US2004069621A1PendingUtilityA1

Electrochemicall cell

Assignee: BAYER AGPriority: Jul 31, 2002Filed: Jul 9, 2003Published: Apr 15, 2004
Est. expiryJul 31, 2022(expired)· nominal 20-yr term from priority
C25B 11/03
42
PatentIndex Score
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Claims

Abstract

The present invention relates to an electrochemical cell suitable for a membrane electrolysis process, comprising (i) at least one anode compartment having a metal electrode, (ii) a cathode compartment having a gas diffusion electrode (iii) and an ion exchange membrane arranged between the anode compartment and the cathode compartment. The metal electrode that functions as an anode is capable of being dipped into an electrolyte during use and is provided with one or more orifices for the passage of gas formed during operation. The metal electrode can optionally be angled and/or curved, and the orifices preferably have guide structures that conduct the gas formed to a side of the metal electrode that faces away from the cathode. The present invention also relates to electrodes per se as well as methods for use of electrodes and electrochemical cells.

Claims

exact text as granted — not AI-modified
What is claimed is:  
     
         1 . An electrochemical cell suitable for use in a membrane electrolysis process, comprising; 
 at least one anode compartment having a metal electrode capable of functioning as an anode;    a cathode compartment having a gas diffusion electrode capable of functioning as a cathode and;    an ion exchange membrane arranged between said anode compartment and said cathode compartment, wherein the metal electrode has at least one orifice for the passage of the gas formed during operation and said metal electrode optionally being angled and/or curved, and further wherein one or more of the orifices are provided with a guide structure which is capable of conducting gas formed to a side of the metal electrode facing away from said cathode compartment.    
     
     
         2 . An electrochemical cell according to  claim 1 , wherein the total cross-sectional area of the orifices is in the range from 20% to 70% of the area which is formed by the height and width of the metal electrode.  
     
     
         3 . An electrochemical cell according to  claim 1 , wherein the metal electrode has a corrugated, zigzag-shaped or rectangular cross section.  
     
     
         4 . An electrochemical cell according to  claim 3 , wherein the metal electrode has a depth of at least 1 mm.  
     
     
         5 . An electrochemical cell according, to  claim 1 , wherein the metal electrode comprises two expanded metals adjacent to one another, wherein one expanded metal faces the cathode compartment and is more finely structured than a second expanded metal facing away from the cathode compartment, the more finely structured expanded metal being rolled flat and the second expanded metal being arranged such that mesh webs thereof are inclined in a direction of the cathode compartment and serve as said guide structures.  
     
     
         6 . A metal electrode comprising: 
 at least one orifice that is provided with a guide, said guide being capable of conducting gas away from said metal electrode.    
     
     
         7 . An electrode as claimed in  claim 6 , wherein said metal electrode is angled and/or curved.  
     
     
         8 . An electrode according to  claim 6 , wherein the total cross-sectional area of all orifices provided in said electrode is in the range from 20% to 70% of the area which is formed by the height and width of the metal electrode.  
     
     
         9 . An electrode according to  claim 6 , wherein the metal electrode has a corrugated, zigzag-shaped or rectangular cross section.  
     
     
         10 . An electrode according to  claim 6 , wherein the metal electrode has a depth of at least 1 mm.  
     
     
         11 . An electrode according to  claim 6 , wherein the metal electrode comprises two expanded metals adjacent to one another, wherein one of said expanded metals is more finely structured than the second expanded metal, the more finely structured expanded metal being rolled flat and the second expanded metal being arranged such that mesh webs thereof are inclined and serve as said guide.  
     
     
         12 . An electrochemical cell comprising a metal electrode as claimed in  claim 6 .  
     
     
         13 . A method for conducting an electrolysis operation comprising employing an electrode according to  claim 6 .  
     
     
         14 . A method for conducting an electrolysis operation comprising employing an electrochemical cell according to  claim 12 .  
     
     
         15 . A method for conducting an electrolysis operation comprising employing an electrochemical cell according to  claim 1 .  
     
     
         16 . An electrochemical cell according to  claim 12 , comprising an anode of a titanium-palladium alloy and a cathode based on carbon.  
     
     
         17 . A method for reducing the voltage required in the electrolysis of aqueous solutions of hydrogen chloride comprising employing an electrode according to  claim 6 .  
     
     
         18 . A method for reducing the voltage required in the electrolysis of aqueous solutions of hydrogen chloride comprising employing an electrochemical cell according to  claim 12 .  
     
     
         19 . A method for carrying out the electrolysis of an aqueous solution of hydrogen chloride comprising employing an anode comprising a combination of at least two expanded metals, one of said expanded metals being more finely structured than the other of said expanded metals.  
     
     
         20 . A method according to  claim 19 , wherein said method permits use of a voltage of less than 1.67 V when a current density of 5 kA/m 2  is employed.

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