Composite regenerable adsorption carbon material and its regeneration method

• US 6,391,185 B1
• Filed: 09/22/2000
• Issued: 05/21/2002
• Est. Priority Date: 01/05/2000
• Status: Expired due to Fees

• Current Assignee: Electrophor Inc.
• Original Assignee: Electrophor Inc.
• Inventors: Shvarev, Alexey E., Mitilineos, Alexander G., Pimenov, Alexander V., Shmidt, Joseph L.
• Primary Examiner(s): Phasge, Arun S.
• Application Number:
  US09/667,846
• Time in Patent Office: 606 Days
• Field of Search: 205/687, 205/768
• US Class Current: 205/687
• CPC Class Codes: B01J 20/20 comprising free carbon; comprising carbon obtained by carbonising processes
• CPC Class Codes: B01J 20/3416 of sorbents or filter aids comprising free carbon, e.g. activated carbon
• CPC Class Codes: B01J 20/3441 Regeneration or reactivation by electric current, ultrasound or irradiation, e.g. electromagnetic radiation such as X-rays, UV, light, microwaves

Abstract

The present process provides improved means for adsorbing components and for regeneration of a composite adsorption carbon material (CRAC) used for effecting the desired separation using an electrochemical process under conditions wherein the specific volumetric electric conductivity of the CRAC differs from that of the electrolyte employed by not more than one order of magnitude, a specific current density of at least 0.01 ampere per gram of CRAC is employed, and a high degree of regeneration of CRAC from polar and non-polar substances and heavy metal ions is obtained, as well as improved adsorption.

Claims

1. A method for regeneration of a composite porous matrix comprised of a regenerable adsorption carbon material (CRAC) which has adsorbed therein substances to be separated therefrom, comprising permeating said porous matrix with an electrolytic solution, and applying an electric current to said electrolytic solution, wherein the specific volumetric electric conductivity of said porous matrix differs from the specific volumetric electric conductivity of the electrolytic solution by not more than one order of magnitude, and wherein electric current is passed through the surface of the carbon-electrolyte solution interface at a specific current density of at least 0.01 ampere per gram of adsorption carbon.

2. The method of claim 1 wherein said composite porous matrix has a specific volume electric conductivity of 1 to 100 (Ohm.m)¹.

3. The method of claim 2 wherein the specific volumetric electric conductivity of said adsorption carbon material is from 0.2 to 5 times the specific volumetric electric conductivity of said electrolytic solution.

4. The method of claim 2 wherein the specific current density of said electric current is at least 0.05 ampere per gram of said composite adsorption carbon material.

5. The method of claim 2 wherein said electrolytic solution is pumped through said composite porous matrix in the course of the regeneration process in order to remove desorbed impurities.

6. The method of claim 5 wherein said electrolytic solution is substantially continuously pumped through said composite porous matrix in the course of the regeneration process.

7. The method of claim 2 wherein the adsorbed substances that are removed from said composite porous matrix during regeneration are selected from the group consisting of nonpolar organic matter, polar organic matter, ionic organic matter, biological organic matter, and ions of heavy metals.

8. The method of claim 1 wherein the procedure restores the ability of said composite adsorption carbon material to adsorb active chlorine.

9. The method of claim 1 wherein the electric current passed through the composite porous matrix is a direct cathodic or anodic current.

10. The method of claim 9 wherein the passage of said electric current takes place in at least two stages with changing polarity.

11. The method of claim 1 wherein said carbon material comprises a porous matrix of activated carbon fibers which have an average fiber length of at least about 1 mm, and which have diameters of 1-30 microns.