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US4295953A Expired / Lapsed US ⏱️ 0.0 years remaining

Filter press type ion exchange membrane-method electrolysis cell

Assignee: ThyssenKrupp Nucera Japan Ltd
•
Filing: 1980-01-02
•
Granted: 1981-10-20
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Expires: 2000-01-02
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Abstract

Abstract A filter-press type ion exchange membrane-method electrolysis cell comprising (a) an anode structure which comprises a rectangular anode frame including a top element, a bottom element and two side elements and anode plates welded to the anode frame, (b) a cathode structure which comprises a rectangular cathode frame including a top element, a bottom element and two side elements and cathode plates welded to the cathode frame, and (c) an ion exchange membrane interposed between the anode structure and the cathode structure; wherein the two side elements of the anode frame and the two side elements of the cathode frame have a tubular structure with a rectangular cross section, the top and bottom elements of the anode frame and the top and bottom elements of the cathode frame have a .].-shaped cross section, and are secured such that their open portions face the inside of an anode compartment and a cathode compartment, respectively, and at least one end of the top element of the anode frame communicates with the top end of the side element of the anode frame and at least one end of the top element of the cathode frame communicates with the top end of the side element of the cathode frame so that the side element communicating with the top element of the anode frame, and the side element communicating with the top element of the cathode frame form conduits for withdrawing gas and solution flowing from the anode compartment and the cathode compartment, respectively, (d) a current disperser surrounding an anode lead bar welded to anode plates within the anode structure and a current disperser surrounding a cathode lead bar welded to cathode plates within the cathode structure, whereby a region not permitting passage of gas is formed between the periphery of the anode lead bar and the inside of the current disperser welded to the anode plates and between the periphery of the cathode lead bar and the inside of the current disperser welded to the cathode plates, thus serving as a passage for a downwardly moving stream of electrolytic solution, and (e) a pipe for supplying an anolyte solution disposed within the anode compartment and a pipe for supplying a catholyte solution disposed within the cathode compartment.

Inventors

  • 👤 Shigeaki Fuseya
  • 👤 Teruo Ichisaka

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 09:12
CPC Classifications
C; C25; C25B; C25B9/00; C25B9/70; C25B9/73; C25B9/77; C25B9/60; C25B9/65

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 374 words
A filter-press type ion exchange membrane-method electrolysis cell comprising (a) an anode structure which comprises a rectangular anode frame including a top element, a bottom element and two side elements and anode plates welded to the anode frame, (b) a cathode structure which comprises a rectangular cathode frame including a top element, a bottom element and two side elements and cathode plates welded to the cathode frame, and (c) an ion exchange membrane interposed between the anode structure and the cathode structure; wherein the two side elements of the anode frame and the two side elements of the cathode frame have a tubular structure with a rectangular cross section, the top and bottom elements of the anode frame and the top and bottom elements of the cathode frame have a .].-shaped cross section, and are secured such that their open portions face the inside of an anode compartment and a cathode compartment, respectively, and at least one end of the top element of the anode frame communicates with the top end of the side element of the anode frame and at least one end of the top element of the cathode frame communicates with the top end of the side element of the cathode frame so that the side element communicating with the top element of the anode frame, and the side element communicating with the top element of the cathode frame form conduits for withdrawing gas and solution flowing from the anode compartment and the cathode compartment, respectively, (d) a current disperser surrounding an anode lead bar welded to anode plates within the anode structure and a current disperser surrounding a cathode lead bar welded to cathode plates within the cathode structure, whereby a region not permitting passage of gas is formed between the periphery of the anode lead bar and the inside of the current disperser welded to the anode plates and between the periphery of the cathode lead bar and the inside of the current disperser welded to the cathode plates, thus serving as a passage for a downwardly moving stream of electrolytic solution, and (e) a pipe for supplying an anolyte solution disposed within the anode compartment and a pipe for supplying a catholyte solution disposed within the cathode compartment.
Claim 2
Dependent Claim 374 words
A filter-press type ion exchange membrane-method electrolysis cell comprising (a) an anode structure which comprises a rectangular anode frame including a top element, a bottom element and two side elements and anode plates welded to the anode frame, (b) a cathode structure which comprises a rectangular cathode frame including a top element, a bottom element and two side elements and cathode plates welded to the cathode frame, and (c) an ion exchange membrane interposed between the anode structure and the cathode structure; wherein the two side elements of the anode frame and the two side elements of the cathode frame have a tubular structure with a rectangular cross section, the top and bottom elements of the anode frame and the top and bottom elements of the cathode frame have a .].-shaped cross section, and are secured such that their open portions face the inside of an anode compartment and a cathode compartment, respectively, and at least one end of the top element of the anode frame communicates with the top end of the side element of the anode frame and at least one end of the top element of the cathode frame communicates with the top end of the side element of the cathode frame so that the side element communicating with the top element of the anode frame, and the side element communicating with the top element of the cathode frame form conduits for withdrawing gas and solution flowing from the anode compartment and the cathode compartment, respectively, (d) a current disperser surrounding an anode lead bar welded to anode plates within the anode structure and a current disperser surrounding a cathode lead bar welded to cathode plates within the cathode structure, whereby a region not permitting passage of gas is formed between the periphery of the anode lead bar and the inside of the current disperser welded to the anode plates and between the periphery of the cathode lead bar and the inside of the current disperser welded to the cathode plates, thus serving as a passage for a downwardly moving stream of electrolytic solution, and (e) a pipe for supplying an anolyte solution disposed within the anode compartment and a pipe for supplying a catholyte solution disposed within the cathode compartment.
Claim 3
Dependent Claim 139 words
The electrolysis cell as set forth in claim 1, wherein one of the side elements of the anode frame is a pipe for withdrawing gas and solution flowing from the anode compartment and the other side element of the anode frame is a closed pipe; one of the side elements of the cathode frame is a pipe for withdrawing gas and solution flowing from the cathode compartment and the other side element of the cathode frame is a closed pipe; and the anode structure and the cathode structure are arranged such that the side element as a withdrawal pipe of the anode frame adjoins the side element as a closed pipe of the cathode frame, and the side element as a withdrawal pipe of the cathode frame adjoins the side element as a closed pipe of the anode frame.

References Cited (Backward Citations)

US1368206A Cited
US2161166A Cited
US4111779A Cited
US4149952A Cited
US4069128A Cited
DE2821984A1 Cited
GB2023181A Cited
US4211627A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-10-19 1985-04-20 1985-10-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-10-19 1989-04-20 1989-10-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-10-19 1993-04-20 1993-10-20 $7700.00 Window Closed / Lapsed

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