IP Library Granted Patent US 8,197,649
Granted Patent B2
US 8,197,649 · App. 11/914,668 · Granted Jun 12, 2012

Ion exchange membrane electrolytic cell

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Quick Facts
Patent No.
US 8,197,649
App. No.
11/914,668
Granted
Jun 12, 2012
Kind
B2
Abstract

[Problems] The liquid pressure of an anode chamber in a two-chamber ion exchange membrane electrolytic cell using a gas diffusion electrode are different among one another depending on depths so that the liquid pressures are applied on an anode or an ion exchange membrane, thereby introducing damage or deformation of the elements. [Means for Solving] A cushion material 10 is accommodated between a cathode gas chamber back plate 9 and a gas diffusion electrode 7 of an ion exchange membrane electrolytic cell 1 such that a repulsive force of the cushion material at the bottom part of the cathode gas chamber is larger than that at the top part. The excessive pressure applied to an ion exchange membrane is suppressed to prevent the generation of scratches or the like by decreasing the repulsive force of the cushion material toward the top in accordance with a differential pressure between an anode chamber pressure and a cathode gas chamber pressure.

Claims (14)

1. An ion exchange membrane electrolytic cell comprising an anode chamber accommodating an anode and a cathode gas chamber accommodating a gas diffusion electrode, the anode and the cathode gas chamber being divided by an ion exchange membrane wherein

a metallic cushion is accommodated under compression between a back plate of the cathode gas chamber and the gas diffusion electrode such that a repulsive force of the metallic cushion at a bottom part of the cathode gas chamber is larger than that at a top part of the cathode gas chamber; and wherein the repulsive force at respective points in a longitudinal direction of the metallic cushion is larger than the pressure difference between the anode chamber liquid pressure and the cathode gas chamber pressure, and the excess of the repulsive force over the pressure difference, during operation of the electrolytic cell, is a minimum of 1 kPa and a maximum of 7.2 kPa.

2. The electrolytic cell as claimed in claim 1 , wherein the metallic cushion is in a form of a coil.

3. The electrolytic cell as claimed in claim 2 , wherein installation density of the coiled metallic cushion accommodated under compression in an upper part of the cathode gas chamber is smaller than the installation density of the coiled metallic cushion accommodated under compression in a lower part of the cathode gas chamber.

4. The electrolytic cell as claimed in claim 2 , wherein a diameter of the coiled metallic cushion accommodated under compression in an upper part of the cathode gas chamber is smaller than the diameter of the coiled metallic cushion accommodated under compression in a lower part of the cathode gas chamber.

5. The electrolytic cell as claimed in claim 1 , wherein the metallic cushion is a wavy mat.

6. The electrolytic cell as claimed in claim 5 , wherein the number of stacked metallic cushion mats accommodated under compression in an upper part of the cathode gas chamber is smaller than the number of stacked metallic cushion mats accommodated under compression in a lower part of the cathode gas chamber.

7. The electrolytic cell as claimed in claim 5 , wherein a diameter of the metallic cushion mat accommodated under compression in an upper part of the cathode gas chamber is smaller than the diameter of the coiled metallic cushion mat accommodated under compression in a lower part of the cathode gas chamber.

8. The electrolytic cell as claimed in claim 1 , wherein the metallic cushion is made of Ni or high Ni alloy.

9. The electrolytic cell as claimed in claim 1 , wherein a maximum of the excess of the repulsive force over the pressure difference is 7 kPa.

10. The electrolytic cell as claimed in claim 1 , wherein a minimum of the excess of the repulsive force over the pressure difference is 1.6 kPa.

11. A method of producing caustic soda comprising a step of introducing into the electrolytic cell claimed in claim 1 reagents to produce caustic soda.

12. A method of producing chlorine comprising a step of introducing into the electrolytic cell claimed in claim 1 reagents to produce chlorine.

13. A method of producing caustic soda and chlorine comprising a step of introducing into the electrolytic cell claimed in claim 1 reagents to produce caustic soda and chlorine.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 19, 2017
From: CHLORINE ENGINEERS CORP., LTD.
To: TOAGOSEI CO., LTD.
Reel/Frame 041012/0351 →
CHANGE OF ADDRESS Recorded Jan 15, 2014
From: KANEKA CORPORATION
To: KANEKA CORPORATION
Reel/Frame 032019/0901 →
CHANGE OF ADDRESS Recorded Oct 3, 2012
From: CHLORINE ENGINEERS CORP., LTD.
To: CHLORINE ENGINEERS CORP., LTD.
Reel/Frame 029074/0353 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 16, 2007
From: SAIKI, KOJI; ASAUMI, KIYOHITO; HAMAMORI, MITSUHARU; OSAKABE, TSUGIYOSHI
To: CHLORINE ENGINEERS CORP., LTD.; KANEKA CORPORATION; TOAGOSEI CO., LTD.
Reel/Frame 020127/0310 →