# US 4,400,250 A · Adsorption onto charcoal cloth > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 4,400,250 A - Document ID: US4400250A - Status: Granted - Kind: A - Application number: 06/285,521 - Filed: 1981-07-21 - Granted: 1983-08-23 - Earliest claimed: 1980-07-24 - Assignees: The Secretary of State for Defence in Her Britannic Majesty's Government of the United Kingdom of Great Britain and Northern Ireland - Inventors: David Fairhurst - Web page: https://patentgrep.com/patent/US4400250A ## CPC - B01D 15/00: Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor - B01D 15/267: {using neutral sorbents, e.g. activated carbon or diatomaceous earth} - B01D 57/02: by electrophoresis (treatment of water, waste water, sewage or sludge by electrophoresis C02F1/469; electrophoretic production of compounds or non-metals C25B7/00; investigating or analysing materials by using electrophoresis G01N27/26) - C02F 1/4691: {Capacitive deionisation} - C02F 1/283: {using coal, charred products, or inorganic mixtures containing them} - C02F 2001/46161: {Porous electrodes} - C02F 2201/4611: Fluid flow - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) - C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes) ## Abstract An apparatus for adsorbing at least one dissolved or suspended constituent from an ionically conducting medium which comprises a cell chamber, fluid inlet and outlet pipes leading into and out of the chamber and, positioned consecutively across the chamber, a charcoal cloth working electrode, a porous plastic, preferably nylon, diaphragm and a graphite or platinum counter electrode. The charcoal cloth working electrode is in intimate electrical contact with a metal wire or gauze and by varying the potential of the wire or gauze with a potentiostat the potential applied to the working electrode can also be varied, preferably by increments of above 0.01 v. Current is supplied to the working electrode by the counter electrode. The porous diaphragm allows the passage of ions from the counter to the working electrode but prevents the passage of particles of charcoal cloth from one electrode to the other. In use an ionically conducting medium containing at least one dissolved or suspended constituent is brought into contact with the charcoal cloth working electrode. By applying an electric potential to the cloth with respect to the medium at least one of the dissolved or suspended constituents is adsorbed on to the cloth. The charcoal cloth working electrode is between 20 and 60 times more efficient than an equivalent graphite electrode. The apparatus and method is useful in the recovery of chemicals from industrial effluent and in the separation of chemical mixtures. ## Claims ### Claim 1 A method of adsorbing at least one constituent from an ionically conducting medium which comprises: a. bringing the medium into contact with a working electrode consisting essentially of charcoal cloth composed of activated fibrous or filamental carbon having a surface area as measured by nitrogen adsorption by the method of Brunnauer/Emmett/Teller, of above 600 m.sup.2 gm.sup.-1 ; and b. applying a d.c. electric potential to the working electrode with respect to the medium, so that at least one of the constituents is adsorbed on the working electrode. ### Claim 2 (depends on 1) A method according to claim 1 wherein the ionically conducting medium is an aqueous medium and the potential difference between the working electrode and the medium is less than 1.5 volts. ### Claim 3 (depends on 1) A method according to claim 1 wherein the ionically conducting medium is a non-aqueous medium and the potential difference between the working electrode and the medium is less than 3 volts. ### Claim 4 (depends on 1) A method according to claim 1 wherein the ionically conducting medium contains a supporting electrolyte. ### Claim 5 A method of separating at least two constituents in a first ionically conducting medium which comprises: a. bringing the medium into contact with a working electrode consisting essentially of charcoal cloth composed of activated fibrous or filamental carbon having a surface area, as measured by nitrogen adsorption by the method of Brunnauer/Emmett/Teller, of above 600 m.sup.2 gm.sup.-1 ; b. applying a d.c. electric potential to the working electrode, with respect to the medium, so that at least one of the constituents is adsorbed on the working electrode; c. removing the first ionically conducting medium; d. contacting the working electrode with a second ionically conducting medium; and e. applying an electric potential to the working electrode with respect to the second medium, so that at least one of the constituents adsorbed on the cloth is released into the medium. ### Claim 6 (depends on 5) A method according to claim 5 wherein the first and second ionically conducting media are aqueous media and the potential difference between the working electrode and the media is less than 1.5 volts. ### Claim 7 (depends on 5) A method according to claim 5 wherein the first and second ionically conducting media are non-aqueous media and the potential difference between the working electrode and the media is less than 3 volts. ### Claim 8 (depends on 5) A method according to claim 5 wherein the first and second ionically conducting media contain a supporting electrolyte. ### Claim 9 An apparatus for adsorbing at least one constituent from an ionically conducting medium and for separating at least two constituents in an ionically conducting medium which comprises: a. an electrochemical cell, having a cell chamber, a fluid inlet pipe leading into the chamber and a fluid outlet pipe leading out of the chamber; b. positioned consecutively across the chamber, a counter electrode, a porous diaphragm and a working electrode, consisting essentially of charcoal cloth composed of activated fibrous or filamental carbon having a surface area, as measured by nitrogen adsorption by the method of Brunnauer/Emmett/Teller, of above 600 m.sup.2 gm.sup.-1 ; c. means for applying a d.c. potential to the working electrode; and d. means for varying the potential applied to the working electrode. ### Claim 10 (depends on 9) An apparatus according to claim 9 wherein the means for applying a potential to the working electrode is selected from the group consisting of a metal wire and a metal gauze. ### Claim 11 (depends on 10) An apparatus according to claim 10 wherein the metal wire or metal gauze is pressed against the working electrode so that the potential applied to the working electrode is variable in increments of about 0.01 volts. ### Claim 12 (depends on 9) An apparatus according to claim 9 wherein the means for varying the potential applied to the working electrode is a potentiostat.