摘要:
A thermolysis based hydrogen and oxygen generator and a method of generating hydrogen and oxygen can include a high pressure pump for pumping fluid, such fluid provided for separating into at least hydrogen molecules and oxygen molecules, a high pressure, high temperature spherical vessel coupled to the high pressure pump, and one or more lasers for focusing energy in a predetermined direction towards the spherical vessel, where the one or more lasers creates heat energy and pressure in the spherical vessel sufficiently to cause the fluid in the spherical vessel to separate into hydrogen molecules and oxygen molecules. The generator can further include a power supply for powering the one or lasers and the high pressure pump, a hydrogen storage tank coupled to the spherical vessel for storing the hydrogen molecules, and an oxygen storage tank coupled to the spherical vessel for storing the oxygen molecules.
摘要:
A system for extracting oxygen from a fluid includes a separator allowing a fluid to pass lengthwise through the separator to produce a mixture with the fluid having at least a portion of oxygen removed from the fluid. The separator includes a wall surrounding an interior portion of a tube. The wall has at least one aperture formed in the wall. The separator also includes at least one magnet positioned adjacently to the at least one aperture. The magnet has a north pole end and a south pole end. A magnetic field gradient is formed between the north pole end and the south pole end, and extends into an interior portion of the tube. The system also includes a storage tank fluidly coupled to the at least one aperture for storing the at least a portion of the oxygen removed from the fluid via the separator.
摘要:
Disclosed is a cycle piston engine power system in which a compression ignition or spark ignition reciprocating piston engine is made non-emissive via a semi-closed cycle, in a manner which produces saleable CO2 product at pressure. The cycle piston engine power system can includes, among other elements, a piston engine for generating power and exhaust gas; a water cooling and separation unit which receives the exhaust gas and cools and removes water from the exhaust gas to create CO2 gas supply; a mixing pressure vessel which receives at least a portion of the CO2 gas supply from the water cooling and separation unit and mixes the CO2 gas supply with oxygen to create a working fluid to be provided to the piston engine; and an oxygen generator for providing oxygen to the mixing pressure vessel.
摘要:
A system and process are provided for extracting a substance from a molecular combination. The process comprises heating the molecular combination to dissociate the molecular combination into cations and anions, moving the cations and anions through a magnetic field to separate cations and anions, and isolating cations from anions with a barrier. The system comprises a non-conductive conduit for guiding an ionized particle stream, a magnetic field source for creating a magnetic field through which the ionized particle stream moves, and a barrier located in the conduit. The ionized particle stream has a velocity relative to the conduit, and the magnetic field source is oriented relative to the velocity of the ionized particle stream so that cations are separated from anions as the ionized particle stream moves through the magnetic field. The barrier is oriented in the conduit so that cations are isolated from anions after separation.
摘要:
In various implementations, methanol is produced using a (CO+H2) containing synthesis gas produced from a combined PDX plus EHTR or a combined ATR plus EHTR at a pressure of 70 bar to 100 bar at the correct stoichiometric composition for methanol synthesis so that no feed gas compressor is required for the feed to the methanol synthesis reactor loop.
摘要翻译:在各种实施方案中,使用由组合的PDX加EHTR或组合的ATR plus EHTR产生的(CO + H 2)的合成气在70巴至100巴的压力下以合适的化学计量组成用于甲醇合成来生产甲醇,使得不 进料气压缩机是进料到甲醇合成反应器回路所必需的。
摘要:
A gasification system and method. The system can include a gasifier and a purification unit fluidly coupled to the gasifier, with the purification unit receiving raw syngas from the gasifier and producing waste gas and a syngas product. The system can also include a first reformer fluidly coupled to the purification unit, with the first reformer receiving a first portion of the waste gas and producing reformed hydrocarbon. The system can further include a second reformer having a first inlet fluidly coupled to the purification unit, a second inlet fluidly coupled to the first reformer, and an outlet fluidly coupled to the purification unit. The second inlet can receive the reformed hydrocarbon from the first reformer, and the first inlet can receive a second portion of the waste gas from the purification unit. The second reformer can produce a recovered raw syngas that is directed to the purification unit.
摘要:
A system and process are provided for extracting a substance from a molecular combination. The process comprises heating the molecular combination to dissociate the molecular combination into cations and anions, moving the cations and anions through a magnetic field to separate cations and anions, and isolating cations from anions with a barrier. The system comprises a non-conductive conduit for guiding an ionized particle stream, a magnetic field source for creating a magnetic field through which the ionized particle stream moves, and a barrier located in the conduit. The ionized particle stream has a velocity relative to the conduit, and the magnetic field source is oriented relative to the velocity of the ionized particle stream so that cations are separated from anions as the ionized particle stream moves through the magnetic field. The barrier is oriented in the conduit so that cations are isolated from anions after separation.
摘要:
In various implementations, methanol is produced using a (CO+H2) containing synthesis gas produced from a combined PDX plus EHTR or a combined ATR plus EHTR at a pressure of 70 bar to 100 bar at the correct stoichiometric composition for methanol synthesis so that no feed gas compressor is required for the feed to the methanol synthesis reactor loop.
摘要翻译:在各种实施方案中,使用由组合的PDX加EHTR或组合的ATR plus EHTR产生的(CO + H 2)的合成气在70巴至100巴的压力下以合适的化学计量组成用于甲醇合成来生产甲醇,使得不 进料气压缩机是进料到甲醇合成反应器回路所必需的。
摘要:
A device includes a chamber to contain plasma, a water vapor injector to inject water vapor into the chamber, a high-frequency wave injector to inject a high-frequency wave inside the chamber, a magnetic structure to generate a magnetic field in the chamber and to generate plasma along the magnetic field lines, a module of the magnetic field presenting a magnetic mirror configuration with at least one electron cyclotron resonance zone to at least partially dissociate the water molecules introduced in vapor phase and to at least partially ionize the products of dissociation. The magnetic mirror configuration is such that the module of the magnetic field presents a nonpoint-shaped minimum, substantially constant, and substantially equal to the magnetic field corresponding to electron cyclotron resonance and at least partially extending along the chamber, such that the plasma has the form of a plasma surface; the water vapor injector injecting the vapor in the form of a supersonic jet and including a planar nozzle and a divertor. The device also includes a selective cryogenic condenser to freeze the oxygen coming from the dissociation without freezing the hydrogen coming from the dissociation and a hydrogen recovery unit configured to recover the hydrogen coming from the dissociation, the oxygen being trapped by the cryogenic condenser.
摘要:
The process and the device serve for cryogenic air fractionation, in particular for supplying an oxygen-enriched (product stream to an oxyfuel power plant. The distillation column system for nitrogen/oxygen separation has a high-pressure column (26) and a low-pressure column (32). The high-pressure column (26) and the low-pressure column (32) are thermally coupled via a condenser-evaporator (37). Feed air (1) is compressed in an air compressor (3), cooled at least in a first post-cooler (6) and purified in a purification device (22), cooled in a main heat exchanger (23a, 23b, 23c) and introduced at least in part (25, 29) into the high-pressure column (26). At least one liquid stream (33, 35) is introduced from the high-pressure column (26) into the low-pressure column (32). An oxygen-enriched product stream (41, 45, 46,47, 48) is taken off from the low-pressure column (32). A first nitrogen stream (63, 64, 65, 66) is withdrawn from the high-pressure column (26) and warmed to a temperature of at least 280 K (6). The warmed first nitrogen stream (67) is work-expanded (72) in a first warm expansion engine (68). The first nitrogen stream (70, 71) which is expanded in the first warm expansion engine (68) is work-expanded in a second warm expansion engine (72).