Patent application number | Description | Published |
20100107634 | Rankine Cycle For LNG Vaporization/Power Generation Process - A method and system for generating power in a vaporization of liquid natural gas process, the method comprising pressurizing a working fluid; heating and vaporizing the working fluid; expanding the working fluid in one or more expanders for the generation of power, the working fluid comprises: 2-11 mol % nitrogen, methane, a third component whose boiling point is greater than or equal to that of propane, and a fourth component comprising ethane or ethylene; cooling the working fluid such that the working fluid is at least substantially condensed; and recycling the working fluid, wherein the cooling of the working fluid occurs through indirect heat exchange with a pressurized liquefied natural gas stream in a heat exchanger, and wherein the flow rate of the working fluid at an inlet of the heat exchanger is equal to the flow rate of the working fluid at an outlet of the heat exchanger. | 05-06-2010 |
20100313933 | Reflector-solar receiver assembly and solar module - A reflector-solar receiver assembly and methods related to the reflector-solar receiver assembly are described. The reflector-solar receiver assembly contains a reflector and a solar receiver. The reflector has a substantially planar light reflecting face and the solar receiver has a substantially planar light receiving face. The normal direction of the light reflecting face and the normal direction of the light receiving face are at an angle of about 90°. The reflector-solar receiver assembly can be installed at an installation site by placing the substantially planar light reflecting face at an angle of about γ−23.5° or about γ+23.5° from the gravitation line of the installation site, γ is the latitude of the installation site, so that the substantially planar light reflecting face reflects at least a portion of sunlight to the substantially planar light receiving face during a majority of the clear days of a year. | 12-16-2010 |
20110308275 | METHOD AND SYSTEM FOR PERIODIC COOLING, STORING, AND HEATING OF ATMOSPHERIC GAS - Disclosed is a method and a system. The method and system involve compressing an atmospheric gas stream to form a supercritical atmospheric gas stream, forming at least a first stream from the supercritical atmospheric gas stream, directing the first stream to a regenerator for cooling to form a first cooled stream, directing the first cooled stream from the regenerator, expanding the first cooled stream to form a liquefied atmospheric gas stream, storing at least a portion of the liquefied atmospheric gas stream, pressurizing at least a portion of the stored portion of the liquefied atmospheric gas stream, and heating at least a portion of a pressurized liquefied atmospheric gas stream in the regenerator. In the method and system, refrigeration below the critical temperature of the atmospheric gas is directly or indirectly provided to at least one portion of the system from a non-combustible source. | 12-22-2011 |
20110308276 | METHOD AND SYSTEM FOR PERIODIC COOLING, STORING, AND HEATING WITH MULTIPLE REGENERATORS - Disclosed are a method and system involving pressurizing an atmospheric gas stream to form at least a compressed atmospheric gas stream, directing the compressed atmospheric gas stream to a first regenerator for cooling, pressurizing to above a second predetermined pressure to form at least a supercritical atmospheric gas stream, directing the supercritical atmospheric gas stream to a second regenerator for cooling, reducing pressure to form at least a liquefied atmospheric gas stream, selectively storing the liquefied atmospheric gas stream, pressurizing the liquefied atmospheric gas stream to form at least a pressurized liquefied atmospheric gas stream, heating the pressurized liquefied atmospheric gas stream in the second regenerator to form at least a heated stream, expanding the heated stream to form at least a medium pressure atmospheric gas stream, directing the medium pressure atmospheric gas stream to the first regenerator, and heating the medium pressure atmospheric gas stream in the first regenerator. | 12-22-2011 |
20110308761 | REGENERATOR, REGENERATION PROCESS, AND LIQUID POLYMER MIXTURE FOR A REGENERATOR - Disclosed is a regenerator, a regeneration process, and a liquid polymer mixture for periodic cooling, storing, and heating of atmospheric gas. The regenerator, the regeneration process, and the liquid polymer mixture involve a liquid polymer that remains in contact with a thermally conductive solid material during a first operational period and a second operational period of a regeneration process. | 12-22-2011 |
20120255312 | Method and System to Produce Electric Power - An open brayton cycle power generation system is enabled and improved by integration of an energy storage system utilizing cryogenic storage of atmospheric gas. A particular improved system is an open brayton cycle power generation system in which the heating source is Concentrating Solar Power. Multiple embodiments are described which permit various modes of operation and improved overall efficiency. | 10-11-2012 |
20130219956 | He-3 Recovery From Natural Helium By Distillation - A system and method for recovering helium-3 from helium. A distillation column having a top section that is smaller in diameter than a main section is provided. The column also includes an intermediate condenser located in the main section and above a helium feed stream. Reflux to the column can be provided by liquid helium-3 from a conduit or from an overhead condenser. In a preferred cycle, the distillation column is operated at a subatmospheric pressure, and in a temperature range between 2.3 K and 4.3 K. | 08-29-2013 |
20130219958 | HE-3 RECOVERY FROM NATURAL HELIUM BY DISTILLATION - A system and method for recovering helium-3 from helium. A distillation column having a top section that is smaller in diameter than a main section is provided. The column also includes an intermediate condenser that condenses vapor from the main section and above a helium feed stream. Reflux to the column can be provided by liquid helium-3 from a conduit or from an overhead condenser. In a preferred cycle, the distillation column is operated at a subatmospheric pressure, and in a temperature range between 2.3 K and 4.3 K. | 08-29-2013 |
20130239807 | Pressure Swing Adsorption Process - A process for separating a primary gas component from a feed gas mixture comprising the primary gas component and secondary gas components in four or more adsorption beds. The process comprises subjecting each of the four or more adsorption beds to a repetitive cycle. The repetitive cycle comprises, in sequence, a feed step, a pressure decreasing equalization step, a provide purge step, a blowdown step, a purge step, a pressure increasing equalization step, and a repressurization step. During the pressure decreasing equalization step, rinse gas is co-currently introduced simultaneous with the withdrawal of pressure equalization gas. Rinse gas is formed by compressing blowdown gas and/or purge gas effluent from the adsorption bed undergoing the purge step. The process is particularly suited for separating H | 09-19-2013 |
20130243686 | Hydrogen Production Process with Low CO2 Emissions - A hydrogen production process wherein steam and a hydrocarbon feed is reacted in a prereformer, the prereformed intermediate is further reacted in an oxygen-based reformer, the reformate is shifted and then separated by a pressure swing adsorber to form a H | 09-19-2013 |
20130255492 | Adsorption Process - A process for separating a first gas, for example CO | 10-03-2013 |
20140053594 | THERMALLY ACTIVATED PRESSURE BOOSTER FOR HEAT PUMPING AND POWER GENERATION - Thermally activated systems and related processes for raising the pressure of a gaseous working fluid are described. The systems and processes can be used for both winter heating and summer cooling with increased efficiency. They can also be used for other applications in need of an efficient thermally driven compressor, such as a power generation process. | 02-27-2014 |
20140353886 | Purification, Recovery, and Recycle of Vent Gas - An apparatus and/or system and method for recycling vent gas from an autoclave is disclosed including cooling and cleaning a vent gas, introducing the cooled and cleaned resultant stream into a purification unit to remove at least a portion of the carbon dioxide and water vapor contained therein, and recycling the purified stream enriched in oxygen into the autoclave or another process requiring enriched oxygen. | 12-04-2014 |
20140373713 | Pressure Swing Adsorption Process - A pressure swing adsorption process for an adsorption system having 12 adsorption beds, the process having a cycle with 5 pressure equalization steps. Background is provided for the various pressure swing adsorption cycle steps. | 12-25-2014 |