A method of producing isolated graphene sheets from a layered graphite, comprising: (a) forming an alkali metal ion-intercalated graphite compound by an electrochemical intercalation which uses a liquid solution of an alkali metal salt dissolved in an organic solvent as both an electrolyte and an intercalate source, layered graphite material as an anode material, and a metal or graphite as a cathode material, and wherein a current is imposed upon a cathode and an anode at a current density for a duration of time sufficient for effecting the electrochemical intercalation of alkali metal ions into interlayer spacing; and (b) exfoliating and separating hexagonal carbon atomic interlayers (graphene planes) from the alkali metal ion-intercalated graphite compound using ultrasonication, thermal shock exposure, exposure to water solution, mechanical shearing treatment, or a combination thereof to produce isolated graphene sheets.

A method of producing isolated graphene sheets from a layered graphite, comprising: (a) forming an alkali metal ion-intercalated graphite compound by an electrochemical intercalation which uses a liquid solution of an alkali metal salt dissolved in an organic solvent as both an electrolyte and an intercalate source, layered graphite material as an anode material, and a metal or graphite as a cathode material, and wherein a current is imposed upon a cathode and an anode at a current density for a duration of time sufficient for effecting the electrochemical intercalation of alkali metal ions into interlayer spacing; and (b) exfoliating and separating hexagonal carbon atomic interlayers (graphene planes) from the alkali metal ion-intercalated graphite compound using ultrasonication, thermal shock exposure, exposure to water solution, mechanical shearing treatment, or a combination thereof to produce isolated graphene sheets.

This invention relates to electrocatalytic processes for the formation of formate esters using at least one catalyst or pre-catalyst; wherein the formate ester can be further hydrolyzed.

Artifacts from the presence of a reference electrode in a thin-film cell configuration can be minimized or eliminated by providing the surface of a reference electrode with a specified surface resistivity. Theoretical considerations are set forth that show that for a given wire size, there is a theoretical surface resistance (or resistivity) that negates all artifacts from the presence of the reference wire. The theory and the experimental results hold for a electrochemical cell in a thin-film configuration.

Artifacts from the presence of a reference electrode in a thin-film cell configuration can be minimized or eliminated by providing the surface of a reference electrode with a specified surface resistivity. Theoretical considerations are set forth that show that for a given wire size, there is a theoretical surface resistance (or resistivity) that negates all artifacts from the presence of the reference wire. The theory and the experimental results hold for a electrochemical cell in a thin-film configuration.

Hydrogen gas as a power source is obtained from gaseous water, including seawater vapor existing abundantly at near-surface levels of the oceans or humid air over land. An integrated system of photovoltaic cells for capturing and harnessing solar energy is combined with a water vapor electrolysis system comprising an electrolyzer with an anode compartment and a cathode compartment separated by a proton exchange membrane. The photovoltaic aspects of the system convert the energy of the sun to drive electrolysis of gaseous water from the environment. The electrolyzer aspects include an anode, a cathode, and a proton exchange membrane. At the anode, oxygen evolution reaction (OER) catalysts oxidize H.sub.2O to oxygen gas and protons, the latter being diffused through a membrane (e.g., a solid polymer electrolyte membrane such as Nafion). At the cathode, photogenerated electrons are conducted to hydrogen evolution reaction (HER) catalysts to reduce the protons to hydrogen gas, while concentration gradients drive the generated O.sub.2 back to the atmosphere.

Hydrogen gas as a power source is obtained from gaseous water, including seawater vapor existing abundantly at near-surface levels of the oceans or humid air over land. An integrated system of photovoltaic cells for capturing and harnessing solar energy is combined with a water vapor electrolysis system comprising an electrolyzer with an anode compartment and a cathode compartment separated by a proton exchange membrane. The photovoltaic aspects of the system convert the energy of the sun to drive electrolysis of gaseous water from the environment. The electrolyzer aspects include an anode, a cathode, and a proton exchange membrane. At the anode, oxygen evolution reaction (OER) catalysts oxidize H.sub.2O to oxygen gas and protons, the latter being diffused through a membrane (e.g., a solid polymer electrolyte membrane such as Nafion). At the cathode, photogenerated electrons are conducted to hydrogen evolution reaction (HER) catalysts to reduce the protons to hydrogen gas, while concentration gradients drive the generated O.sub.2 back to the atmosphere.

A method of producing oil, gas, and ash fertilizer from a feedstock includes inputting the feedstock into a reaction chamber having a wall, and combusting the feedstock in the reaction chamber. An electrical current flow is induced between the reaction chamber wall and the feedstock so as to cause arcing in the feedstock within the reaction chamber. Ash reaction byproducts migrate downward through the reaction chamber onto ash support structure, which is substantially electrically isolated from the reaction chamber wall. Gas and liquid reaction byproducts migrate upward through the reaction chamber to an upper chamber by a partial vacuum in the upper chamber, and are evacuated therefrom. The oil and gas are then separated from the evacuated gas/liquid products, providing the oil and the gas products. The oil is refinable, the gas is high in energy content, and the ash fertilizer is high in nitrogen.

A method of producing oil, gas, and ash fertilizer from a feedstock includes inputting the feedstock into a reaction chamber having a wall, and combusting the feedstock in the reaction chamber. An electrical current flow is induced between the reaction chamber wall and the feedstock so as to cause arcing in the feedstock within the reaction chamber. Ash reaction byproducts migrate downward through the reaction chamber onto ash support structure, which is substantially electrically isolated from the reaction chamber wall. Gas and liquid reaction byproducts migrate upward through the reaction chamber to an upper chamber by a partial vacuum in the upper chamber, and are evacuated therefrom. The oil and gas are then separated from the evacuated gas/liquid products, providing the oil and the gas products. The oil is refinable, the gas is high in energy content, and the ash fertilizer is high in nitrogen.

There is disclosed an electrochemical deblocking solution for use on an electrode microarray. There is further disclosed a method for electrochemical synthesis on an electrode array using the electrochemical deblocking solution. The solution and method are for removing acid-labile protecting groups for synthesis of oligonucleotides, peptides, small molecules, or polymers on a microarray of electrodes while substantially improving isolation of deblocking to active electrodes. The method comprises applying a voltage or a current to at least one electrode of an array of electrodes. The array of electrodes is covered by the electrochemical deblocking solution.