Divided Electrochemical Cell and Low Cost High Purity Hydride Gas Production Process
US-2015345037-A1 · Dec 3, 2015 · US
US2017370009A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017370009-A1 |
| Application number | US-201615193090-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 26, 2016 |
| Priority date | Jun 26, 2016 |
| Publication date | Dec 28, 2017 |
| Grant date | — |
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A method of producing graphene sheets from coke or coal powder, comprising: (a) forming an intercalated coke or coal compound by electrochemical intercalation conducted in an intercalation reactor, which contains (i) a liquid solution electrolyte comprising an intercalating agent; (ii) a working electrode that contains the powder in ionic contact with the liquid electrolyte, wherein the coke or coal powder is selected from petroleum coke, coal-derived coke, meso-phase coke, synthetic coke, leonardite, lignite coal, or natural coal mineral powder; and (iii) a counter electrode in ionic contact with the electrolyte, and wherein a current is imposed upon the working electrode and the counter electrode for effecting electrochemical intercalation of the intercalating agent into the powder; and (b) exfoliating and separating graphene planes from the intercalated coke or coal compound using an ultrasonication, thermal shock exposure, mechanical shearing treatment, or a combination thereof to produce isolated graphene sheets.
Opening claim text (preview).
1 . A method of producing isolated graphene sheets from a supply of coke or coal powder containing therein domains of hexagonal carbon atoms and/or hexagonal carbon atomic interlayers with an interlayer spacing, said method comprising: (a) forming an intercalated coke or coal compound by an electrochemical intercalation procedure which is conducted in an intercalation reactor, wherein said reactor contains (i) a liquid solution electrolyte comprising an intercalating agent; (ii) a working electrode that contains said coke or coal powder as an active material in ionic contact with said liquid solution electrolyte, wherein said coke or coal powder is selected from petroleum coke, coal-derived coke, meso-phase coke, synthetic coke, leonardite, anthracite, lignite coal, bituminous coal, natural coal mineral powder, or a combination thereof; and (iii) a counter electrode in ionic contact with said liquid solution electrolyte, and wherein a current is imposed upon said working electrode and said counter electrode at a current density for a duration of time sufficient for effecting electrochemical intercalation of said intercalating agent into said interlayer spacing; and (b) exfoliating and separating said hexagonal carbon atomic interlayers from said intercalated coke or coal compound using an ultrasonication, thermal shock exposure, mechanical shearing treatment, or a combination thereof to produce said isolated graphene sheets. 2 . The method of claim 1 , wherein multiple particles of said coke or coal powder are dispersed in said liquid solution electrolyte, disposed in a working electrode compartment, and supported or confined by a current collector in electronic contact therewith, and wherein said working electrode compartment and said multiple particles supported thereon or confined therein are not in electronic contact with said counter electrode. 3 . The method of claim 2 , wherein said multiple particles are clustered together to form a network of electron-conducting pathways. 4 . The method of claim 1 , wherein said reactor further contains a graphene plane-wetting agent dissolved in said liquid solution electrolyte. 5 . The method of claim 4 , wherein said graphene plane-wetting agent is selected from melamine, ammonium sulfate, sodium dodecyl sulfate, sodium (ethylenediamine), tetraalkyammonium, ammonia, carbamide, hexamethylenetetramine, organic amine, pyrene, 1-pyrenecarboxylic acid, 1-pyrenebutyric acid, 1-pyrenamine, poly(sodium-4-styrene sulfonate), or a combination thereof. 6 . The method of claim 1 , wherein said method is conducted intermittently or continuously and said supply of coke or coal powder and said liquid solution electrolyte are provided into said reactor intermittently or continuously. 7 . The method of claim 2 , wherein said method is conducted intermittently or continuously and said supply of coke or coal powder and said liquid solution electrolyte are provided into said working electrode compartment intermittently or continuously. 8 . The method of claim 1 , wherein said coke or coal powder in said working electrode compartment is dispersed in the liquid solution electrolyte at a concentration higher than 20% by weight. 9 . The method of claim 1 , wherein said coke or coal powder in said working electrode compartment is dispersed in the liquid solution electrolyte at a concentration higher than 50% by weight. 10 . The method of claim 1 , wherein said mechanical shearing treatment comprises operating air milling, air jet milling, ball milling, rotating-blade mechanical shearing, or a combination thereof. 11 . The method of claim 1 , wherein the imposing current provides a current density in the range of 0.1 to 600 A/m 2 . 12 . The method of claim 1 , wherein the imposing current provides a current density in the range of 1 to 500 A/m 2 . 13 . The method of claim 1 , wherein the imposing current provides a current density in the range of 10 to 300 A/m 2 . 14 . The method of claim 1 , wherein said thermal shock exposure comprises heating said intercalated coke or coal compound to a temperature in the range of 300-1,200° C. for a period of 15 seconds to 2 minutes. 15 . The method of claim 1 , wherein said isolated graphene sheets contain single-layer graphene. 16 . The method of claim 1 , wherein said isolated graphene sheets contain few-layer graphene having 2-10 hexagonal carbon atomic interlayers or graphene planes. 17 . The method of claim 4 , wherein said electrochemical intercalation includes intercalation of both said intercalating agent and said wetting agent into the interlayer spacing. 18 . The method of claim 1 , further comprising a step of re-intercalating said isolated graphene sheets using an electrochemical or chemical intercalation method to obtain intercalated graphene sheets and a step of exfoliating and separating said intercalated graphene sheets to produce single-layer graphene sheets using ultrasonication, thermal shock exposure, exposure to water solution, mechanical shearing treatment, or a combination thereof. 19 . The method of claim 1 , wherein said intercalating agent includes a species selected from a Brønsted acid selected from phosphoric acid (H 3 PO 4 ), dichloroacetic (Cl 2 CHCOOH), or an alkylsulfonic acid selected from methanesulfonic (MeSO 3 H), ethanesulfonic (EtSO 3 H), or 1-propanesulfonic (n-PrSO 3 H), or a combination thereof. 20 . The method of claim 1 , wherein said intercalating agent includes a metal halide. 21 . The method of claim 1 , wherein said intercalating agent includes a metal halide selected from the group consisting of MCl (M=Li, Na, K, Cs), MCl 2 (M=Zn, Ni, Cu, Mn), MCl 3 (M=Al, Fe, Ga), MCl, (M=Zr, Pt), MF 2 (M=Zn, Ni, Cu, Mn), MF 3 (M=Al, Fe, Ga), MF, (M=Zr, Pt), and combinations thereof. 22 . The method of claim 1 , wherein said intercalating agent includes an alkali metal salt selected from lithium perchlorate (LiClO 4 ), sodium perchlorate (NaClO 4 ), potassium perchlorate (KClO 4 ), sodium hexafluorophosphate (NaPF 6 ), potassium hexafluorophosphate (KPF 6 ), sodium borofluoride (NaBF 4 ), potassium borofluoride (KBF 4 ), sodium hexafluoroarsenide, potassium hexafluoroarsenide, sodium trifluoro-metasulfonate (NaCF 3 SO 3 ), potassium trifluoro-metasulfonate (KCF 3 SO 3 ), bis-trifluoromethyl sulfonylimide sodium (NaN(CF 3 SO 2 ) 2 ), sodium trifluoromethanesulfonimide (NaTF SI), bis-trifluoromethyl sulfonylimide potassium (KN(CF 3 SO 2 ) 2 ), a sodium ionic liquid salt, lithium perchlorate (LiClO 4 ), lithium hexafluorophosphate (LiPF 6 ), lithium borofluoride (LiBF 4 ), lithium hexafluoroarsenide (LiAsF 6 ), lithium trifluoro-metasulfonate (LiCF 3 SO 3 ), bis-trifluoromethyl sulfonylimide lithium (LiN(CF 3 SO 2 ) 2 ), lithium bis(oxalato)borate (LiBOB), lithium oxalyldifluoroborate (LiBF 2 C 2 O 4 ), lithium oxalyldifluoroborate (LiBF 2 C 2 O 4 ), lithium nitrate (LiNO 3 ), Li-Fluoroalkyl-Phosphates (LiPF 3 (CF 2 CF 3 ) 3 ), lithium bisperfluoro-ethysulfonylimide (LiBETI), lithium bis(trifluoromethanesulphonyl)imide, lithium bis(fluorosulphonyl)imide, lithium trifluoromethanesulfonimide (LiTFSI), an ionic liquid lithium salt, or a combination thereof. 23 . The method of claim 1 , wherein said intercalating agent includes an organic solvent selected from 1,3-dioxolane (DOL), 1,2-dimethoxyethane (DME), tetraethylene glycol dimethylether (TEGDME), poly(ethylene glycol) dimethyl ether (PEGDME), diethylene glycol dibutyl ether (DEGDBE), 2-ethoxyethyl ether (
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