Abstract:
A processing facility is provided that includes a feedstock separation system configured to separate a feed stream into a lights stream and a heavies stream, a hydrogen production system configured to produce hydrogen and carbon dioxide from the lights stream, and a carbon dioxide conversion system configured to produce synthetic hydrocarbons or the carbon dioxide. The processing facility also includes a hydroprocessing system configured to process the heavies stream, and a hydroprocessor separation system configured to separate a hydroprocessing system effluent into a separator tops stream and a separator bottoms stream, wherein the separator bottoms stream is fed to the hydrogen production system.
Abstract:
The present disclosure describes a hybrid photovoltaic (PV) panel that includes: a first photovoltaic (PV) layer comprising photovoltaic cells capable of converting energy from incident solar power into electricity; a second transparent layer arranged underneath the first PV layer such that a portion of the incident solar power passes through; and a third thermal collection layer arranged underneath the second transparent layer and comprising absorbing material capable of absorbing energy from the portion of the incident solar power that has passed through the second transparent layer, wherein the second transparent layer includes a thermally insulating material to provide a thermal barrier between the first PV layer and the third thermal collection layer such that when the PV panel is operated, the first PV layer operates at a temperature lower than a temperature of the thermal collection layer.
Abstract:
A system integrating heavy fuel coking and chemical looping combustion is provided. The system includes a source of heavy fuel, a cracking reactor into which the fuel and metal oxides are introduced, a fuel reactor in fluid communication with the cracking reactor, and an air reactor in fluid communication with the fuel reactor. In the cracking reactor, the fuel undergoes a cracking reaction forming products and petcoke deposits on the metal oxides. The fuel reactor is configured to gasify metal oxides with petcoke deposits to produce syngas and reduce the metal oxides. The system transports a first portion of the reduced metal oxides to the cracking reactor and a second portion to the fuel reactor. The air reactor is configured to receive reduced metal oxides from the fuel reactor and oxidize them. The system is further configured to transport the oxidized metal oxides to the fuel reactor.
Abstract:
A process for power generation using a chemical looping combustion concept is integrated with heavy liquid fuel coking in a cracking reactor, and is configured such that petcoke deposits on metal oxide particles from the cracking reactor are used as fuel in the chemical looping combustion reaction. The process is also configured such that metal oxide particles provide the heat necessary for the cracking reaction to be initiated in the cracking reactor.
Abstract:
A process for power generation using a chemical looping combustion concept is integrated with heavy liquid fuel coking in a cracking reactor, and is configured such that petcoke deposits on metal oxide particles from the cracking reactor are used as fuel in the chemical looping combustion reaction. The process is also configured such that metal oxide particles provide the heat necessary for the cracking reaction to be initiated in the cracking reactor.
Abstract:
A chemical looping combustion (CLC) process for sour gas combustion is integrated with a gas turbine combined cycle and a steam generation unit, and is configured to provide in-situ removal of H2S from the sour gas fuel by reacting the H2S with a oxygen carrier at a location within the fuel reactor of the CLC unit. The process is also configured such that oxygen-rich exhaust gases from the gas turbine combined cycle is used to feed the air reactor of the CLC unit and re-oxidize oxygen carriers for recirculation in the CLC unit.
Abstract translation:用于酸性气体燃烧的化学循环燃烧(CLC)方法与燃气轮机联合循环和蒸汽发生单元集成,并且被配置为通过使H2S与氧气载体反应从酸性气体燃料中原位除去H 2 S 在CLC单元的燃料反应器内的位置。 该方法还被配置为使得来自燃气轮机联合循环的富氧废气用于进料CLC单元的空气反应器并再次氧化氧载体以在CLC单元中再循环。
Abstract:
A processing facility is provided. The processing facility includes an asphaltenes and metals (AM) removal system configured to process a feed stream to produce a power generation stream, a hydroprocessing feed stream, and an asphaltenes stream. A power generation system is fed by the power generation feed stream. A hydroprocessing system is configured to process the hydroprocessing feed stream to form a gas stream and a liquid stream. A hydrogen production system is configured to produce hydrogen, carbon monoxide and carbon dioxide from the gas feed stream. A carbon dioxide conversion system is configured to produce synthetic hydrocarbons from the carbon dioxide, and a cracking system is configured to process the liquid feed stream.
Abstract:
The present disclosure describes a hybrid photovoltaic (PV) panel that includes: a first photovoltaic (PV) layer comprising photovoltaic cells capable of converting energy from incident solar power into electricity; a second transparent layer arranged underneath the first PV layer such that a portion of the incident solar power passes through; and a third thermal collection layer arranged underneath the second transparent layer and comprising absorbing material capable of absorbing energy from the portion of the incident solar power that has passed through the second transparent layer, wherein the second transparent layer includes a thermally insulating material to provide a thermal barrier between the first PV layer and the third thermal collection layer such that when the PV panel is operated, the first PV layer operates at a temperature lower than a temperature of the thermal collection layer.
Abstract:
An apparatus includes a housing that defines a first zone, a second zone, a third zone, and a fourth zone. The apparatus includes an inlet, a first outlet, a second outlet, and a conveyor belt. The inlet is configured to receive a carbon dioxide-containing fluid in the first zone. The first outlet is configured to discharge a carbon dioxide-depleted fluid from the first zone. The second outlet is configured to discharge a carbon dioxide-rich fluid from the third zone. The conveyor belt passes through each of the zones. The conveyor belt includes a carbon dioxide sorbent. Within the first zone, the carbon dioxide sorbent is configured to adsorb carbon dioxide from the carbon dioxide-containing fluid to produce the carbon dioxide-depleted fluid. Within the third zone, the carbon dioxide sorbent is configured to desorb the captured carbon dioxide to produce the carbon dioxide-rich fluid.
Abstract:
A hydrocarbon is reacted with water in the presence of a catalyst to form hydrogen, carbon monoxide, and carbon dioxide. Hydrogen is selectively allowed to pass through a hydrogen separation membrane to a permeate side of a reactor, while water and carbon-containing compounds remain in a retentate side of the reactor. An outlet stream is flowed from the retentate side to a heat exchanger. The outlet stream is cooled to form a cooled stream. The cooled stream is separated into a liquid phase and a vapor phase. The liquid phase is flowed to the heat exchanger and heated to form steam. The vapor phase is cooled to form condensed water and a first offgas stream. The first offgas stream is cooled to form condensed carbon dioxide and a second offgas stream. The steam and the second offgas stream are recycled to the reactor.