US20110024303A1 - Electrolyser - Google Patents

Electrolyser Download PDF

Info

Publication number
US20110024303A1
US20110024303A1 US12/599,631 US59963108A US2011024303A1 US 20110024303 A1 US20110024303 A1 US 20110024303A1 US 59963108 A US59963108 A US 59963108A US 2011024303 A1 US2011024303 A1 US 2011024303A1
Authority
US
United States
Prior art keywords
stack
electrolyser
platen
plates
front face
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US12/599,631
Inventor
Zdenek Cerny
Francis Michael Burke
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Martinrea International Inc
Original Assignee
Martinrea International Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Martinrea International Inc filed Critical Martinrea International Inc
Assigned to MARTINREA INTERNATIONAL INC. reassignment MARTINREA INTERNATIONAL INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CERNY, ZDENEK, BURKE, FRANCIS MICHAEL
Publication of US20110024303A1 publication Critical patent/US20110024303A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/02Hydrogen or oxygen
    • C25B1/04Hydrogen or oxygen by electrolysis of water
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/05Pressure cells
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/70Assemblies comprising two or more cells
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T156/00Adhesive bonding and miscellaneous chemical manufacture
    • Y10T156/10Methods of surface bonding and/or assembly therefor

Definitions

  • This invention relates to an assembly for securing and compressing a stack electrolysis cell.
  • Electrolysis cells have long been used to generate hydrogen from water, generally in the form of an electrolyte solution.
  • porous anode and cathode plates are arranged in a stack with an electrolyte permeable-gas impermeable membrane placed between each anode and cathode pair (for example as described in PCT Publication No. WO2004/020701 and Canadian Patent Application No. 2,400,775 ELECTROLYZER, Helmke et al., both of which are incorporated herein by reference).
  • electrolyte is circulated through the porous anodes and cathodes.
  • the channels are created by cutting holes or slots in each plate that align when the plates are stacked.
  • the aligned holes and slots form the channels to circulate electrolyte and provide for output of the product gases.
  • An advantageous method of manufacturing such a cell has been to stack the anode plates, cathode plates and membranes and encase the resulting stack in an electrolyte impermeable-gas impermeable membrane such as epoxy resin.
  • the epoxy is used to assist in sealing the edges of the plates and to secure the plates in an aligned stack.
  • the resultant electrolyser may thus be comprised of multiple electrolysis cells encased in an epoxy resin casing. Ports may be provided through the epoxy casing to permit circulation of electrolyte and output of the product gases. Electricity may be provided to the cells via an electrical connection that extends out of the epoxy.
  • FIG. 1A is an exploded perspective view of a stack of electrolysis plates.
  • FIG. 1B is a perspective view of the assembled stack of electrolysis plates of FIG. 1 a.
  • FIG. 2 perspective view of an assembled electrolyser according to an embodiment of the invention.
  • FIG. 3 is a cross-sectional elevation of the electrolyser of FIG. 2 .
  • the invention provides an electrolyser comprising a stack of electrolysis plates, the plates being maintained in substantially parallel alignment, and a press for applying a compressive force transversely to the stack, to compress the stack between opposed faces of the cell, the press comprising a front face, a compression support plate fixed in position relative to the front face and spaced from the front face, a moving platen, the stack being disposed between the platen and the front face, and a compression member for applying a compressive force to the platen such that the platen applies a transverse compressive force substantially uniformly over a face of the stack, whereby the press maintains the electrolysis plates in substantially parallel alignment when the electrolyser is in operation.
  • the compression member comprises a spring bearing against the platen; the spring is actuated by a disk threadedly secured to the compression support plate and bearing against the spring; the spring is disposed in a recess disposed on a face of the platen; the spring surrounds a hub disposed in the recess; the hub surrounds a key; the front face is formed by a jacket; the front face is formed integrally with side faces of the jacket; and/or the compression support plate is affixed to the side walls.
  • the invention further provides a method of stabilising an electrolyser comprising a stack of electrolysis plates, the electrolysis plates being in substantially parallel alignment, the method comprising the steps of: a. locating the stack of electrolysis plates in a press comprising a front face and a compression support plate fixed in position relative to the front face; and b. rotating a threaded compression member to apply a compressive force to a platen bearing against the stack, such that the platen applies a transverse compressive force substantially uniformly over a face of the stack; whereby the press maintains the electrolysis plates in substantially parallel alignment when the electrolyser is in operation.
  • FIG. 1A illustrates an exploded view of a stack 10 of electrolysis plates 12 comprising alternating porous anode and cathode plates with an electrolyte permeable-gas impermeable membrane 12 a between each anode-cathode pair.
  • the electrolysis plates 12 may be assembled into the stack 10 having positive and negative terminals 11 , 13 , respectively, as illustrated in FIG. 1B , and encased in a sealant such as epoxy, a silicone compound or any other suitable sealant, to seal the edges of the plates and, in conjunction with the compression member described below, maintain the plates 12 in the stack 10 in precise parallel alignment within the electrolysis cell 20 .
  • a sealant such as epoxy, a silicone compound or any other suitable sealant
  • slots in the plates align when stacked to form channels through the stack 10 .
  • the channels permit circulation of electrolyte through the stack 10 and output of the product gases from the cell 20 .
  • a first product gas (in the case of the electrolysis cell shown, one of hydrogen and oxygen) is output from one or more first gas output ports 22
  • a second product gas (in the case of the electrolysis cell shown, the other of hydrogen and oxygen) is output from one or more second gas output ports 24
  • electrolyte is input through one or more electrolyte input ports 28
  • electrolyte is output through a set of one or more electrolyte output ports 26 , as illustrated in FIGS. 1B and 2 .
  • the placement and number of ports may vary from the embodiment illustrated in FIGS. 1B and 2 .
  • an output 29 for a thermocouple for monitoring the temperature of the electrolysis cell 20 .
  • a current supplied to electrodes 11 , 13 results in hydrogen and oxygen gas being generated in the electrolysis plates 12 of the cell 20 .
  • the generation of these product gases increases the internal pressure of the cell 20 , causing the product gases to egress through the first and second product gas ports 22 , 24 .
  • a higher electrical input may be supplied to the electrodes 11 , 13 .
  • the higher electrical input results in the product gases being generated more quickly, the internal pressure of the cell 20 increasing and a higher flow rate of product gases from product gas ports 22 , 24 .
  • the electrolysis cell 20 may be operated at higher levels of gas output, and consequent higher internal operating pressures, if a substantially even compressive force is applied to opposite faces of the cell 20 and maintained during operation.
  • the compression member accommodates thermal expansion of the encased stack 10 while under the compressive force.
  • the invention provides a press for securing the electrolyser containing the stack 10 of electrolysis plates 12 , comprising a compression plate for compressing the encased stack 10 against the jacket 30 of the cell 20 , and a disk spring 50 which can be adjusted to set a rest compression and which allows the compression plate to move as the stack 10 expands while maintaining a relatively constant pressure against the encased stack 10 as the cell 20 heats up.
  • the stack 10 is contained within a jacket 30 constructed of a sturdy, rigid material such as stainless steel, carbon fibre, plastic (for example polyetheretherketon (PEEK), PVC, CPVC), or other suitable material.
  • the jacket 30 is bent to form the front face 30 a and sides 30 b , however these may be formed as separate components if desired.
  • the electrodes 11 , 13 protrude through one end plate 30 c and another end plate 30 d seals the opposite end of the cell 20 .
  • the ends 30 c , 30 d may be bolted or otherwise suitably affixed to the front face and sides 30 a , 30 b of the jacket 30 .
  • a compression platen 32 is movably disposed opposite to the face 30 a , preferably nested within the jacket 30 as shown in FIG. 3 .
  • the compression platen 32 is similarly formed from a sturdy, rigid material and spans the length and width of the stack 10 .
  • a compression member comprising a disk spring 50 is disposed generally centrally along the platen 32 , for applying a compressive force to the stack 10 .
  • the disk spring 50 may be mounted in a recess 32 a in the outer face of the platen 32 , and surrounds a hub 52 and key 54 which interlocks with a rotatable disk 56 threadedly engaged to an opening 42 through a compression support plate 40 , the hub 52 maintaining the spring 50 in axial alignment beneath the disk 56 .
  • the compression support plate 40 is in turn bolted to the jacket 30 (as seen in FIG. 2 ).
  • the compression support plate 40 and jacket 30 thus form a press frame containing disk spring 50 in contact with moving platen 32 .
  • an elastomer layer 46 may be positioned between the stack 10 and the face 30 a of the electrolysis cell 20 , serving as a thermal insulator and allow for any imperfections between face 30 a and the facing side of the electrolysis cell 20 .
  • the elastomer layer 46 may for example be composed of Ethylene Propylene Dieene Monomer, but any suitable thermal insulating material may be used if desired.
  • the cell 20 is assembled by inserting the encased stack 10 into the jacket (after inserting a thermally insulating layer 46 , if desired), and inserting the platen 32 over the stack 10 .
  • the disk spring 50 is mounted in the recess 32 a about the hub 52 and key 54 , and the support plate 40 (with disk 56 threaded into opening 42 ) is bolted to the jacket 30 .
  • the disk 56 can be tightened to a desired torque, forcing platen 32 toward stack 10 and thus applying a uniform compression over the face of the stack 10 (the opposite face of the stack 10 bearing against the interior of face 30 a of jacket 30 , applying a uniform compression over the opposite face of the stack 10 ).
  • This manner of compression is superior to conventional compression means such as corner bolts, because a single member can be adjusted to apply even compression over the entire face of the stack.
  • corner bolts could be tightened to supply an initial uniform compression, through constant expansion and contraction the compression will eventually become non-uniform and allow the plates 12 to come out of parallel alignment. Even the slightest loss of parallel alignment between the plates 12 will result in reduced efficiency of the cell 20 , and substantial loss of parallel alignment will result in catastrophic failure of the cell 20 .
  • slots in the plates 12 form channels (not shown) through the stack 10 which permit circulation of electrolyte through the stack 10 and output of the product gases from the cell 20 .
  • a current supplied to electrodes 11 , 13 results in hydrogen and oxygen gas being generated in the electrolysis plates 12 of the cell 20 via electrolysis, as is well known.
  • the generation of the product gases increases the internal pressure of the cell 20 , causing the product gases to egress through the first and second product gas ports 22 , 24 .
  • hydrogen is output from first gas output port 22
  • oxygen is output from second gas output port 24 .
  • Electrolyte is circulated through input port 28 and output port 26 , ensuring a constant supply of electrolyte solution.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

An electrolyser comprising a stack of electrolysis plates, the plates being maintained in substantial alignment to comprise an electrolysis cell, and a press for applying a compressive force to opposed ends of the cell whereby the press maintains the electrolysis plates in substantial alignment when the electrolyser is in operation.

Description

    FIELD OF THE INVENTION
  • This invention relates to an assembly for securing and compressing a stack electrolysis cell.
  • BACKGROUND OF THE INVENTION
  • Electrolysis cells have long been used to generate hydrogen from water, generally in the form of an electrolyte solution.
  • In a particular electrolysis cell, porous anode and cathode plates are arranged in a stack with an electrolyte permeable-gas impermeable membrane placed between each anode and cathode pair (for example as described in PCT Publication No. WO2004/020701 and Canadian Patent Application No. 2,400,775 ELECTROLYZER, Helmke et al., both of which are incorporated herein by reference). By providing separate channels to each of the anodes and cathodes, the product gases generated at each of the anodes and cathodes may be separately output from the cell. Electrolyte is circulated through the porous anodes and cathodes. In order to circulate the electrolyte and provide an outlet for the product gases, the channels are created by cutting holes or slots in each plate that align when the plates are stacked. The aligned holes and slots form the channels to circulate electrolyte and provide for output of the product gases.
  • An advantageous method of manufacturing such a cell has been to stack the anode plates, cathode plates and membranes and encase the resulting stack in an electrolyte impermeable-gas impermeable membrane such as epoxy resin. The epoxy is used to assist in sealing the edges of the plates and to secure the plates in an aligned stack. The resultant electrolyser may thus be comprised of multiple electrolysis cells encased in an epoxy resin casing. Ports may be provided through the epoxy casing to permit circulation of electrolyte and output of the product gases. Electricity may be provided to the cells via an electrical connection that extends out of the epoxy.
  • While this method of creating an electrolyser from a stack of anode and cathode plates has been successful, it does suffer from some limitations. The resulting electrolysers are limited in their gas output rate as elevated internal pressures cause the epoxy to swell and allow the plates to separate. Once the plates separate, even by a relatively small amount, the channels may no longer be completely separate. Even a small breakdown in channel integrity may result in co-mingling of product gases and electrolyte, reducing output from the electrolyser.
  • It would be advantageous to provide for a stack cell and a method of manufacturing such a stack cell that alleviates these limitations.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • In drawings which illustrate embodiments of the invention by way of example only:
  • FIG. 1A is an exploded perspective view of a stack of electrolysis plates.
  • FIG. 1B is a perspective view of the assembled stack of electrolysis plates of FIG. 1 a.
  • FIG. 2 perspective view of an assembled electrolyser according to an embodiment of the invention.
  • FIG. 3 is a cross-sectional elevation of the electrolyser of FIG. 2.
  • DETAILED DESCRIPTION OF THE INVENTION
  • The invention provides an electrolyser comprising a stack of electrolysis plates, the plates being maintained in substantially parallel alignment, and a press for applying a compressive force transversely to the stack, to compress the stack between opposed faces of the cell, the press comprising a front face, a compression support plate fixed in position relative to the front face and spaced from the front face, a moving platen, the stack being disposed between the platen and the front face, and a compression member for applying a compressive force to the platen such that the platen applies a transverse compressive force substantially uniformly over a face of the stack, whereby the press maintains the electrolysis plates in substantially parallel alignment when the electrolyser is in operation.
  • In further embodiments of the electrolyser of the invention: The compression member comprises a spring bearing against the platen; the spring is actuated by a disk threadedly secured to the compression support plate and bearing against the spring; the spring is disposed in a recess disposed on a face of the platen; the spring surrounds a hub disposed in the recess; the hub surrounds a key; the front face is formed by a jacket; the front face is formed integrally with side faces of the jacket; and/or the compression support plate is affixed to the side walls.
  • The invention further provides a method of stabilising an electrolyser comprising a stack of electrolysis plates, the electrolysis plates being in substantially parallel alignment, the method comprising the steps of: a. locating the stack of electrolysis plates in a press comprising a front face and a compression support plate fixed in position relative to the front face; and b. rotating a threaded compression member to apply a compressive force to a platen bearing against the stack, such that the platen applies a transverse compressive force substantially uniformly over a face of the stack; whereby the press maintains the electrolysis plates in substantially parallel alignment when the electrolyser is in operation.
  • FIG. 1A illustrates an exploded view of a stack 10 of electrolysis plates 12 comprising alternating porous anode and cathode plates with an electrolyte permeable-gas impermeable membrane 12 a between each anode-cathode pair.
  • The electrolysis plates 12 may be assembled into the stack 10 having positive and negative terminals 11, 13, respectively, as illustrated in FIG. 1B, and encased in a sealant such as epoxy, a silicone compound or any other suitable sealant, to seal the edges of the plates and, in conjunction with the compression member described below, maintain the plates 12 in the stack 10 in precise parallel alignment within the electrolysis cell 20.
  • As more fully described in WO2004/020701 and CA2,400,775, which are incorporated herein by reference, slots in the plates align when stacked to form channels through the stack 10. The channels permit circulation of electrolyte through the stack 10 and output of the product gases from the cell 20. A first product gas (in the case of the electrolysis cell shown, one of hydrogen and oxygen) is output from one or more first gas output ports 22, a second product gas (in the case of the electrolysis cell shown, the other of hydrogen and oxygen) is output from one or more second gas output ports 24, electrolyte is input through one or more electrolyte input ports 28, and electrolyte is output through a set of one or more electrolyte output ports 26, as illustrated in FIGS. 1B and 2. As will be appreciated, the placement and number of ports may vary from the embodiment illustrated in FIGS. 1B and 2. Also shown is an output 29 for a thermocouple, for monitoring the temperature of the electrolysis cell 20.
  • During operation of the cell 20, a current supplied to electrodes 11, 13 results in hydrogen and oxygen gas being generated in the electrolysis plates 12 of the cell 20. The generation of these product gases increases the internal pressure of the cell 20, causing the product gases to egress through the first and second product gas ports 22, 24. In order to increase the gas output of the cell 20, a higher electrical input may be supplied to the electrodes 11, 13. The higher electrical input results in the product gases being generated more quickly, the internal pressure of the cell 20 increasing and a higher flow rate of product gases from product gas ports 22, 24.
  • However, the higher electrical input increases the temperature of the stack 10 with attendant increased thermal expansion of the stack 10. Any separation of the plates 12 within the stack 10 (either by spreading or by loss of parallel alignment) consequent to thermal expansion causes loss of output gases and therefore reduces the efficiency of the cell 20.
  • It has been found that the electrolysis cell 20 may be operated at higher levels of gas output, and consequent higher internal operating pressures, if a substantially even compressive force is applied to opposite faces of the cell 20 and maintained during operation. In the preferred embodiment the compression member accommodates thermal expansion of the encased stack 10 while under the compressive force.
  • In the embodiment illustrated, the invention provides a press for securing the electrolyser containing the stack 10 of electrolysis plates 12, comprising a compression plate for compressing the encased stack 10 against the jacket 30 of the cell 20, and a disk spring 50 which can be adjusted to set a rest compression and which allows the compression plate to move as the stack 10 expands while maintaining a relatively constant pressure against the encased stack 10 as the cell 20 heats up.
  • As illustrated in FIGS. 2 and 3, the stack 10 is contained within a jacket 30 constructed of a sturdy, rigid material such as stainless steel, carbon fibre, plastic (for example polyetheretherketon (PEEK), PVC, CPVC), or other suitable material. As shown the jacket 30 is bent to form the front face 30 a and sides 30 b, however these may be formed as separate components if desired. The electrodes 11, 13 protrude through one end plate 30 c and another end plate 30 d seals the opposite end of the cell 20. The ends 30 c, 30 d may be bolted or otherwise suitably affixed to the front face and sides 30 a, 30 b of the jacket 30.
  • A compression platen 32 is movably disposed opposite to the face 30 a, preferably nested within the jacket 30 as shown in FIG. 3. The compression platen 32 is similarly formed from a sturdy, rigid material and spans the length and width of the stack 10.
  • A compression member comprising a disk spring 50 is disposed generally centrally along the platen 32, for applying a compressive force to the stack 10. The disk spring 50 may be mounted in a recess 32 a in the outer face of the platen 32, and surrounds a hub 52 and key 54 which interlocks with a rotatable disk 56 threadedly engaged to an opening 42 through a compression support plate 40, the hub 52 maintaining the spring 50 in axial alignment beneath the disk 56.
  • The compression support plate 40 is in turn bolted to the jacket 30 (as seen in FIG. 2). The compression support plate 40 and jacket 30 thus form a press frame containing disk spring 50 in contact with moving platen 32.
  • Optionally an elastomer layer 46 may be positioned between the stack 10 and the face 30 a of the electrolysis cell 20, serving as a thermal insulator and allow for any imperfections between face 30 a and the facing side of the electrolysis cell 20. The elastomer layer 46 may for example be composed of Ethylene Propylene Dieene Monomer, but any suitable thermal insulating material may be used if desired.
  • The cell 20 is assembled by inserting the encased stack 10 into the jacket (after inserting a thermally insulating layer 46, if desired), and inserting the platen 32 over the stack 10. The disk spring 50 is mounted in the recess 32 a about the hub 52 and key 54, and the support plate 40 (with disk 56 threaded into opening 42) is bolted to the jacket 30.
  • After assembly of the cell 20, the disk 56 can be tightened to a desired torque, forcing platen 32 toward stack 10 and thus applying a uniform compression over the face of the stack 10 (the opposite face of the stack 10 bearing against the interior of face 30 a of jacket 30, applying a uniform compression over the opposite face of the stack 10). This manner of compression is superior to conventional compression means such as corner bolts, because a single member can be adjusted to apply even compression over the entire face of the stack. Moreover, even if corner bolts could be tightened to supply an initial uniform compression, through constant expansion and contraction the compression will eventually become non-uniform and allow the plates 12 to come out of parallel alignment. Even the slightest loss of parallel alignment between the plates 12 will result in reduced efficiency of the cell 20, and substantial loss of parallel alignment will result in catastrophic failure of the cell 20.
  • In operation, as described in WO2004/020701 and CA2,400,775, which are incorporated herein by reference, slots in the plates 12 form channels (not shown) through the stack 10 which permit circulation of electrolyte through the stack 10 and output of the product gases from the cell 20. A current supplied to electrodes 11, 13 results in hydrogen and oxygen gas being generated in the electrolysis plates 12 of the cell 20 via electrolysis, as is well known. The generation of the product gases increases the internal pressure of the cell 20, causing the product gases to egress through the first and second product gas ports 22, 24. In the case of the electrolysis cell shown, hydrogen is output from first gas output port 22, and oxygen is output from second gas output port 24. Electrolyte is circulated through input port 28 and output port 26, ensuring a constant supply of electrolyte solution.
  • Increasing the electrical input results in the product gases being generated more quickly, the internal pressure of the cell 20 increasing and a higher flow rate of product gases from product gas ports 22, 24. However, it also results in greater thermal expansion of the stack 10. As the stack 10 expands transversely (relative to the plane parallel to the plates 12) the disk spring 50 yields to maintain a substantially constant compression against the stack 10. This not only prevents misalignment of the plates 12, but also reduces the risk of cracking of the epoxy encasement material. The compression remains uniform, because the pressure from disc spring 50 is applied generally centrally to the platen 32 over the area of the disk spring 50.
  • Various embodiments of the present invention having been thus described in detail by way of example, it will be apparent to those skilled in the art that variations and modifications may be made without departing from the invention. The invention includes all such variations and modifications.

Claims (11)

1. An electrolyser, comprising
a stack of electrolysis plates, the plates being maintained in substantially parallel alignment, and
a press for applying a compressive force transversely to the stack, to compress the stack between opposed faces of the cell, the press comprising
a front face,
a compression support plate fixed in position relative to the front face and spaced from the front face,
a moving platen, the stack being disposed between the platen and the front face, and
a compression member for applying a compressive force to the platen such that the platen applies a transverse compressive force substantially uniformly over a face of the stack,
whereby the press maintains the electrolysis plates in substantially parallel alignment when the electrolyser is in operation.
2. The electrolyser of claim 1 wherein the compression member comprises a spring bearing against the platen.
3. The electrolyser of claim 2 wherein the spring is actuated by a disk threadedly secured to the compression support plate and bearing against the spring.
4. The electrolyser of claim 2 wherein the spring is disposed in a recess disposed on a face of the platen.
5. The electrolyser of claim 4 wherein the spring surrounds a hub disposed in the recess.
6. The electrolyser of claim 5 wherein the hub surrounds a key.
7. The electrolyser of claim 1 wherein the front face is formed by a jacket.
8. The electrolyser of claim 7 wherein the front face is formed integrally with side faces of the jacket.
9. The electrolyser of claim 8 wherein the compression support plate is affixed to the side walls.
10. A method of stabilising an electrolyser comprising a stack of electrolysis plates, the electrolysis plates being in substantially parallel alignment, the method comprising the steps of:
a. locating the stack of electrolysis plates in a press comprising a front face and a compression support plate fixed in position relative to the front face; and
b. rotating a threaded compression member to apply a compressive force to a platen bearing against the stack, such that the platen applies a transverse compressive force substantially uniformly over a face of the stack;
whereby the press maintains the electrolysis plates in substantially parallel alignment when the electrolyser is in operation.
11. The method of claim 10 wherein in step b. the compressive force is applied to the platen generally centrally.
US12/599,631 2007-05-10 2008-05-09 Electrolyser Abandoned US20110024303A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CAPCT/CA2007/000837 2007-05-10
PCT/CA2007/000837 WO2008138096A1 (en) 2007-05-10 2007-05-10 Electrolyser
PCT/CA2008/000902 WO2008138125A1 (en) 2007-05-10 2008-05-09 Electrolyser

Publications (1)

Publication Number Publication Date
US20110024303A1 true US20110024303A1 (en) 2011-02-03

Family

ID=40001618

Family Applications (2)

Application Number Title Priority Date Filing Date
US12/599,535 Abandoned US20110094892A1 (en) 2007-05-10 2007-05-10 Electrolyser
US12/599,631 Abandoned US20110024303A1 (en) 2007-05-10 2008-05-09 Electrolyser

Family Applications Before (1)

Application Number Title Priority Date Filing Date
US12/599,535 Abandoned US20110094892A1 (en) 2007-05-10 2007-05-10 Electrolyser

Country Status (4)

Country Link
US (2) US20110094892A1 (en)
EP (2) EP2150638A4 (en)
CA (1) CA2723668A1 (en)
WO (2) WO2008138096A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014138856A1 (en) 2013-03-12 2014-09-18 Next Hydrogen Corporation End pressure plate for electrolysers
JP2018080505A (en) * 2016-11-16 2018-05-24 トヨタ車体株式会社 Vehicle control unit

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102009021506A1 (en) * 2009-05-15 2011-01-13 Culture, James, Colorado Springs Method and device for producing a hydrogen-containing gas mixture

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3743544A (en) * 1970-12-16 1973-07-03 United Aircraft Corp Fuel cell
US4891117A (en) * 1988-07-15 1990-01-02 The Dow Chemical Company Method and apparatus for installing gasket members between flat plate structures

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2012046A (en) * 1930-01-31 1935-08-20 Nat Aniline & Chem Co Inc Electrolytic process and apparatus
US3287251A (en) 1962-04-02 1966-11-22 Horne Bi-polar electrochemical cell
US4107023A (en) 1976-07-09 1978-08-15 Hooker Chemicals & Plastics Corporation Filter press halate cell
ZA815034B (en) * 1981-02-02 1982-08-25 Olin Corp Method for assembling membrane electrolytic cells
US4430179A (en) * 1981-08-03 1984-02-07 Olin Corporation Portable method for filter press cell assembly
GB8626010D0 (en) 1986-10-30 1986-12-03 Ici Plc Assembling filter press type structure
US4846951A (en) * 1988-07-15 1989-07-11 The Dow Chemical Company Process and apparatus for controlling gasket force in electrolysis cells
GB9526577D0 (en) * 1995-12-28 1996-02-28 Nat Power Plc Method for the fabrication of electrochemical cells
US6040072A (en) * 1997-11-19 2000-03-21 Lynntech, Inc. Apparatus and method for compressing a stack of electrochemical cells
US6210823B1 (en) * 1998-08-19 2001-04-03 Matsushita Electric Industrial Co. Ltd. Polymer electrolyte fuel cell
CA2256987C (en) * 1998-12-23 2003-01-07 Peter Ling Terminal seal for electrolytic devices
CA2342320A1 (en) * 1999-07-01 2001-01-11 Squirrel Holdings Ltd. Membrane-separated, bipolar multicell electrochemical reactor
CA2333859A1 (en) 2001-02-01 2002-08-01 Donald W. Kirk Electrochemical cell stacks
JP4153702B2 (en) * 2002-01-30 2008-09-24 本田技研工業株式会社 Resin-metal joint for sealing
US7688764B2 (en) 2002-06-20 2010-03-30 Motorola, Inc. Method and apparatus for speaker arbitration in a multi-participant communication session
CA2400775C (en) 2002-08-28 2010-12-07 Fatpower Inc. Electrolyzer
US20040046526A1 (en) * 2002-09-06 2004-03-11 Richards William R. Modular fuel cell
JP4639583B2 (en) * 2003-03-06 2011-02-23 トヨタ自動車株式会社 Fuel cell
JP2005001910A (en) * 2003-06-10 2005-01-06 Taiheiyo Cement Corp Method for converting incinerated ash into cement raw material
US7416807B2 (en) * 2003-08-01 2008-08-26 Matsushita Electric Industrial Co., Ltd. Polymer electrolyte fuel cell
JP4174022B2 (en) * 2003-10-20 2008-10-29 本田技研工業株式会社 Fuel cell stack
US20050095485A1 (en) * 2003-10-31 2005-05-05 3M Innovative Properties Company Fuel cell end plate assembly
US20060093890A1 (en) * 2004-10-29 2006-05-04 Steinbroner Matthew P Fuel cell stack compression systems, and fuel cell stacks and fuel cell systems incorporating the same
JP2006316288A (en) * 2005-05-10 2006-11-24 Honda Motor Co Ltd High-pressure hydrogen production apparatus
JP5040043B2 (en) * 2006-06-20 2012-10-03 トヨタ自動車株式会社 Fuel cell

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3743544A (en) * 1970-12-16 1973-07-03 United Aircraft Corp Fuel cell
US4891117A (en) * 1988-07-15 1990-01-02 The Dow Chemical Company Method and apparatus for installing gasket members between flat plate structures

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014138856A1 (en) 2013-03-12 2014-09-18 Next Hydrogen Corporation End pressure plate for electrolysers
US9404190B2 (en) 2013-03-12 2016-08-02 Next Hydrogen Corporation End pressure plate for electrolysers
US10041178B2 (en) 2013-03-12 2018-08-07 Next Hydrogen Corporation End pressure plate for electrolysers
JP2018080505A (en) * 2016-11-16 2018-05-24 トヨタ車体株式会社 Vehicle control unit

Also Published As

Publication number Publication date
WO2008138125A1 (en) 2008-11-20
EP2155930A1 (en) 2010-02-24
CA2723668A1 (en) 2008-11-20
EP2150638A4 (en) 2011-08-31
US20110094892A1 (en) 2011-04-28
EP2155930A4 (en) 2010-10-13
WO2008138096A1 (en) 2008-11-20
EP2150638A1 (en) 2010-02-10

Similar Documents

Publication Publication Date Title
US6607858B2 (en) Electrochemical fuel cell stack with improved reactant manifolding and sealing
US6599653B1 (en) Molded fuel cell plates with seals
JP4597800B2 (en) High pressure hydrogen production equipment
RU2545508C2 (en) Compression device for fuel or electrolytic cells in fuel-cell battery or electrolytic-cell battery
JP5615379B2 (en) Energy converters, especially fuel cell stacks or electrolysers
WO2001023644A1 (en) Water-electrolysis-device-use electrode plate, electrode plate unit, solid electrolytic membrane unit and electrolytic cell
JP2015504116A (en) Electrolytic cell
DK181123B1 (en) An electrolysis system
US8097375B2 (en) Procedure for filling a fuel cell anode supply manifold with hydrogen for start-up
EP3543376A1 (en) Cooling plate assembly and an electrolyser stack comprising the same
US8722271B2 (en) Flow field plate with relief ducts for fuel cell stack
US8709220B2 (en) Water electrolysis apparatus
JPH08167424A (en) Solid high polymer electrolyte fuel cell
KR20170045248A (en) Seal designs for multicomponent bipolar plates of an electrochemical cell
JP2006070322A (en) High pressure hydrogen production device
JP4494975B2 (en) Fuel cell stack
US20110024303A1 (en) Electrolyser
US20110180398A1 (en) Water electrolysis apparatus
JP2006328527A (en) Apparatus for producing hydrogen
JP2003160891A (en) Clamping device in solid polymer type water electrolytic cell
US10041178B2 (en) End pressure plate for electrolysers
JP2004253269A (en) Polymer electrolyte fuel cell and its operating method
CA2723669A1 (en) Electrolyser
US20040247981A1 (en) Molded fuel cell plates with seals
JP6096753B2 (en) Fuel cell stack

Legal Events

Date Code Title Description
AS Assignment

Owner name: MARTINREA INTERNATIONAL INC., CANADA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:CERNY, ZDENEK;BURKE, FRANCIS MICHAEL;SIGNING DATES FROM 20101014 TO 20101018;REEL/FRAME:025183/0810

AS Assignment

Owner name: AVON PRODUCTS, INC., NEW YORK

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SANTHANAM, UMA;HONG, QI;YIM, SUNGHAN;REEL/FRAME:028885/0855

Effective date: 20120830

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION