# US 10,500,563 B2 · Emissions control system including capability to clean and/or rejuvenate carbon-based sorbents and method of use > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 10,500,563 B2 - Document ID: US10500563B2 - Status: Granted - Kind: B2 - Application number: 16/042,692 - Filed: 2018-07-23 - Published: 2018-11-15 - Granted: 2019-12-10 - Earliest claimed: 2014-07-25 - Assignees: Chemical and Metal Technologies LLC - Applicants: Chemical and Metal Technologies LLC - Inventors: Hal Stuhler; Lori Stuhler; Van T. Walworth; Scott Drummond - Web page: https://patentgrep.com/patent/US10500563B2 ## CPC - B01J 20/205: {Carbon nanostructures, e.g. nanotubes, nanohorns, nanocones, nanoballs (carbon nanotubes per se C01B32/15)} - B01D 53/64: Heavy metals or compounds thereof, e.g. mercury - B01D 53/8665: {Removing heavy metals or compounds thereof, e.g. mercury} - B01D 53/96: Regeneration, reactivation or recycling of reactants - B01J 8/36: with fluidised bed through which there is an essentially horizontal flow of particles - B01J 19/006: {Baffles} - B01J 19/2425: {in parallel} - B01J 20/0237: {Compounds of Cu} - B01J 20/0244: {Compounds of Zn} - B01J 20/0251: {Compounds of Si, Ge, Sn, Pb (B01J20/10 takes precedence)} - B01J 20/0266: {Compounds of S} - B01J 20/041: {Oxides or hydroxides} - B01J 20/06: comprising oxides or hydroxides of metals not provided for in group B01J20/04 - B01J 20/18: Synthetic zeolitic molecular sieves - B01J 20/20: comprising free carbon; comprising carbon obtained by carbonising processes - B01J 20/3236: {containing metal, other than zeolites, e.g. oxides, hydroxides, sulphides or salts} - B01J 20/324: {containing free carbon, e.g. activated carbon} - B01D 53/8609: {Sulfur oxides} - B01D 53/8625: {Nitrogen oxides} - B01D 2253/102: Carbon - B01D 2257/602: Mercury or mercury compounds - B01J 2219/00768: vertical - B01J 2219/00772: in a helix - B01J 2219/30242: Star - B01J 2220/42: Materials comprising a mixture of inorganic materials (materials coated or impregnated on a carrier B01J20/32) - B01J: CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS - 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) ## Abstract A system and method for cleaning, conditioning, and/or rejuvenating carbon-based sorbents is disclosed where a chemical cleaning process is used to separate contaminants from the sorbent. The contaminants can be disposed of or recycled for industrial uses. The cleaned and/or rejuvenated carbon-based sorbent is recycled back into a reverse venturi shaped fluidized bed apparatus for later use. Spent carbon-based sorbent can be routed for appropriate disposal. The carbon-based sorbents include, but are not limited to, activated carbon sorbent and biochar sorbent. Optionally, the sorbents can be processed through the system prior to exposure to contaminated emissions to enhance and increase the porosity of the outer surface of the sorbents. ## Claims ### Claim 1 An emissions control system including a fluidized bed apparatus for removing contaminants from emissions, comprising: a housing shaped as a reverse venturi, said housing including an entry portion for receiving the emissions at a pre-determined entry flow rate, an exit portion for expelling the emissions at a pre-determined exit flow rate, and an enlarged portion disposed between said entry portion and said exit portion of said housing for trapping the contaminants in the emissions; said entry portion, said exit portion, and said enlarged portion of said housing being arranged in fluid communication with each other; a mass of reactive material disposed within said enlarged portion of said housing; said mass of reactive material having a reactive outer surface disposed in contact with the emissions, said mass of reactive material including a carbon-based sorbent; and at least one sorbent treatment subsystem disposed in fluid communication with said housing of said fluidized bed apparatus, said at least one sorbent treatment subsystem including a solvent for separating the contaminants from said carbon-based sorbent after said carbon-based sorbent has been exposed to the emissions. ### Claim 2 (depends on 1) The emissions control system as set forth in claim 1, wherein said at least one sorbent treatment subsystem is internal to said housing of said fluidized bed apparatus. ### Claim 3 (depends on 1) The emissions control system as set forth in claim 1 wherein said at least one sorbent treatment subsystem is external to said housing of said fluidized bed apparatus. ### Claim 4 (depends on 1) The emissions control system as set forth in claim 1, wherein said at least one sorbent treatment subsystem includes an entry port for receiving contaminated sorbent from said housing of said fluidized bed apparatus, a cleaning and rejuvenation station, a sorbent disposal station, a contaminant disposal station, a bulk refill station, and a return port for returning clean sorbent to said housing of said fluidized bed apparatus. ### Claim 5 (depends on 1) The emissions control system as set forth in claim 1, wherein said solvent includes at least one of: methyl ethyl ketone, methylene chloride, and ethanol. ### Claim 6 (depends on 1) The emissions control system as set forth in claim 1, wherein said at least one sorbent treatment subsystem is configured to heat said solvent to a temperature within an optimum effective temperature range of 125 degrees Celsius to 145 degrees Celsius. ### Claim 7 (depends on 1) The emissions control system as set forth in claim 1, wherein said at least one sorbent treatment subsystem is configured to heat said solvent to a temperature that is at least 5 degrees Celsius above ambient temperature and no greater than 210 degrees Celsius. ### Claim 8 (depends on 1) The emissions control system as set forth in claim 1, wherein said at least one sorbent treatment subsystem includes water for rinsing said carbon-based sorbent to separate said carbon-based sorbent from said solvent which contains contaminants. ### Claim 9 (depends on 8) The emissions control system as set forth in claim 8, wherein said at least one sorbent treatment subsystem is configured to heat said water to a temperature within an optimum effective temperature range of 63 degrees Celsius to 83 degrees Celsius. ### Claim 10 (depends on 8) The emissions control system as set forth in claim 8, wherein said at least one sorbent treatment subsystem is configured to heat said water to a temperature that is at least 5 degrees Celsius above ambient temperature and no greater than 98 degrees Celsius. ### Claim 11 (depends on 1) The emissions control system as set forth in claim 1, wherein said at least one sorbent treatment subsystem does not include a furnace burn station. ### Claim 12 (depends on 1) The emissions control system as set forth in claim 1, wherein said at least one sorbent treatment subsystem does not emit carbon dioxide during the cleaning and rejuvenation of said carbon-based sorbent. ### Claim 13 (depends on 1) The emissions control system as set forth in claim 1, wherein said carbon-based sorbent includes at least one of activated carbon and biochar. ### Claim 14 An emissions control system including a fluidized bed apparatus for removing contaminants from emissions, comprising: a housing shaped as a reverse venturi, said housing including an entry portion for receiving the emissions at a pre-determined entry flow rate, an exit portion for expelling the emissions at a pre-determined exit flow rate, and an enlarged portion disposed between said entry portion and said exit portion of said housing for trapping the contaminants in the emissions; said entry portion, said exit portion, and said enlarged portion of said housing being arranged in fluid communication with each other; a mass of reactive material disposed within said enlarged portion of said housing; said mass of reactive material having a reactive outer surface disposed in contact with the emissions, said mass of reactive material including a carbon-based sorbent; and at least one sorbent treatment subsystem including a solvent for treating said carbon-based sorbent before said carbon-based sorbent has been exposed to the emissions. ### Claim 15 (depends on 14) The emissions control system as set forth in claim 14, wherein said solvent chemically interacts with said carbon-based sorbent and increases a porosity of said reactive outer surface of said mass of reactive material. ### Claim 16 An emissions control method for removing contaminants from emissions comprising the steps of: routing the emissions through at least one pre-filter containing a pre-filter sorbent; routing the emissions away from the at least one pre-filter and into a treatment system having a reverse venturi shaped fluidized bed apparatus containing a reactive material that chemically binds with the contaminants carried in the emissions; selecting a carbon-based sorbent as the reactive material in the reverse venturi shaped fluidized bed apparatus; trapping the contaminants in the reactive material contained in the reverse venturi shaped fluidized bed apparatus; and routing the carbon-based sorbent through at least one sorbent treatment subsystem containing a solvent that cleans and conditions the carbon-based sorbent. ### Claim 17 (depends on 16) The method as set forth in claim 16, further comprising the steps of: heating the solvent in the sorbent treatment subsystem; and spraying the heated solvent on the carbon-based sorbent to clean and condition the carbon-based sorbent. ### Claim 18 (depends on 17) The method as set forth in claim 17, wherein the solvent is heated to a temperature within an optimum effective temperature range of 125 degrees Celsius to 145 degrees Celsius. ### Claim 19 (depends on 17) The method as set forth in claim 17, wherein the solvent is heated to a temperature that is at least 5 degrees Celsius above ambient temperature and no greater than 210 degrees Celsius. ### Claim 20 (depends on 17) The method as set forth in claim 17, further comprising the step of: recirculating the heated solvent in the sorbent treatment subsystem for at least 45 minutes. ### Claim 21 (depends on 16) The method as set forth in claim 16, further comprising the step of: rinsing the carbon-based sorbent in the sorbent treatment subsystem with water to clean the carbon-based sorbent. ### Claim 22 (depends on 21) The method as set forth in claim 21, further comprising the step of: heating the water in the sorbent treatment subsystem to a temperature within an optimum effective temperature range of 63 degrees Celsius to 83 degrees Celsius. ### Claim 23 (depends on 21) The method as set forth in claim 21, further comprising the step of: heating the water in the sorbent treatment subsystem to a temperature that is at least 5 degrees Celsius above ambient temperature and no greater than 98 degrees Celsius. ### Claim 24 (depends on 16) The subsystem as set forth in claim 16, further comprising the steps of: separating cleaned carbon-based sorbent from spent carbon-based sorbent; disposing of the spent carbon-based sorbent; and routing the cleaned sorbent back to the reverse venturi shaped fluidized bed apparatus. ### Claim 25 (depends on 24) The method as set forth in claim 24, further comprising the step of: replacing the spent carbon-based sorbent with new carbon-based sorbent and routing the new carbon-based sorbent to the reverse venturi shaped fluidized bed apparatus. ### Claim 26 (depends on 16) The subsystem as set forth in claim 16, further comprising the step of: separating the contaminants from the solvent using a distillation process and recycling the solvent.