly 250.

(44) Adjacent to the second membrane assembly 250 is a second end frame 240. In an exemplary embodiment, the second end frame 240 is HDPE. The second end frame 240 includes a chamber aperture 248 and, in the illustrated embodiment, 16 stack compression bolt holes 202 which receive a like number of stack compression bolts (not shown). The second end frame 240 further includes at least one water inlet 234, an oxygen outlet 236, and a hydrogen outlet 238. Shown in analogous detail in FIG. 3, and as described analogously above in reference to the first end frame 240, the cathode side of the second end frame 240 further includes a channel 244 (shown in analogously in FIG. 3 and discussed above with the first end frame 240) formed between the chamber aperture 248 and the hydrogen outlet 238. Further, the channel 244 may include at least one channel support 246.

(45) Likewise, the cathode side of the second end frame 240 further includes a channel 244 formed between the chamber aperture 248 and the at least one water inlet 234. Further, this channel 244 may include at least one channel support. 246.

(46) Adjacent to the cathode side of the second end frame 240 is the cathode 231. The description of the cathode 231 is similar to that of the anode 230. The cathode 231 further includes an oxygen outlet 236, a hydrogen outlet 238, and one or more water inlets 234.

(47) Adjacent to the cathode 231, and interposed between the cathode 231 and a stack open end compression plate 290, is a stack open end insulator plate 280. While the stack open end insulator plate 280 is formed similarly to the stack closed end insulator plate 220, the stack open end insulator plate 280 further includes at least one water inlet 234, an oxygen outlet 236, and a hydrogen outlet 238. In an exemplary embodiment, the stack open end insulator plate 280 is -inch HDPE. The stack open end insulator plate 280 includes a series of stack compression bolt holes 202. In the illustrated embodiment, there are 16 stack compression bolt holes 202 which receive a like number of stack compression bolts (not shown). Also, in an exemplary embodiment, the stack open end insulator plate 280 includes an electrical stud hole 204 to receive, and to allow for protrusion of, the electrical stud 232 attached to the cathode 231. On the cathode side of the stack open end insulator plate 280 may further include a set of seals such as O-rings (not shown) seated in a like set of grooves 284 formed to seal the one or more water inlets 234, the oxygen outlet 236, and the hydrogen outlet 238 formed in the cathode 231. Likewise, a similar set of grooves 284 and seals may be included in the open end compression plate side of the open end insulator plate 280.

(48) Adjacent to the stack open end insulator plate 280 is the stack open end compression plate 290. In an exemplary embodiment, the stack open end compression plate 290 is -inch hot-rolled steel plate. The stack open end compression plate 280 may also comprise a material such as cold-rolled steel, composite, or other material with sufficient strength. In an exemplary embodiment, the surface of the stack open end compression plate 290 facing the stack open end insulator plate 280 is treated with blanchard grinding. The stack open end compression plate 290 also includes at least one water inlet 234, an oxygen outlet 236, and a hydrogen outlet 238. Along a periphery of the stack open end compression plate 290 are a plurality of stack compression bolt holes 202. In the illustrated embodiment, there are 16 stack compression bolt holes 202 which receive a like number of stack compression bolts (not shown). Also, in an exemplary embodiment, the stack open end compression plate 290 includes an electrical stud hole 204 to receive, and to allow for protrusion of, an electrical stud 232 attached to the cathode 231.

(49) The exemplary embodiment illustrated in FIGS. 3 and 4 shows one interior electrode 270. Larger capacities may be assembled by adding additional interior parts. For example, a plurality of assemblies, each assembly comprising a membrane assembly 250, a first interior frame 260, an interior electrode 270, and a second interior frame 260, may be included. As appropriate, a first end frame 240, an additional membrane assembly 250, and a second end frame 240, would be required.

(50) Although not shown, the electrolyzer 102 may be held together with a plurality of stack compression bolts spanning the electrolyzer 102 from the stack closed end compression plate 200 and the stack open end compression plate 290. Each compression bolt may be surrounded, substantially along its entire length, by a seal (not shown), which may also function as an insulator. By way of example only, such seal could be Parflex (Parflex Division, Parker-Hannifin, Ravenna, Ohio) 588N-10 non-conducting, high-pressure hose. In an exemplary embodiment, the compression bolts are torqued to 55 pounds.

(51) Turning now to FIG. 11, in an exploded view of a further exemplary embodiment, a framed electrode 270 may be provided and used in multi-cell electrolyzer. The electrode 270 is partially encased within, and formed as one with, two interior frames 320 which frames 320 may comprise HDPE. In the illustrated embodiment, the channels 244 have a depth that extends to the surface of the electrode 270. Channel supports 246 may be omitted. As illustrated in FIG. 11, one side of the framed electrode 270 may comprise a tongue 264 and the other side a coordinating groove 266 to enhance fit and seal. Multiple framed electrodes 270 could be combined with, for example, multiple framed membranes 256, described below.

(52) In a further exemplary embodiment shown in FIG. 12, a framed membrane 256 may also be provided and used in multi-cell electrolyzers 102. A membrane 256, which may not include a membrane gasket 254, is partially encased within, and formed as one with, two frames 330. As shown in FIG. 12, the membrane 256 is large enough to extend beyond the water inlets 234 and the hydrogen 238 and oxygen 236 outlets. In addition, the associated holes in the membrane 256 (shown as 234, 238, and 236, respectively) are larger than their counterparts. This enables the frame material (e.g., HDPE) to seal the holes 234, 238, and 236. In addition, where peripheral bolt holes 202 (not shown in FIG. 12) are included, such holes in the membrane 256 may also be larger. In the illustrated embodiment, the channels 244 have a depth that does not extend to the surface of the membrane. As illustrated in FIG. 12, one side of the framed membrane 256 may comprise a tongue 264 and the other side a coordinating groove 266 to enhance fit and seal.

(53) In a further exemplary embodiment, the framed membrane 256 further comprises an electrode ledge 272 (FIG. 4, shown associated with the interior frame 260, e.g.) formed therein. As constructed, then, a plurality of framed membranes 256 may be stacked with an interior electrode 270 inserted therebetween.

(54) In a further exemplary embodiment shown in FIG. 13, a membrane module 502 may also be provided and used in a multi-cell electrolyzer 102 (FIG. 3). A membrane 556, is partially encased within, and suspended within, a frame comprising a first frame portion 504 and a second frame portion 506. Although shown as a first frame portion 504 and a second frame portion 506, as one of ordinary skill in the relevant art will recognize, and as shown and described, the frame of the membrane module 502 itself may be formed, by, for example injection molding, as an integral piece. The first frame portion 504 and the second frame portion 506 may comprise HDPE, polypropylene, or other suitable material. Also shown in FIG. 13, as an aid to understanding, is an electrode 570. When assembled, an electrode 570 is held between two membrane modules 502. The electrode 570 is sized to nest in the first frame portion 504 on an electrode ledge 520. (Also seen in FIGS. 14 and 15.)

(55) The membrane module 502 may further include slots 510 to accommodate compression bolts (not shown, described herein above). The membrane module 502 also further includes water inlets 516 through which water is introduced, and gas discharge outlets 512 and 514. Regarding the gas discharge outlets 512 and 514, as will be understood by one of ordinary skill in the relevant art, when electrolyzing water, either hydrogen or oxygen will discharge from the outlets 512, 514 depending upon the applied polarity.

(56) The first frame portion 504 is formed to include at least one tongue 518 and the second frame portion 506 formed to include at least one groove 528. (FIGS. 13, 14 and 15.) Thus, when assembled, the at least one tongue 518 mates with an associated at least one groove 528 in an adjacent membrane module 502.

(57) The membrane module 502 is also formed to include a curtain 508. (Also seen in FIGS. 14 and 15.) The curtain 508 provides stability to the membrane module 502 and facilitates separation of the evolved gases, for example, hydrogen and oxygen. The curtain 508 is further formed to include protrusions 526 and 527 which, along with portions of the channel supports 546, hold the electrode 570 in a spaced-apart position from the curtain 508, thereby enabling evolved gases to travel to the gas outlets 512 and 514. (Also seen in FIG. 14.) In addition, the curtain 508 may be thinner (e.g., 0.050 inches) at a curtain edge 532 (FIG. 15) and form a wedge therefrom of, for example, 15 degrees to, for example, 0.075 inches.

(58) The membrane module 502 is formed to further include a gas slope 522. (Shown in FIG. 13, but best seen in FIG. 14, and especially FIG. 15.) The gas slope 522 inclines upward toward the gas outlet 512, for example, to facilitate passage of evolved gas to the gas outlet 512.

(59) Turning now to FIGS. 17-20, views of the mold designed to produce the membrane module 502 are shown. FIG. 17 shows a first portion mold section 580 which can be better understood by referring to the FIG. 17 indication of FIG. 13 which shows a face of the first frame portion 504. (See also, FIG. 14.) Thus, the first portion mold section 580 includes the at least one mold groove 582 which ultimately forms the at least one tongue 518 as seen in FIGS. 13 and 14.

(60) Turning now to FIG. 18, detail of the indicated portion FIG. 18 of FIG. 17 is shown. In addition to the at least one mold groove 582, FIG. 18 shows one of, exemplarily, at least one pinch hole protrusion 584, 596, and at least one curtain protrusion indent 592, 594 to produce the protrusions 527, 526 of the curtain (FIG. 14). A plurality of such protrusions 592, 594 are placed in the mold (FIG. 17).

(61) Turning now to FIG. 19, a second portion mold section 572 is shown, which can be understood by referring to the FIG. 19 indication of FIG. 15 which shows a face of the second frame portion 506. Thus, the second portion mold section 572 includes the at least one mold tongue 574 which ultimately forms the at least one groove 528 as seen in FIG. 15.

(62) Turning now to FIG. 20, detail of the indicated portion FIG. 20 of FIG. 19 is shown. In addition to the at least one mold tongue 574, FIG. 20 shows pinch hole protrusions 576, 584 and at least one curtain protrusion indent 578, 590. The at least one curtain protrusion indent 578, 590 produces the curtain protrusion (not shown, but analogous to curtain protrusions 526, 527 of FIG. 14). FIG. 20 also shows one of, exemplarily, four membrane hangers 588. The membrane hangers 588 are arranged generally at four interior corners in the second portion mold section 572. The membrane hangers 588 could, of course, be included in the first portion mold section 580. The membrane hangers 588 are situated and spaced to align with matching membrane hanger holes 530 in the membrane 556 (FIG. 16).

(63) The membrane module 502 is produced using the first portion mold section 580 and the second portion mold section 572. The membrane 556 is hung off the membrane hangers 588 by the membrane hanger holes 530 and, thus the membrane 556 is suspended in the second portion mold section 572. When so suspended, the first portion mold section 580 is mated with the second portion mold section 572, thus the membrane 556 is suspended within the mold sections 580, 572. When the first portion mold section 580 and the second portion mold section 572 are so mated, and the membrane 556 suspended, the pinch hole protrusions 584, 576, 596 pinch the membrane 556 around the periphery of the membrane 556 to hold it in place during the injection process. The pinching action of the pinch hole protrusions 584, 576, 596 thus form the membrane pinch holes 524 shown, for example, in FIG. 14.

(64) In an exemplary embodiment, interior frames 260 have a gross thickness at the borders of about 0.110 in. The thickness of the interior frame 260 along the edge of the electrode ledge is about 0.086 in. When torqued, the membrane assembly is about 0.005 in. This configuration results in an inter-electrode gap of about 0.177 in.

(65) FIG. 6 illustrates the detail of the fabric of a ripstop nylon membrane 256. As shown, the membrane 256 includes a pattern of ribs 300 comprising interwoven ripstop reinforcement threads in a crosshatch pattern with fabric planes 302 therebetween.

(66) FIG. 5 illustrates the detail of a channel 244 between an illustrative oxygen outlet 236 and an aperture 248. One or more channel supports 246 are shown which help keep the channel 244 from collapsing under the compressive load. Also shown in FIG. 5 is the electrode ledge 272 for providing fit and sealing to the interior electrode 270 (FIG. 4).

(67) Turning now to FIG. 7, shown generally is the electrolyzer process 100, the electrolyzer 102 is shown, along with the hydrogen collector 104, the oxygen collector 106, and a hydrogen expansion tank 105. Feedwater 40, which is formed from the water supply 34 and the electrolyte supply 36, is drawn from the feedwater tank 38 (FIG. 1). Feedwater 40 is supplied by a pump 126 and managed by a solenoid valve 132 which are described more fully herein below. As can be seen in FIG. 7, feedwater 40 may be balanced throughout the electrolyzer process 100 and provides feedwater 40 in the electrolyzer 102, the hydrogen collector 104, and the oxygen collector 106. The feedwater 40 enters the electrolyzer 102 through the one or more water inlet 234, shown illustratively in FIG. 7 as two water inlets 234. Feedwater 40 also provides a controlled liquid level in the hydrogen collector 104 and the oxygen collector 106, the control of which is described more fully herein below. An electrical supply 156 and power supply 134 are also provided and shown in FIG. 7. In the illustrated embodiment, 250 VDC power is supplied to the cathode 231 (not shown) and to the anode 230 (not shown) through the electrical studs 232. During operation, hydrogen 32 and oxygen 30 are withdrawn from the electrolyzer 102 through the hydrogen outlet 238 and oxygen outlet 236, respectively.

(68) The hydrogen collector 104 may include appropriate liquid level sensors and transmitters. Four such instruments are shown in FIG. 7. A water level high transmitter 136 indicates when the water level in the hydrogen collector 104 is high. A water level low transmitter 148 indicates when the water level in the hydrogen collector 104 is low. A pair of water level transmitters 140, 144 initiate turning off and on, respectively, the feedwater pump 126. As will be appreciated by those skilled in the art, the functions of these multiple level transmitters may be provided by as few as one sophisticated level transmitter. At the outlet of the hydrogen collector 104 is a hydrogen relief valve 128.

(69) The illustrative embodiment shown in FIG. 7 further includes a hydrogen expansion tank 105 downstream of the hydrogen collector 104. In an exemplary embodiment, the hydrogen expansion tank 105 helps stabilize the levels of water in the hydrogen collector 104 and the oxygen collector 106 when starting up with pressure preexisting in the hydrogen storage 12 (FIG. 1). A hydrogen expansion tank 105 having a volume of about 0.58 times the oxygen collector 106 should accomplish feedwater level stability long enough for the pressure in the electrolyzer process 100 to rise above the pressure in the hydrogen storage 12 (FIG. 1) and allow hydrogen to flow from the hydrogen collector 104 to the hydrogen storage 12 (FIG. 1). Lacking this feature, the feedwater level in the hydrogen collector 104 could drop enough to prematurely activate the feedwater pump 126 which could cause the electrolyzer process 100 to overfill with feedwater 40. In such case, as the electrolyzer process 100 becomes overfilled, as described above, when the system reaches pressure above that of the hydrogen storage 12, the water in the hydrogen collector 104 will reach the high water level fault indicator before the oxygen release valve 130 on the oxygen collector 106 is triggered by the level transmitter 150. Thus, unwanted or unnecessary shutdowns are avoided. Alternatively, the hydrogen collector 104 may be sized sufficiently larger than the oxygen collector 106.

(70) Associated with the oxygen collector 106, and downstream thereof, is an oxygen sensor 158 (e.g., Bosch 13275). The oxygen sensor 158 is used to detect, by inference, hydrogen in the oxygen 30. Of course, a second oxygen sensor 158 could be used to detect oxygen in the hydrogen 32. Also included with the oxygen collector 106 may be a pressure relief valve 172.

(71) The oxygen collector 106 may also include appropriate liquid level sensors and transmitters. Six such instruments are shown in FIG. 7. A water level high transmitter 138 indicates when the water level in the oxygen collector 106 is high. A water level low transmitter 154 indicates when the water level in the oxygen collector 106 is low. In addition, a series of sensors and transmitters control the discharge of oxygen 30 from the oxygen collector 106. In the illustrated embodiment, there are a pair of oxygen-off transmitters 142, 146 that effect the closing of an oxygen release control valve 130. In operation, when the water level in the oxygen collector 106 rises to either oxygen-off transmitter 142, 146, the oxygen release control valve 130 is closed and remains closed until the water level lowers to a point which activates either oxygen-on transmitter 150, 152 at which time the oxygen release control valve 130 is opened and remains open until the water level rises and actuates oxygen-off transmitter 142, 146 at which time the oxygen release control valve 130 is closed. During operation this cycle repeats to continuously balance the electrolyzer process 100 and remains active even if the electrolyzer process 100 is not active. As will be appreciated by those skilled in the relevant art, the functions of these multiple level transmitters may be provided by as few as one sophisticated level transmitter.

(72) Further illustrated in the exemplary embodiment shown in FIG. 7 are one or more heat transfer coils 107 which can effectively utilize excess heat. Shown in FIG. 7 is a coil 107 within each collector 104, 106 and in combination with a fan 120. A pump 124 circulates a suitable heat transfer fluid (e.g., water) through the collectors 104, 106 and the heat sink 107 associated with the fan 120. The excess heat recovered from the collectors 104, 106 may be utilized, for example, in space heating or by placing a coil 107 downstream of the air handler of a forced air furnace.

(73) Circuit Diagrams

(74) The following tables are intended to provide exemplary values for the electronic circuit elements shown in FIGS. 8-10 and described herein.

(75) Resistors ()

(76) TABLE-US-00001 R1 = 100K R2 = 100K R3 = 10 R4 = 47K R5 = 100K R6 = 100 R7 = 22K R8 = 470 R9 = 100K R10 = 100K R11 = 470 R12 = 470 R13 = 100 R14 = 100 R15 = 100K R16 = 100K R17 = 470 R18 = 47K R19 = 100K R20 = 470 R21 = 22K R22 = 100K R23 = 100K R24 = 470 R25 = 47 R26 = 100 R27 = 100K R28 = 47K R29 = 22K R30 = 470 R31 = 10 meg R32 = 100K R33 = 100K R34 = 0.001
Capacitors (f)

(77) TABLE-US-00002 C1 = 0.001 C2 = 0.001 C3 = 100 C4 = 100 C5 = 0.1 C6 = 0.001 C7 = 0.001 C8 = 0.001 C9 = 0.001 C10 = 4700 C11 = 0.001 C12 = 0.001 C13 = 0.001
Transistors (MOSFET)

(78) TABLE-US-00003 T1 = 2984 T2 = 2984 T3 = 2984 T4 = 2984 T5 = 2984 T6 = 2984 T7 = 2984 T8 = 2984 T9 = 2984 T10 = 2984
Amplifiers

(79) TABLE-US-00004 A1 = NTE A2 = NTE A3 = NTE 943 943 943
Integrated Circuits

(80) TABLE-US-00005 IC1 = 4013 IC2 = 555 IC3 = 960 IC4 = 4013 IC5 = 960 IC6 = 4013 IC7 = 4013
Diodes

(81) TABLE-US-00006 D1 = high D2 = 1N914 D3 = power D4 = H.sub.2 temperature on storage tank full D5 = 1N914 D6 = water D7 = high D8 = H2 in level fault O.sub.2 fault D9 = pump D10 = D11 = D12 = system on 1N914 1N914 warm
Switches

(82) TABLE-US-00007 S1 = control S2 = control S3 = continuous S4 = 136-H.sub.2 system off system on or water high pulsed operation S5 = 138-O.sub.2 S6 = 148-H.sub.2 S7 = 154-O.sub.2 S8 = 142-O.sub.2 water high water low water low release closed S9 = 146-O.sub.2 S10 = 150- S11 = 152- S12 = 140- release O.sub.2 release O.sub.2 release feedwater closed open open pump off S13 = 144- feedwater pump on
Contactors

(83) TABLE-US-00008 Coil K1 and Coil K2 and Coil K3 and K4 = K4- contact K1- contact K2- contact K3- over temperature energizes time delay battery saver redundancy coil K2 operates circuit pump and water input solenoid K5 = K5- K6 = K6- solid state solid state relay relay

(84) Looking first at FIG. 8, a power logic circuit 400 controls the overall control scheme. Power logic circuit 400 cooperates with the water level fault circuit 440 to shut off power if the water level becomes unbalanced. For example, if either of switches S4-S7 are closed (see, also, FIG. 7), a fault condition is indicated at D6 and a fault condition goes from fault output 442 to fault input 402. The power logic circuit 440 also cooperates with the oxygen sensor circuit 460 (FIG. 10) to shut off power if an unsafe level of hydrogen arises in the oxygen (see, also, FIG. 7). For example, if the oxygen sensor 158 detects an unsafe level of hydrogen in the oxygen, a fault condition is indicated at D8 and a fault condition goes from fault output 462 to fault input 402.

(85) An operational temperature circuit 410 monitors heat levels in the electrolyzer 102. A thermistor 174 (see, also, FIG. 7) actuates when an unsafe temperature level (e.g., 160 deg. F.) is reached. This condition is indicated by LED D1. This shuts off the power to the electrolyzer 102, which remains off until the temperature drops below the preset temperature level. Thus, the electrolyzer 102 turns on and off to keep the electrolyzer 102 within a safe temperature regime.

(86) An intermittent/pulsed operation circuit 420 provides adjustable intermittent power through a switch S3 to the electrolyzer 102 to regulate heat and to improve efficiency. This circuit also enables varying modes of operation of the electrolyzer 102. For example, the circuit may be cycled on-and-off at intervals from about one second to about two minutes or greater. This allows the hydrogen and oxygen to clear the electrodes, thereby increasing the effective surface area of the electrode. In addition, such intermittent operation assists in controlling the heat of the hydrogen generation system. In addition, the intermittent/pulsed operation circuit can enable the hydrogen system 10 to more effectively utilize power available from the wind turbine 24 (FIG. 1). An intermittent no-load condition of the wind turbine 24 allows it to gain inertia in low wind conditions. Then, when a load is applied, the kinetic energy of the spinning turbine 24 is applied to the electrolyzer 102.

(87) A pressure switch circuit 430 controls the pressure in the hydrogen storage 12 (FIG. 1) via a pressure switch 170. As long as the pressure switch 170 is closed, indicating below preset maximum pressure in the hydrogen storage 12, MOFSET T4 conducts to coils K5 and K6 which are operably connected to contacts K5 and K6 (shown in the power supply circuit 490, FIG. 9, discussed below) and power remains on. When the pressure in the hydrogen storage 12 reaches the preset maximum pressure, power to the electrolyzer 102 is shut off. Normal operation is indicated at an LED D3 and a full pressure condition in the hydrogen storage 12 is indicated at an LED D4. When the pressure in the hydrogen storage 12 drops below a preset pressure condition, indicating there is room for more hydrogen in the hydrogen storage 12, power to the electrolyzer 102 is turned back on.

(88) A water level fault circuit 440 monitors the water levels in the collection towers 104, 106 and shuts off power if the water level becomes unbalanced. The water level fault circuit 440 cooperates with the power logic circuit 400 discussed above.

(89) Associated with the pump control circuit 450a, shown in FIG. 8, is a pump control circuit 450b shown in FIG. 9. And, shown associated with the pump control circuit 450b are two switches, switch S12, which is operably connected to the water pump off level transmitter 140 on the hydrogen collector 104, and switch S13, which is operably connected to the water pump on level transmitter 144 on the hydrogen collector 104. In operation, when level transmitter 144 senses a need for feedwater 40, coil K1 is energized in the pump control circuit 450b (FIG. 9) which closes contact K1 in the pump control circuit 450a (FIG. 8). The closing of contact K1 energizes coil K2 of the pump control circuit 450a which closes contact K2 of the pump control circuit 450a, thus powering the feedwater pump 126 (FIGS. 7 and 8) and opening the feedwater solenoid valve 132 (FIG. 7). When the level transmitter 140 on the hydrogen collector 104 senses sufficient feedwater 40, coil K1 is de-energized and the feedwater pump 126 is turned off and the feedwater solenoid valve 132 is closed. Coil K2 de-energizes after a preset time and must be reset in order to be reactivated. This provides protection to the pump 126 in such case when the feedwater 40 has been turned off or is empty. It also helps prevent overfilling in the event water level transmitter 140 fails.

(90) Turning now to FIG. 10, the oxygen sensor circuit 460 interprets the voltage levels of the oxygen sensor as it correlates to the proportion of hydrogen in the oxygen. The oxygen sensor circuit 460 cooperates with the power logic circuit 400 (FIG. 8). The oxygen sensor circuit 460 will shut down the electrolyzer process 102 if the level of hydrogen in the oxygen 30 reaches unsafe levels by energizing a fault output 462 which is fed into the fault input 402 of the power logic circuit 400. An indicator LED D8 is also illuminated.

(91) A battery saver circuit 470 shown in FIG. 9 is designed to automatically disconnect a battery 476 from the control circuits, thus preventing complete discharge of the battery 476 in the event of an extended power failure. This disconnect will occur if a power interruption lasts longer than about eight hours. The battery saver circuit 470 automatically reconnects the battery 476 when power is restored. The eight hours of standby allows for cool down and release of pressure by the control circuits in case of a power failure. This helps prevent the control circuits from draining the battery 476 in the event of an extended power outage.

(92) In operation, when AC power is present, the standby transformer 472 supplies power to the rectifier diode D10 which feeds IC5. The output of IC5 then charges capacitor C10 through blocking diode D11. When charge is sufficient, the logic level MOSFET T10 conducts and energizes coil K3. This connects the battery 476 to the control circuits and a 12 VDC power supply via a normally-open contact K3. If AC power is removed, or a power outage is experienced for e.g., eight hours or other preset time, the MOSFET T10 de-energizes K3 which effectively disconnects the battery 476.

(93) A warm-up circuit 480 monitors the warm-up phase of the operation of the electrolyzer process 100 and regulates the pressure inside the electrolyzer 102. An LED D12 is illuminated when the electrolyzer process 100 reaches operational temperature. With further reference to FIG. 7, during the warm-up phase, a hydrogen relief valve 128 is opened to vent the hydrogen 32 being produced to prevent any pressure from developing until the electrolyzer 102 reaches a preset and adjustable temperature that causes the electrolyzer 102 to expand and tightens the seals to hold pressure. In the alternative, a flare system may be provided to burn hydrogen being vented. The hydrogen relief valve 128 is then closed and the hydrogen 32 is further processed, in, for example, a dryer 122 and sent to hydrogen storage 12 (FIG. 1). If power to the electrolyzer process 100 is shut down for a period of time that would be sufficient for the electrolyzer 102 to contract, the bypass valve 128 is reopened to relieve all pressure from the electrolyzer 102 to prevent damage.

(94) A power supply circuit 490 controls the main power to the electrolyzer 102. In an exemplary embodiment, a rectifier 498 converts 240 VAC to 250 VDC using two NTE6036 diodes and two NTE6037 diodes. As a redundant backup to the high temperature circuit 410 which includes thermistor 174, a thermal fuse 496, set to 180 deg. F. or whatever reform temperature of the material used in the electrolyzer 102, for example HDPE, helps protect the electrolyzer 102 from a thermal overload. If the thermal fuse 496 is tripped, a coil K4 is de-energized and two contacts K4 are opened, shutting off power to the electrolyzer 102. In addition, de-energizing coils K5 and K6 opens contacts K5 and K6 to shut off power to the electrolyzer 102. This may be effected by such conditions as a water level fault 442, the off button S1, a high temperature condition, oxygen mix, the intermittent circuit 420, or the pressure switch 170. Also shown in FIG. 9 is a fan 499 to help cool the rectifier 498 and solid state relays K5 and K6.

(95) Also shown in FIG. 9 is a water level balance circuit 500 which is operably connected to the electrolyzer process 100. Switches S8 and S9, associated with level transmitters 142 and 146, respectively, cause the oxygen release solenoid 130 (FIGS. 7 and 9) to be closed. Conversely, switches S10 and S11, associated with level transmitters 150 and 152, respectively, cause the oxygen release solenoid 130 to be open. Thus, the water level in the electrolyzer process 100 is balanced.

(96) Test Results

(97) Tests were performed on an electrolyzer having the following configuration:

(98) TABLE-US-00009 Number of Cells 111 cells Electrode 11 11 inches Size Inter-electrode 0.177 inches Feedwater 5 oz. NaOH per Gap gal. distilled water Nominal Voltage 240 VAC (converted to DC with four 85-amp diodes in a bridge configuration)

(99) Test 1

(100) TABLE-US-00010 Time 4.5 minutes Average Voltage 253.3 V Average Amperage 27.43 amps KWH 0.5211 KWH H2 Produced 4.32 scf H2 Conversion 0.0791 KWH/ cu. ft. H2 H2 KWH 0.34 KWH Efficiency 65.2 percent Equivalent

(101) Test 2

(102) TABLE-US-00011 Time 1 hour Average Voltage 240 V Average Amperage 35 amps KWH 8.4 KWH H2 Produced 66.84 scf H2 Conversion 0.0791 KWH/ cu. ft. H2 H2 KWH Equivalent 5.28 KWH Efficiency 62.9 percent

(103) Test 3

(104) TABLE-US-00012 Time 9 minutes Average Voltage 246.5 V Average Amperage 36.76 amps KWH 1.36 KWH H2 Produced 11.36 scf H2 Conversion 0.0791 KWH/ cu. ft. H2 H2 KWH Equivalent 0.90 KWH Efficiency 66.1 percent

(105) While certain preferred embodiments of the present invention have been disclosed in detail, it is to be understood that various modifications may be adopted without departing from the spirit of the invention of scope of the following claims.