Coated activated carbon for automotive emission control
View Patent ↗A method for avoidance of attrited carbon dust is disclosed to lead to improved canister performance in emission control. Product attrition by dusting of granular and shaped activated carbons is disclosed to be reduced significantly, or essentially eliminated, by the application of a thin, continuous polymer coating on the granular or shaped activated carbon, without a reduction in adsorption velocity or capacity of the activated carbon when used in automotive emission control canisters.
1. A method for capturing fuel vapor from a fluid stream containing same in an automobile by routing said stream through an emission control canister comprising an activated carbon material exhibiting initial, pre-coating butane activity and butane working capacity values and having its surface coated with a continuous film of a polymer, said polymer film being operable for essentially eliminating attrition of the activated carbon material resulting from dusting and wherein the coated activated carbon material exhibits final, post-coating butane activity and butane working capacity values at least 90% of the initial, pre-coating butane activity and butane working capacity values, respectively.
2. The method of claim 1 wherein the final, post-coating butane activity and butane working capacity values are at least 95% of the initial, pre-coating butane activity and butane working capacity values, respectively.
3. The method of claim 1 wherein the final, post-coating butane activity and butane working capacity values are at least 98% of the initial, pre-coating butane activity and butane working capacity values, respectively.
4. The method of claim 1 wherein the final, post-coating butane activity and butane working capacity values are at least 100% of the initial, pre-coating butane activity and butane working capacity values, respectively.
5. A method for capturing gasoline vapor and combustion emission from a fluid stream containing same in an automobile by routing said stream through an emission control canister comprising a polymer-coated activated carbon material exhibiting essentially no dusting attrition of the activated carbon material and said activated carbon material exhibits initial, pre-coated butane activity and butane working capacity values and wherein the coated activated carbon material exhibits final, post-coating butane activity and butane working capacity values at least 90% of the initial, pre-coating butane activity and butane working capacity values, respectively.
6. The method of claim 5 wherein the final, post-coating butane activity and butane working capacity values are at least 95% of the initial, pre-coating butane activity and butane working capacity values, respectively.
7. The method of claim 6 wherein the final, post-coating butane activity and butane working capacity values are at least 98% of the initial, pre-coating butane activity and butane working capacity values, respectively.
8. The method of claim 7 wherein the final, post-coating butane activity and butane working capacity values are at least 100% of the initial, pre-coating butane activity and butane working capacity values, respectively.
9. A method for capturing gasoline vapor and combustion emission from a fluid stream containing same in an automobile by routing said stream through an emission control canister comprised of a polymer-coated activated carbon prepared by coating the activated carbon material according to the steps of:
(a) spraying an emulsion of the polymer onto exposed surfaces of the activated carbon material while it is in a state of turbulence at a processing temperature above ambient temperature; and
(b) drying the coated activated carbon material at above ambient temperature.
10. The method of claim 9 comprising a further step
(c) de-dusting the dry coated activated carbon material by removing any residual dust therefrom.
11. The method of claim 9 further comprising an initial step of heating the active carbon material at above ambient temperature.
12. The method of claim 9 wherein the processing temperature is maintained from 50° F. (10° C.) to 280° F. (138° C.) for from about 1 minute to about 12 hours.
13. The method of claim 12 wherein the processing temperature is maintained from about 70° F. (21° C.) to about 250° C. (121° C.) for from about 5 minutes to about 6 hours.
14. The method of claim 1 wherein the polymer is selected from the group consisting of polyethylene, polypropylene, polyisobutylene, polystyrene, polyisoprene, polychloroprene, poly-4-methyl-1-pentene, polybutadiene, polybutene, polyacrylate, polymethyl methacrylate, polybutylmethacrylate, polymethacrylates, polyacrylic acid, polytetrafluoroethylene, trifluoroethylene, vinyl fluoride, fluorvinylidene, fluorobutylene, fluoropropylene, polyurethane, polyethylene terephthalate, styrene butadiene, modified polybutadiene, epoxies, modified alkyds, polyesters, starches, methyl cellulose, ethyl cellulose, carboxymethyl cellulose, polyvinyl acetate, cellulose acetate, cellulose nitrate, cellulose triacetate, cellulose acetate, phthalate, cellulose propionate morpholinobutyrate, hydroxypropylmethyl cellulose, ethylene vinyl acetate, acrylic polymers and copolymers, polysulfones, polyether sulfones, polyethers, polyethylene, glycols, polyimines, polybutylene, polyvinyl ethers, polyvinyl esters, polyalkylsulfides, polyarylsulfides, lignosulfonates, polyacrylamide, cyanoacrylate, polyamides, polyimides, polysiloxanes, methacrylonitrile, polyacrylonitrile, polyvinyl pyridine, polyvinyl benzene, polyvinyl acetate, polyvinyl pyrrolidene, polyvinyl butyral, polyvinyl alcohol, polyvinyl chloride, polyvinyl formaldehyde, polyformaldehyde, polycarbonates, and polyvinylidene chloride.
15. The method of claim 14 wherein the polymer is selected from the group consisting of acrylic polymer and polyethylene.
16. The method of claim 1 wherein the active carbon material is derived from a member of the group consisting of coal, lignocellulosic materials, petroleum, bone, and blood.
17. The method of claim 16 wherein the lignocellulosic materials are selected from the group consisting of including pulp, paper, residues from pulp production, wood chips, sawdust, wood flour, nut shell, kernel, and fruit pits.
18. The method of claim 5 wherein the polymer is selected from the group consisting of polyethylene, polypropylene, polyisobutylene, polystyrene, polyisoprene, polychloroprene, poly-4-methyl-1-pentene, polybutadiene, polybutene, polyacrylate, polymethyl methacrylate, polybutylmethacrylate, polymethacrylates, polyacrylic acid, polytetrafluoroethylene, trifluoroethylene, vinyl fluoride, fluorvinylidene, fluorobutylene, fluoropropylene, polyurethane, polyethylene terephthalate, styrene butadiene, modified polybutadiene, epoxies, modified alkyds, polyesters, starches, methyl cellulose, ethyl cellulose, carboxymethyl cellulose, polyvinyl acetate, cellulose acetate, cellulose nitrate, cellulose triacetate, cellulose acetate, phthalate, cellulose propionate morpholinobutyrate, hydroxypropylmethyl cellulose, ethylene vinyl acetate, acrylic polymers and copolymers, polysulfones, polyether sulfones, polyethers, polyethylene, glycols, polyimines, polybutylene, polyvinyl ethers, polyvinyl esters, polyalkylsulfides, polyarylsulfides, lignosulfonates, polyacrylamide, cyanoacrylate, polyamides, polyimides, polysiloxanes, methacrylonitrile, polyacrylonitrile, polyvinyl pyridine, polyvinyl benzene, polyvinyl acetate, polyvinyl pyrrolidene, polyvinyl butyral, polyvinyl alcohol, polyvinyl chloride, polyvinyl formaldehyde, polyformaldehyde, polycarbonates, and polyvinylidene chloride.
19. The method of claim 18 wherein the polymer is selected from the group consisting of polysiloxane, acrylic copolymer and polyethylene.
20. The method of claim 1 wherein a color pigment is added to the polymer emulsion to produce a colored activated carbon material.