Electrolysis devices and systems include a first plate having first and second outlets; a first screen extending below the first plate proximate to the first outlet wherein a inner diameter of the first screen?an inner diameter of the first outlet; a tube extending below the first plate wherein the tube is disposed around the first screen with a first gap between the first screen and the tube; a second screen extending below the first plate such that the second screen is disposed around the tube with a second gap between the tube and the second screen; the second outlet is either disposed between the tube and the second screen or outside of the second screen; and wherein a length of the first screen is less that a length of the second screen, and a length of the tube is greater than the length of the second screen.

The delayed coking method includes directing a heated secondary feedstock, which contains heated primary feedstock and recirculate, from a reaction furnace to a coking chamber. Vapor-liquid coking products formed in the coking chamber are then directed to a fractionation column, which fractionates hydrocarbon gas, gasoline, light and heavy gas oils, and bottom residues. Heavy gas oil from the fractionation column is directed to a thermal cracking furnace, the products of which are cooled by cooled light gas oil and directed to an evaporator for separation. In the evaporator, gases and light boiling products are removed by evaporation and returned to the fractionation column, and the remaining distillate cracking residue is separated and used as a component of the recirculate, along with bottom residues from the fractionation column. The resulting process produces high quality and high yield needle and anode cokes.

The delayed coking method includes directing a heated secondary feedstock, which contains heated primary feedstock and recirculate, from a reaction furnace to a coking chamber. Vapor-liquid coking products formed in the coking chamber are then directed to a fractionation column, which fractionates hydrocarbon gas, gasoline, light and heavy gas oils, and bottom residues. Heavy gas oil from the fractionation column is directed to a thermal cracking furnace, the products of which are cooled by cooled light gas oil and directed to an evaporator for separation. In the evaporator, gases and light boiling products are removed by evaporation and returned to the fractionation column, and the remaining distillate cracking residue is separated and used as a component of the recirculate, along with bottom residues from the fractionation column. The resulting process produces high quality and high yield needle and anode cokes.

Apparatus for processing waste-derived cellulose fibre into carbon char comprises an autoclave for treating waste with steam to produce processed material. The processed material includes cellulose fibre and plastics. The apparatus also includes a drying system for drying the cellulose fibre, and a torrefying unit for torrefying the dried cellulose fibre to produce carbon char. Thermal conversion means for thermally converting either said plastics or said VOCs provides heat for at least one of the autoclave, the drying system and the torrefying unit.

Apparatus for processing waste-derived cellulose fibre into carbon char comprises an autoclave for treating waste with steam to produce processed material. The processed material includes cellulose fibre and plastics. The apparatus also includes a drying system for drying the cellulose fibre, and a torrefying unit for torrefying the dried cellulose fibre to produce carbon char. Thermal conversion means for thermally converting either said plastics or said VOCs provides heat for at least one of the autoclave, the drying system and the torrefying unit.

A method for converting agricultural biomass or industrial bio waste into biofuel using concentrated radiated energy is disclosed. Biomass or bio waste is stored inside a batch reactor in either solid or semisolid state. Unwanted moisture and unwanted oxygen are removed from the stored agricultural biomass or industrial bio waste. Concentrated radiated energy is directed towards the biomass or bio waste through a radiated energy concentrator that focuses the concentrated radiated energy. Biomass or bio waste is kept within the depth of focus of the concentrated radiated energy during the conversion operation. Due to substantial matching of the absorption peak of biomass or bio waste with the emission peak of the concentrated radiated energy, the biomass or bio waste that is within the depth of focus instantaneously decomposes into biofuel. The biofuel thus generated is at ambient temperature with higher energy density.

A system, method and apparatus for creating an electric glow discharge includes a non-conductive housing having a longitudinal axis, a first opening aligned with the longitudinal axis, and a second opening aligned with the longitudinal axis and opposite the first opening, a first electrically conductive screen disposed proximate to the first opening of the housing and substantially perpendicular to the longitudinal axis, a second electrically conductive screen disposed proximate to the second opening of the housing and substantially perpendicular to the longitudinal axis, wherein the second electrically conductive screen separated from the first electrically conductive screen by a substantially equidistant gap, a non-conductive granular material disposed within the substantially equidistant gap, and the electric glow discharge is created whenever the first electrically conductive screen has a first polarity, the second electrically conductive screen has a second polarity, and an electrically conductive fluid is introduced into the substantially equidistant gap.

A system, method and apparatus for creating an electric glow discharge includes a non-conductive housing having a longitudinal axis, a first opening aligned with the longitudinal axis, and a second opening aligned with the longitudinal axis and opposite the first opening, a first electrically conductive screen disposed proximate to the first opening of the housing and substantially perpendicular to the longitudinal axis, a second electrically conductive screen disposed proximate to the second opening of the housing and substantially perpendicular to the longitudinal axis, wherein the second electrically conductive screen separated from the first electrically conductive screen by a substantially equidistant gap, a non-conductive granular material disposed within the substantially equidistant gap, and the electric glow discharge is created whenever the first electrically conductive screen has a first polarity, the second electrically conductive screen has a second polarity, and an electrically conductive fluid is introduced into the substantially equidistant gap.

A heat receiver, a reactor, and a heater utilize the heat of concentrated solar light for thermal decomposition and/or chemical reaction of coals, etc. The heat receiver includes: a side portion forming a substantially cylindrical side surface; a substantially circular bottom portion connected to the lower edge of the side portion; and a ceiling connected to the upper edge of the side portion. A substantially circular aperture is formed in the center of the ceiling. The heat receiver has a substantially cylindrical cavity and the opening portion is open. When the cavity has a diameter of D and a length of L, and the aperture has a diameter of d, d=D/2 or less and L=2D or more. Concentrated solar light entering the heat receiver is to be contained in the heat receiver to effectively utilize the solar light.

A heat receiver, a reactor, and a heater utilize the heat of concentrated solar light for thermal decomposition and/or chemical reaction of coals, etc. The heat receiver includes: a side portion forming a substantially cylindrical side surface; a substantially circular bottom portion connected to the lower edge of the side portion; and a ceiling connected to the upper edge of the side portion. A substantially circular aperture is formed in the center of the ceiling. The heat receiver has a substantially cylindrical cavity and the opening portion is open. When the cavity has a diameter of D and a length of L, and the aperture has a diameter of d, d=D/2 or less and L=2D or more. Concentrated solar light entering the heat receiver is to be contained in the heat receiver to effectively utilize the solar light.