Novel electrodes and methods of preparing and using same

• US 5,076,898 A
• Filed: 02/22/1989
• Issued: 12/31/1991
• Est. Priority Date: 07/28/1986
• Status: Expired due to Fees

• Current Assignee: S.E.R.E Srl
• Original Assignee: S.E.R.E Srl
• Inventors: Nidola, Antonio, Martelli, Gian N.
• Primary Examiner(s): Tung, T.
• Assistant Examiner(s): Ryser, David G.
• Application Number:
  US07/265,577
• Time in Patent Office: 1,042 Days
• Field of Search: 204/283, 204/290 R, 204/291, 204/292, 204/98, 204/128, 156/155, 264/49, 264/104, 427/77, 427/336
• US Class Current: 205/620
• CPC Class Codes: C25B 9/23 comprising ion-exchange membranes in or on which electrode material is embedded

Abstract

An electrode comprising a gas permeable and liquid permeable coating bonded to an ion exchange membrane, said coating comprising low overvoltage electrocatalytic particles, more electroconductive electrolyte resistant particles and an electrolyte resistant binder compatible with the membrane to bond the particles thereto, the electrode coating being provided with a plurality of pores with a pore size of at least 0.1 microns.

Effective porosity is imparted to the layer of particles by means of a sacrificial, pore-forming agent and by leaching out such agent after the particles have been bonded together and the layer formed is in its desired thickness, preferably after it has been deposited upon the membrane.

Surface resistivity of the layer is reduced and the layer is effectively reinforced by incorporating electroconductive particles which often have a higher overvoltage than the electrocatalytic particles and also have high electroconductivity. Silver and materials having approximately the equivalent electroconductivity of silver are incorporated for this purpose.

Claims

1. A method of generating chlorine comprising electrolyzing an aqueous alkali metal chloride in an electrolytic cell having an anode and a cathode separated by a cation exchane diaphragm which is substantially impermeable to electrolyte flow therethrough, at least the cathode thereof comprising a layer or coating of electrocatalytic particles and electroconductive particles bonded together on an ion-exchange membrane by sintering with an electrolyte-resistant, fluorinated polymeric binder, said layer or coating having relatively small pores dispersed therethrough and a plurality of relatively larger channels larger than the small pores and of 10 to 150 microns and communicating therewith, extending from the exterior of the layer or coating into the interior of the layer coating and feeding aqueous alkali metal chloride to the anode and water to the cathode.

2. The method of claim 1 wherein the electrocatalytic particles are ruthenium dioxide and the electroconductive particles are silver.

7. The process of claim 1 wherein the average diameter of the channels is at least 5 times greater than the average diameter of the pores.

3. A process for the preparation of an electrode comprising a layer or coating of electroconductive particles and electrocatalytic particles bonded together by sintering with an electrolyte-resistant, fluorinated polymeric binder, said layer or coating having relatively small pores dispersed therethrough and a plurality of coarse channels larger than said pores and communicating therewith, extending from the exterior of the layer or coating into the interior of the layer or coating comprising bonding to an ion exchange membrane a layer of low overvoltage particles, a solid leachable material and an electrolyte resistant, fluorinated polymeric binder compatible with the membrane by applying a film of an aqueous coagulum which is then dried and sintered and leaching out the solid leachable material to produce coarse channels through which catholyte may move to contact the conductive electrocatalytic particles and evolved hydrogen can escape.

4. The process of claim 3 wherein the leachable material is aluminum.

5. The process of claim 3 wherein the leachable material is a water-soluble inorganic salt.

6. The process of claim 3 wherein the pores have an average diameter of at least 0.1 micron.

8. The process of claim 3 wherein the low overvoltage particles are a mixture of ruthenium dioxide and silver particles.

9. The process of claim 3 wherein the degree of porosity is 0.5 to 1.0 micron.