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Небесная энциклопедия

Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

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Мониторинг СМИ

Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

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Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
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Применить Всего найдено 16059. Отображено 100.
12-01-2012 дата публикации

Sieve bed

Номер: US20120006199A1
Принадлежит: Airsep Corp

A sieve bed including an inlet end, an outlet end, a retainer disposed toward the inlet end and including an interior portion, an exterior portion, a plurality of openings disposed toward the exterior portion, and a passage disposed toward the interior portion, an inlet cap and an inlet port configured to receive a feed stream, wherein the inlet cap includes at least a portion spaced from the retainer thereby defining an inlet chamber in fluid communication with the inlet port and the plurality of openings, an outlet lid disposed toward the outlet end, an exterior wall extending from the inlet cap to the outlet lid, an intermediate wall spaced from the exterior wall and extending from the retainer toward and terminating short of the outlet lid and an interior wall spaced from the intermediate wall and extending from the retainer proximate the passage to at least the outlet lid.

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12-01-2012 дата публикации

Process for removing sulphur-containing, nitrogen-containing and halogen-containing impurities contained in a synthesis gas

Номер: US20120010306A1
Принадлежит: IFP Energies Nouvelles IFPEN

The invention relates to a process for finally removing sulphur-containing, nitrogen-containing and halogen-containing impurities contained in a synthesis gas, said process including: a) a joint step for hydrolysing COS and HCN contained in the gas and for collecting the halogen-containing compounds, using a TiO 2 -based catalyst, b) a washing step using a solvent, c) a step for desulphurisation on a collecting or adsorbing mass. The synthesis gas purified in accordance with the process of the invention contains less than 10 ppb by weight, less than 10 ppb by weight of nitrogen-containing impurities and less than 10 ppb by weight of halogen-containing impurities.

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19-01-2012 дата публикации

Separation of a Sour Syngas Stream

Номер: US20120012000A1
Принадлежит: Air Products and Chemicals Inc

A feed stream, comprising hydrogen sulphide (H 2 S), carbon dioxide (CO 2 ), hydrogen (H 2 ) and, optionally, carbon monoxide (CO), is separated into at least a CO 2 product stream and an H 2 or H 2 and CO product stream. The stream is separated using a pressure swing adsorption system, an H 2 S removal system and a further separation system, which systems are used in series to separate the stream. The method has particular application in the separation of a sour (i.e. sulphur containing) syngas, as for example produced from the gasification of solid or heavy liquid carbonaceous feedstock.

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19-01-2012 дата публикации

Membranes and Reactors for CO2 Separation

Номер: US20120014852A1
Автор: Kevin Huang
Принадлежит: UNIVERSITY OF SOUTH CAROLINA

The present disclosure relates to a system for carbon dioxide separation. The system includes a conducting membrane having two phases. The first phase is a solid oxide porous substrate. The second phase is molten carbonate. The second phase is positioned within the solid oxide porous substrate of the first phase. The system also includes a H 2 and CO 2 gas input stream separated from a CH 4 gas input stream by the conducting membrane. The CO 2 is removed from the H 2 and CO 2 gas input stream as it contacts the membrane resulting in a H 2 gas output stream from the H 2 and CO 2 gas input stream and a CO and H 2 gas output stream from the CH 4 gas input stream.

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26-01-2012 дата публикации

USE OF A TiO2- BASED COMPOSITION FOR CAPTURING HALOGENATED COMPOUNDS CONTAINED IN A GASEOUS MIXTURE

Номер: US20120020861A1
Принадлежит: Individual

The invention is concerned with the use of a TiO 2 -based composition for capturing halogenated compounds contained in a gaseous mixture, said composition comprising between 10 wt. % and 100 wt. % of TiO 2 and between 1 wt. % and 30 wt. % of at least one sulfate of an alkaline-earth metal selected from calcium, barium, strontium and magnesium.

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23-02-2012 дата публикации

Process for purifying natural gas and regenerating one or more adsorbers

Номер: US20120042689A1
Принадлежит: UOP LLC

One exemplary embodiment can be a process for purifying a natural gas by using first and second adsorbers. The process may include passing a feed including the natural gas through the first adsorber to obtain a purified natural gas product, regenerating the second adsorber in a heating stage, and regenerating the second adsorber in a cooling stage. The heating stage may include separating a portion of the feed comprised in a regeneration gas, passing the regeneration gas to a dryer for removing water, heating the regeneration gas with a heater after exiting the dryer, and passing the regeneration gas to the second adsorber to regenerate the second adsorber. The cooling stage may include expelling at initiation of cooling at least a part of a fluid present in the second adsorber to the dryer to desorb water from a molecular sieve in the dryer, and cooling the second adsorber by circulating the regeneration gas bypassing the heater.

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08-03-2012 дата публикации

Oxygen concentrator system and methods for oral delivery of oxygen enriched gas

Номер: US20120055475A1
Автор: William R. Wilkinson
Принадлежит: Inova Labs Inc

Described herein are various embodiments of an oxygen concentrator system. In some embodiments, an oxygen concentrator system may be used to provide oxygen enriched gas to a patient using a mouthpiece.

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08-03-2012 дата публикации

Process for producing a purified synthesis gas stream

Номер: US20120058921A1
Принадлежит: Individual

A process for producing a purified synthesis gas stream from a feed synthesis gas stream comprising besides the main constituents carbon monoxide and hydrogen also hydrogen sulphide, HCN and/or COS, the process comprising the steps of: (a) removing HCN and/or COS by contacting the feed synthesis gas stream with a catalyst in a HCN/COS reactor in the presence of steam/water, to obtain a synthesis gas stream depleted in HCN and/or in COS; (b) converting hydrogen sulphide in the synthesis gas stream depleted in HCN and/or in COS to elemental sulphur, by contacting the synthesis gas stream with an aqueous reactant solution containing solubilized Fe(III) chelate of an organic acid, at a temperature below the melting point of sulphur, and at a sufficient solution to gas ratio and conditions effective to convert H 2 S to sulphur and inhibit sulphur deposition, to obtain a synthesis gas stream depleted in hydrogen sulphide; (c) removing carbon dioxide from the synthesis gas stream depleted in hydrogen sulphide, to obtain the purified synthesis gas stream and a gas stream enriched in CO 2 .

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15-03-2012 дата публикации

Method and apparatus for removing contaminant from fluid

Номер: US20120063981A1
Принадлежит: ExxonMobil Research and Engineering Co

Methods, apparatus, and systems for removing contaminant in a fluid (e.g., chemical and petrochemical gas streams) using nanostructures of a sorbent material coated on plates such as a silicon wafer. A plurality of such coated plates can be assembled to form a sorption structure having channels between the plates. When a fluid containing the contaminant is directed through the channels, the contaminant is adsorbed by the nanostructures of the sorbent material.

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29-03-2012 дата публикации

Hydrogen sulfide conversion to hydrogen

Номер: US20120076721A1
Автор: James A. Wasas
Принадлежит: SWAPSOL Corp

A process and system for substantially eliminating contaminants from a gas and a gas produced therefrom.

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26-04-2012 дата публикации

Chemical looping air separation unit and methods of use

Номер: US20120100055A1
Автор: Justin M. Weber
Принадлежит: Individual

The disclosure provides for oxygen separation from air by utilizing an initial oxygen carrier which undergoes an endothermic reduction reaction to produce a carrier product and gaseous oxygen. The gaseous oxygen is withdrawn, and the carrier product is subsequently further reduced with a fuel in a combustion process, releasing heat and generating a oxygen acceptor. The oxygen acceptor is oxidized in an exothermic reaction. The method thus couples the exothermic oxidation reaction, the endothermic reduction reaction, and the chemical energy supplied by the fuel for a net heat release. In an embodiment, the initial oxygen carrier is CuO, the carrier product is Cu 2 O, and the oxygen acceptor is Cu.

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26-04-2012 дата публикации

Dynamic hydrogen-storage apparatus and the method thereof

Номер: US20120100065A1
Принадлежит: Institute of Nuclear Energy Research

This invention provides a dynamic hydrogen-storage apparatus and the method thereof, which includes the following steps: (a) filling a container with a porous hydrogen-storage material which is loaded or doped with a catalyst; (b) setting an operational pressure and a pressure drop for the operation of storing hydrogen; (c) providing the hydrogen-storage material with a hydrogen so as to increase the pressure of the hydrogen to the operational pressure; (d) decreasing the pressure of the hydrogen by the pressure drop; and (e) repeating steps (c) and (d) for a predetermined amount of times.

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03-05-2012 дата публикации

Method for the direct amination of hydrocarbons into amino hydrocarbons, including electrochemical separation of hydrogen and electrochemical reaction of the hydrogen into water

Номер: US20120107707A1
Принадлежит: BASF SE

Process for the direct amination of hydrocarbons to aminohydrocarbons by reaction of a feed stream E comprising at least one hydrocarbon and at least one aminating reagent to form a reaction mixture R comprising aminohydrocarbon and hydrogen in a reaction zone RZ and electrochemical separation of at least part of the hydrogen formed in the reaction from the reaction mixture R by means of a gastight membrane-electrode assembly having at least one selectively proton-conducting membrane and at least one electrode catalyst on each side of the membrane, where at least part of the hydrogen is oxidized to protons at the anode catalyst on the retentate side of the membrane and the protons pass through the membrane and on the permeate side are reacted with oxygen to form water, where the oxygen originates from an oxygen-comprising stream O which is brought into contact with the permeate side of the membrane, over the cathode catalyst.

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14-06-2012 дата публикации

Process For Reducing Contaminants In An Industrial Fluid Stream

Номер: US20120145001A1
Принадлежит: Individual

This invention provides novel processes utilizing compositions comprising substituted polyamines as acid gas scrubbing solutions and methods of using the compositions in an industrial system. The invention relates to the use of such polyamine compounds in industrial processes to remove acidic contaminants from natural and industrial fluid streams, such as natural gas, combustion gas, natural gas, synthesis gas, biogas, and other industrial fluid streams. The compositions and methods of the invention are useful for removal, absorption, or sequestration of acidic contaminants and sulfide contaminants including CO 2 , H 2 S, RSH, CS 2 , COS, and SO 2 .

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21-06-2012 дата публикации

Rotary fluid processing systems and associated methods

Номер: US20120152116A1
Принадлежит: Prometheus Technologies LLC

Rotary fluid processing systems and associated methods are disclosed. A purification system in accordance with the particular embodiment includes a rotatable adsorbent-containing heat/mass transfer element that is generally symmetric about a rotation axis, and includes multiple radial flow paths oriented transverse to the rotation axis and multiple axial flow paths oriented transverse to the radial flow paths. The axial flow paths and radial flow paths are in thermal communication with each other, and are generally isolated from fluid communication with each other at the heat transfer element. Particular embodiments can further include a housing arrangement having multiple manifolds with individual manifolds having an entry port and an exit port, and with individual manifolds having different circumferential locations relative to the rotation axis. Still further embodiments can include a seal arrangement positioned between the heat transfer element and the housing arrangement to expose the radial flow paths, but not the axial flow paths, to the entry and exit ports of one of the manifolds, and expose the axial flow paths, but not the radial flow paths, to the entry and exit ports of another of the manifolds.

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09-08-2012 дата публикации

Membrane Element, Gas Separation Device and Internal Combustion Engine

Номер: US20120199004A1
Принадлежит: Individual

The present invention provides a membrane element, a gas separation device, and an internal combustion engine capable of improving gas separation performance. A gas separation device 1 including membrane elements 2 includes rigid members 32 arranged in a direction intersecting folds of a pleated structure 26 in open regions R 1 and R 2 of the pleated structure 26 surrounded by a reinforcement frame 27 . The open regions R 1 and R 2 are each separated into a supply region and an exhaust region of gas by an elastic epoxy resin adhesive S provided between the rigid member 32 and the pleated structure 26.

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30-08-2012 дата публикации

Carbon Dioxide Permeable Membrane

Номер: US20120219483A1
Принадлежит: Columbia University of New York

A carbon dioxide permeable membrane is described. In some embodiments, the membrane includes a body having a first side and an opposite second side; a plurality of first regions formed from a molten carbonate having a temperature of about 400 degrees Celsius to about 1200 degrees Celsius, the plurality of first regions forming a portion of the body and the plurality of first regions extending from the first side of the body to the second side of the body; a plurality of second regions formed from an oxygen conductive solid oxide, the plurality of second regions combining with the plurality of first regions to form the body and the plurality of second regions extending from the first side of the body to the second side of the body; and the body is configured to allow carbon dioxide to pass from the first side to the second side.

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06-09-2012 дата публикации

Swing Adsorption Processes Utilizing Controlled Adsorption Fronts

Номер: US20120222551A1
Автор: Harry W. Deckman
Принадлежит: ExxonMobil Research and Engineering Co

A process for reducing the loss of valuable products by improving the overall recovery of a contaminant gas component in swing adsorption processes. The present invention utilizes at least two adsorption beds, in series, with separately controlled cycles to control the adsorption front and optionally to maximize the overall capacity of a swing adsorption process and to improve overall recovery a contaminant gas component from a feed gas mixture.

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06-09-2012 дата публикации

Pressure-Temperature Swing Adsorption Process for the Separation of Heavy Hydrocarbons from Natural Gas Streams

Номер: US20120222552A1
Принадлежит: ExxonMobil Research and Engineering Co

The present invention relates to a pressure-temperature swing adsorption process wherein gaseous components that have been adsorbed can be recovered from the adsorbent bed at elevated pressures. In particular, the present invention relates to a pressure-temperature swing adsorption process for the separation of C 2+ hydrocarbons (hydrocarbons with at least 2 carbon atoms) from natural gas streams to obtain a high purity methane product stream. In more preferred embodiments of the present processes, the processes may be used to obtain multiple, high purity hydrocarbon product streams from natural gas stream feeds resulting in a chromatographic-like fractionation with recovery of high purity individual gaseous component streams.

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06-09-2012 дата публикации

Gas Purification Process Utilizing Engineered Small Particle Adsorbents

Номер: US20120222555A1
Принадлежит: ExxonMobil Research and Engineering Co

A gas separation process uses a structured particulate bed of adsorbent coated shapes/particles laid down in the bed in an ordered manner to simulate a monolith by providing longitudinally extensive gas passages by which the gas mixture to be separated can access the adsorbent material along the length of the particles. The particles can be laid down either directly in the bed or in locally structured packages/bundles which themselves are similarly oriented such that the bed particles behave similarly to a monolith but without at least some disadvantages. The adsorbent particles can be formed with a solid, non-porous core with the adsorbent formed as a thin, adherent coating on the exposed exterior surface. Particles may be formed as cylinders/hollow shapes to provide ready access to the adsorbent. The separation may be operated as a kinetic or equilibrium controlled process.

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06-09-2012 дата публикации

Systems and methods for gas treatment

Номер: US20120222556A1
Принадлежит: Blue Zone Tech Ltd

A system and process for the recovery of at least one halogenated hydrocarbon from a gas stream. The recovery includes adsorption by exposing the gas stream to an adsorbent with a lattice structure having pore diameters with an average pore opening of between about 5 and about 50 angstroms. The adsorbent is then regenerated by exposing the adsorbent to a purge gas under conditions which efficiently desorb the at least one adsorbed halogenated hydrocarbon from the adsorbent. The at least one halogenated hydrocarbon (and impurities or reaction products) can be condensed from the purge gas and subjected to fractional distillation to provide a recovered halogenated hydrocarbon.

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20-09-2012 дата публикации

Methods for controlling impurity buildup on adsorbent for pressure swing adsorption processes

Номер: US20120234165A1
Принадлежит: UOP LLC

Embodiments of methods for controlling impurity buildup on adsorbent for a pressure swing adsorption (PSA) process are provided. The method comprises the steps of operating the PSA process including performing (a) a first depressurizing equalization step, and (b) a providing purge step. Impurities are sensed in an effluent from the PSA process. If the impurities sensed in the effluent have reached a predetermined upper impurity level, then the PSA process is operated including performing (b) and not (a).

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27-09-2012 дата публикации

Method and device for treating a carbon-dioxide-containing gas flow, wherein the energy of the vent gas (work and cold due to expansion) is used

Номер: US20120240619A1
Принадлежит: Linde KCA Dresden GmbH

The invention relates to a method and a device for treating a carbon-dioxide-containing gas stream, in particular from a large-scale fired plant, e.g. from a power plant. The precompressed gas stream is separated in a carbon dioxide purification stage into a gas substream having an elevated carbon dioxide content (carbon dioxide product stream) and a gas substream having a decreased carbon dioxide content (vent gas stream). The carbon dioxide product stream is fed to further utilization and/or storage. In particular, by injecting the carbon dioxide underground, the emission of gases harmful to the climate can be reduced. For improving the energy efficiency, it is proposed that the vent gas stream is expanded in at least one expansion turbine and both the resultant kinetic energy and the resultant refrigeration are utilized for energy recovery. For utilizing the kinetic energy, the expansion turbine can be coupled to a compressor (booster) which compresses the crude gas stream and/or the carbon dioxide product stream. For utilizing the refrigeration generated in the expansion, the at least partially expanded vent gas stream can be brought into heat exchange with process streams which are to be cooled, e.g. the crude gas stream and/or the carbon dioxide product stream.

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11-10-2012 дата публикации

Control method and apparatus

Номер: US20120255436A1
Принадлежит: Praxair Technology Inc

A method and apparatus for controlling the electrical power applied to an electrically driven oxygen separation device having one or more composite membrane elements to separate oxygen from an oxygen containing feed. The composite membrane elements have a resistance increasing during the operation thereof that would act to reduce oxygen output if applied voltage were held constant. In order to increase the time interval for renewing the composite membrane elements, the electrical potential difference is controlled such that the electric current drawn by the elements remains at a substantially constant level by increasing the electrical potential difference as the resistance increases until a predetermined voltage level is reached. Once this level is obtained, the electrical potential difference is maintained at a constant level and the electric current being drawn and the oxygen output is allowed to decay to a predetermined low level after which the element or elements are replaced.

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25-10-2012 дата публикации

Gas concentrator with removable cartridge adsorbent beds

Номер: US20120266883A1
Принадлежит: Inogen Inc

portable oxygen concentrator designed for medical use where the sieve beds, adsorbers, are designed to be replaced by a patient. The concentrator is designed so that the beds are at least partially exposed to the outside of the system and can be easily released by a simple user-friendly mechanism. Replacement beds may be installed easily by patients, and all gas seals will function properly after installation.

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01-11-2012 дата публикации

Oxygen enrichment device

Номер: US20120272966A1
Принадлежит: Teijin Pharma Ltd

Disclosed is an oxygen enrichment that can follow changes in adsorption performance in response to changes in the temperature of the usage environment and can reduce power consumption. The oxygen enrichment device has a purge step control means that controls a purge step time to increase/decrease the length of a purge step so as to maximize the oxygen concentration by changing opening/closing timing of a flow-channel switching means while the oxygen enrichment device is running.

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22-11-2012 дата публикации

Process For The Production Of Hydrogen And Carbon Dioxide

Номер: US20120291485A1

This present invention provides a method to more efficiently recover hydrogen and carbon dioxide, preferably at least 50%, even more preferably at least 75%, and most preferably at least 90% of the carbon dioxide. The present invention further provides the design for capture of at least 80%, carbon dioxide from syngas that allows for the simultaneous production of medium to high amounts of hydrogen in the syngas as a part of the production of hydrogen in a hydrogen generation plant. By using the process of the present invention, especially in terms of a hydrogen generation plant, it is possible to increase recovery of hydrogen and capture of the carbon dioxide in the syngas stream by balancing the recycle of the hydrogen rich permeate from the hydrogen membrane separation units to the process unit and/or the water gas shift as capacity allows when a carbon dioxide separation unit, a carbon dioxide membrane separation unit and two hydrogen membrane separation units are utilized.

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13-12-2012 дата публикации

Apparatus for generating hydrocarbon fuel

Номер: US20120315193A1
Автор: Bayne Carew
Принадлежит: Individual

An apparatus suitable for generating gaseous hydrocarbon fuel from a carbon based synthesis gas including a reaction chamber having a rotating shaft including a plurality of radial blades mixing and circulating carbon based synthesis gas and particulate catalyst upwardly generating gaseous hydrocarbon fuel, a stripping chamber located above the reaction chamber having a second axial rotating shaft including a plurality of radial blades driving hydrocarbon fuel radially outwardly, a source of hot stripping gas, an annular filter surrounding the stripping chamber and an annular gas collection chamber surrounding the filter. The blades in the stripping chamber are rotated independently at a greater velocity than the blades in the reaction chamber and the reaction is controlled by the temperature of the synthesis gas and the rotational velocity of the mixing blades in the reaction chamber.

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20-12-2012 дата публикации

Oxygen separation membrane

Номер: US20120318145A1
Принадлежит: KONINKLIJKE PHILIPS ELECTRONICS NV

The invention relates to membranes, in particular oxygen separation membranes, which enable improved gas separation conditions with respect to cost, price, size, weight, and noise. The membrane, in particular oxygen separation membrane, according to the invention comprises a support layer ( 28 ) and a separation layer ( 30 ), wherein the separation layer ( 30 ) is permeable for oxygen and has a sorptive affinity for at least one other gas, in particular for nitrogen, wherein the membrane ( 20 ) is designed such that substantially only the separation layer ( 30 ) is heatable by a heating device.

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03-01-2013 дата публикации

Method for the adsorptive drying of purified biogas and for regenerating laden adsorbents

Номер: US20130000486A1
Автор: Lothar Guenther
Принадлежит: DGE Dr Ing Guenther Engineering GmbH

In a method for adsorptively drying purified biogas and regenerating laden absorbents, foreign matter is not allowed to enter the purified biogas, the content of methane in the gas remains virtually unchanged and the effort involved in regenerating the laden adsorbent is reduced. Drying and regeneration are effected in a closed biogas cycle, wherein separate layers based on silica gel and molecular sieves are used as the adsorbent. The biogas to be dried first flows through the silica gel layer. The adsorbent is regenerated with exclusively heated, dried biomethane having a temperature of up to 150° C. which, after contact with adsorbent, is recirculated to the outflow of purified biogas. After regeneration, the bed is cooled by biomethane, which is subsequently recirculated to the outflow of purified biogas. Methane-containing water accumulating during drying and regeneration is recirculated to the biogas generation and/or purification.

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10-01-2013 дата публикации

Oxygen concentrator

Номер: US20130008438A1
Принадлежит: Ikiken Co Ltd, Terumo Corp

To provide an oxygen concentrator that can ensure safety by interrupting oxygen in a case where the oxygen concentrator is exposed to fire or an abnormal high-temperature environment when a user thereof is inhaling oxygen with a cannula. The oxygen concentrator includes: a compressor separating compressed air by compressing raw air; an oxygen outlet for discharging oxygen acquired from the compressed air; a coupler mounted on a tube of a cannula and removably connecting the tube to the oxygen outlet, and moreover having a temperature sensor; and a control unit stopping operation of the compressor to interrupt the supply of oxygen when a temperature sensed by the temperature sensor reaches a predetermined temperature or higher.

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24-01-2013 дата публикации

System and Method for Separation of Captured Gases from Exhaust

Номер: US20130019753A1
Автор: Cornel Gleason
Принадлежит: JAGS LLC

In one example, we discuss the separation of the captured gases as byproducts, for future/other purposes, coming from conventional power generators or factories or from algae biofuel production facility (or any other similar sources). This increases the energy production, saves the environment, conserves the resources, improves the air quality, reduces the global warming, increases water supply, reduces the cost, and improves agriculture and food resources, around the globe. In one example, we discuss the biofuel production, method, and system.

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07-02-2013 дата публикации

Oxygen Concentrator Having Structural Sieve Beds

Номер: US20130031784A1
Принадлежит: Invacare Corp

Embodiments of oxygen concentrators having a sieve bed that includes a vessel filled with a separation medium are disclosed. The sieve bed vessel at least partially supports one chassis component of the oxygen concentrator with respect to another chassis component. of the oxygen concentrator.

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21-02-2013 дата публикации

Zn5(BTA)6(TDA)2 - A ROBUST HIGHLY INTERPENETRATED METAL-ORGANIC FRAMEWORK CONSTRUCTED FROM PENTANUCLEAR CLUSTERS FOR SELECTIVE SORPTION OF GAS MOLECULES

Номер: US20130043407A1
Принадлежит: University of Texas System

Disclosed herein are highly interpenetrated robust metal-organic frameworks having the repeat unit Zn 5 (BTA) 6 (TDA) 2 , useful for applications such as selective gas storage, selective gas sorption and/or separation, and gas detection.

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28-02-2013 дата публикации

Method and apparatus for the supply of dry gases

Номер: US20130047848A1
Принадлежит: Air Products and Chemicals Inc

A built in purifier for a cylinder of essentially nitrogen free gas having a low water content is provided with a molecular sieve 3A adsorbent to adsorb water from the gas, the 3A adsorbent having a particularly low adsorption capacity for nitrogen.

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28-02-2013 дата публикации

Gas separations with redox-active metal-organic frameworks

Номер: US20130053585A1
Принадлежит: UNIVERSITY OF CALIFORNIA

Fe 2 (dobdc) has a metal-organic framework with a high density of coordinatively-unsaturated Fe II centers lining the pore surface. It can be effectively used to separate O 2 from N 2 and in a number of additional separation applications based on selective, reversible electron transfer reactions. In addition to being an effective O 2 separation material, it can be used for many other processes, including paraffin/olefin separation, nitric oxide/nitrous oxide separation, acetylene storage, and as an oxidation catalyst.

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07-03-2013 дата публикации

Membrane Separation Apparatus for Fuel Gas Conditioning

Номер: US20130055897A1
Автор: Kaaeid A. Lokhandwala
Принадлежит: Membrane Technology and Research Inc

Disclosed herein is a membrane separation apparatus that includes an integrated filter element. The apparatus is useful in the conditioning of fuel gas to separate methane from C 2+ hydrocarbons.

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07-03-2013 дата публикации

Production of magnesium metal

Номер: US20130056916A1
Принадлежит: Individual

A process of producing magnesium metal includes providing magnesium carbonate, and reacting the magnesium carbonate to produce a magnesium-containing compound and carbon dioxide. The magnesium-containing compound is reacted to produce magnesium metal. The carbon dioxide is used as a reactant in a second process. In another embodiment of the process, a magnesium silicate is reacted with a caustic material to produce magnesium hydroxide. The magnesium hydroxide is reacted with a source of carbon dioxide to produce magnesium carbonate. The magnesium carbonate is reacted to produce a magnesium-containing compound and carbon dioxide. The magnesium-containing compound is reacted to produce magnesium metal. The invention also relates to the magnesium metal produced by the processes described herein.

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14-03-2013 дата публикации

Carbon Dioxide Recovery System

Номер: US20130064720A1
Принадлежит: HITACHI LTD

A carbon dioxide recovery system is provided, in which, a filling rate of the carbon dioxide sorbent in the container indicated by f [%] is positive and larger than or equal to the value obtained by the following expression of 100×(p/(RT))×(x−C)/(a×(100+x/r−100×x/(rC)−x)+(p/(RT))×(x−C)), with respect to the effective molar quantity of the captured carbon dioxide per 1 L of the carbon dioxide sorbent (=a) of the carbon dioxide sorbent to be used, wherein a demanded concentration of recovered carbon dioxide is indicated by x [%], and an amount of the captured gases other than carbon dioxide is indicated by r, and a concentration of dried carbon dioxide in a carbon dioxide-containing gas is indicated by C [%], and a total pressure of the carbon dioxide sorbent occurring when carbon dioxide is captured is indicated by p [Pa].

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21-03-2013 дата публикации

Method and device for the absorptive removal of carbon dioxide from biogas

Номер: US20130071307A1
Принадлежит: MT Biomethan GmbH

The absorptive removal of carbon dioxide from biogas using a scrubbing liquid in which carbon dioxide is chemically bound proceeds by heating the loaded scrubbing liquid, occurring after the absorption, to a temperature at which liberation of CO 2 begins. Immediately thereafter, the loaded scrubbing liquid is fed to at least one centrifugal separator for separating off the gas phase from the liquid phase, wherein methane and dissolved fractions of CO 2 escape via the gas phase. After separation is complete, the gas phase is passed into the absorber unit and the liquid phase is further heated to the temperature required for desorption and fed to the desorption unit for regeneration.

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28-03-2013 дата публикации

Device for the adsorption treatment of a fluid or fluid stream

Номер: US20130074689A1
Принадлежит: Clariant Produkte Deutschland GmbH

A device for adsorption treatment of a fluid or fluid stream, comprising a container for receiving adsorber material, wherein the container has a fluid inlet opening and a fluid outlet opening, and two fluid connection devices, wherein one of the fluid connection devices is provided at the fluid inlet opening and the other one of the fluid connection devices is provided at the fluid outlet opening, wherein the fluid connection devices are locked in a fluid-tight manner and are designed in such a way that they can each be connected to a fluid line connector and unlocked and, if they are connected to the respective fluid line connector they can be unlocked or are unlocked.

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25-04-2013 дата публикации

Exhaust Gas Treating System Using Polymer Membrane For Carbon Dioxide Capture Process

Номер: US20130098246A1
Принадлежит: Korea Institute of Energy Research KIER

Disclosed is an exhaust gas treating system having an exhaust gas treating apparatus for carbon dioxide capture process which additionally removes harmful substances remaining in the gas discharged from the existing flue-gas desulfurization process by using separation membrane so as to efficiently carry out the carbon dioxide capture process. The exhaust gas treating system using polymer membrane, comprises a carbon dioxide capture equipment for capturing carbon dioxide from the exhaust gas of a boiler, a flue-gas denitrification equipment placed between the boiler and the carbon dioxide capture equipment, a dust-collecting equipment and a flue-gas desulfurization equipment.

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02-05-2013 дата публикации

Method and system for capturing carbon dioxide in an oxyfiring process where oxygen is supplied by regenerable metal oxide sorbents

Номер: US20130108518A1
Автор: Raja Ankush Jadhav
Принадлежит: Chevron USA Inc

An oxyfiring system is disclosed. The oxyfiring system comprises (a) an oxidation reactor for oxidizing a reduced metal oxide; (b) a decomposition reactor wherein a decomposition fuel is combusted and oxidized metal oxide sorbents are reduced with oxygen being released and a flue gas with an oxygen enriched carbon dioxide stream is produced; (c) a fuel combustion reactor for combusting a primary fuel and the oxygen enriched carbon dioxide stream into a primary flue gas; and (d) separation apparatus for separating a portion of the primary flue gas so that a carbon dioxide enriched stream can be prepared.

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09-05-2013 дата публикации

Carbon Dioxide Purification

Номер: US20130111949A1
Принадлежит: Lummus Technology Inc

A process for the recovery of carbon dioxide from a gas mixture that includes pretreating a gas mixture comprising carbon dioxide, water vapor, and one or more light gases in a pretreating system to form a cooled gas mixture, fractionating the cooled gas mixture to recover a bottoms fraction comprising carbon dioxide and an overheads fraction comprising carbon dioxide and the light gases, passing the overheads fraction over a membrane selective to carbon dioxide to separate a carbon dioxide permeate from a residue gas comprising the light gases, recycling the carbon dioxide permeate to the pretreating system, and recovering at least a portion of the bottoms fraction as a purified carbon dioxide product stream is described.

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06-06-2013 дата публикации

Hydrogen production system and method of controlling flow rate of offgas in the system

Номер: US20130139684A1
Принадлежит: Sumitomo Seika Chemicals Co Ltd

A hydrogen manufacturing system for performing offgas flow control includes: a vaporizer ( 1 ) for heating a material mixture containing a hydrocarbon material; a reforming reactor ( 2 ) for generating hydrogen-containing reformed gas by reforming reactions of the material; a PSA separator ( 5 ) for repeating a cycle of adsorption and desorption, where in the adsorption PSA separation is performed with an adsorption tower loaded with an adsorbent to adsorb unnecessary components in the reformed gas and extract hydrogen-enriched gas out of the tower, and in the desorption the offgas containing the unnecessary components from the adsorbent and remaining hydrogen is discharged from the tower; and a buffer tank ( 6 ) for holding the offgas before supplying to the vaporizer. The offgas flow supply from the tank ( 6 ) to the vaporizer is changed continuously over time when the cycle time is changed according to load change on the separator ( 5 ).

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04-07-2013 дата публикации

Power plant

Номер: US20130167557A1
Принадлежит: General Electric Co

A power plant includes a compressor configured to compress inlet air for combustion. The power plant also includes an air separation unit configured to receive and remove nitrogen from an air supply. The power plant further includes a fluid manipulator operably coupled to the air separation unit and the compressor, wherein the fluid manipulator is configured to receive nitrogen removed from the air separation unit at an inlet pressure and an inlet temperature and produce a modified pressure and a modified temperature of the nitrogen prior to selectively delivering the nitrogen to the compressor.

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01-08-2013 дата публикации

Process for separating co2 from a gaseous stream

Номер: US20130195744A1
Принадлежит: VTU HOLDING GMBH

Process for separating CO 2 from a gaseous stream by chemisorption to 1-ethyl-3-methylimidazolium (emim) or 1-propyl-3-methylimidazolium (pmim), characterized in that emim or pmim are present as carboxylate salt and that chemisorption is carried out in the presence of guanidinium acetate or 1-butyl-3-methylimidazolium (bmim) acetate.

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15-08-2013 дата публикации

Method and device for vacuum pressure swing adsorption with temporary storage

Номер: US20130206004A1
Автор: Matthias Grahl
Принадлежит: Linde GmbH

Adsorptive decomposition of a gas mixture is performed by vacuum pressure swing adsorption. The gas mixture is condensed to the adsorption pressure by means of at least one condenser prior to being fed into the vacuum pressure swing adsorption process. Regeneration of the adsorber(s) is carried out by means of at least one vacuum pump. The condensed gas mixture ( 1, 5, 6 ) is at least periodically and/or at least partially temporarily stored (S1) and/or fed to a consumer at those times when no gas mixture is being fed to the vacuum pressure swing adsorption process; and/or at least one of the vacuum pumps (P) that is not required for the regeneration is used at least occasionally for another application at those times when no regeneration of the adsorber or an adsorber (A, A′) is being carried out.

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15-08-2013 дата публикации

Production of high purity butene-1 from c4 olefins/paraffins mixed gas

Номер: US20130206575A1

A hybrid process comprising an adsorption process and a distillation process for the separation of butene-1 from a C4 hydrocarbon mixture gas including butene-1, trans-2-butene, cis-2-butene, normal butane, isobutane, etc. is provided. The hybrid process comprises introducing a gaseous C4 mixture into the adsorption tower loaded with adsorbents which adsorb olefins selectively to discharge C4 paraffins to the outlet of the tower, desorbing C4 olefins selectively adsorbed in the adsortion tower to produce high purity C4 olefins mixture gas in which isobutane and normal butane was removed, and separating the high C4 olefins mixture gas (a mixture of butene-1, trans-2-butene, cis-2-butene, and a trace amount of C4 paraffins) via distinction to obtain high purity butene-1 including a trace amount of isobutane in the top of the distillation tower and obtain a mixture gas including trans-2-butene, cis-2-butene and a trace amount of normal butane in the bottom of the tower.

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19-09-2013 дата публикации

Membrane-Based Gas Separation Process Using Ejector-Driven Gas Recycle

Номер: US20130239804A1
Принадлежит: Membrane Technology and Research Inc

Disclosed herein is a gas separation process that utilizes ejector recycle with a membrane separation step in combination with a second separation step. The second separation step may be a second membrane separation step, or may involve a different type of separation process.

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17-10-2013 дата публикации

Final biogas purification process

Номер: US20130269523A1
Принадлежит: Individual

The present invention relates to a process for the purification by adsorption of a feed flow rich in methane and comprising at least carbon dioxide.

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24-10-2013 дата публикации

Method for processing fischer-tropsch off-gas

Номер: US20130276630A1
Принадлежит: Shell Oil Co

A method for producing a gas comprising at least 80 vol % carbon monoxide from a Fischer-Tropsch off-gas comprises: (1) feeding Fischer-Tropsch off-gas through a column comprising an adsorbent bed at high pressure and discharging effluent; (2) reducing the pressure in the column and the bed slightly; (3) rinsing the column and the adsorbent bed with methane or a mixture of methane and carbon dioxide; (4) reducing the pressure of the column and adsorbent bed to a low pressure; (5) rinsing the column and adsorbent bed with a mixture of hydrogen and nitrogen; (6) pressurizing the column and adsorbent bed to a high pressure using a mixture of hydrogen and nitrogen. The product stream obtained in step (3) comprising at least 80 vol % carbon monoxide can be sent as feed to a Fischer-Tropsch reaction. In an embodiment, a gas comprising at least 80 vol % hydrogen is also produced.

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14-11-2013 дата публикации

Method for drying a wet co2 rich gas stream from an oxy-combustion process

Номер: US20130298599A1
Принадлежит: Alstom Technology AG

A method for drying a wet CO 2 rich gas stream from an oxy-combustion process that includes: compressing the wet CO 2 rich gas stream to a drying process operating pressure, cooling the wet CO 2 rich gas stream in at least one cooler, alternately drying the wet CO 2 rich gas stream in at least one dryer which contains at least one desiccant bed and regenerating the desiccant bed by conducting a heated regenerating gas through the dryer in opposite direction to the flow direction of the wet CO 2 rich gas stream, separating the dried CO 2 rich gas stream in a purification process to a purified CO 2 gas stream and a waste gas stream rich in nitrogen and oxygen, whereby the waste gas stream rich in nitrogen and oxygen is used as regenerating gas, and subsequently to the regeneration the dryer is purged at least once by a pressurized CO 2 rich gas stream conducted from the compressor, and whereby the dryer is charged up to the drying process operating pressure with a pressurized CO 2 rich gas stream conducted from the compressor before each drying process.

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21-11-2013 дата публикации

Method for producing carbon molecular sieve membranes in controlled atmospheres

Номер: US20130305921A1
Принадлежит: Georgia Tech Research Corp, Shell Oil Co

The invention concerns carbon molecular sieve membranes (“CMS membranes”), and more particularly the use of such membranes in gas separation. In particular, the present disclosure concerns an advantageous method for producing CMS membranes with desired selectivity and permeability properties. By controlling and selecting the oxygen concentration in the pyrolysis atmosphere used to produce CMS membranes, membrane selectivity and permeability can be adjusted. Additionally, oxygen concentration can be used in conjunction with pyrolysis temperature to further produce tuned or optimized CMS membranes.

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19-12-2013 дата публикации

Method and arrangement for generating oxygen

Номер: US20130333563A1
Принадлежит: Koninklijke Philips NV

The invention relates to a method of generating oxygen. The method comprises the steps of: intermittently guiding a stream of oxygen comprising gas through at least one adsorption chamber ( 12 ) being equipped with an oxygen separation adsorbent ( 16 ), thereby defining an adsorption mode and a desorption mode of the at least one adsorption chamber ( 12 ), and thereby enriching the oxygen comprising gas with respect to oxygen, guiding the enriched oxygen comprising gas to a primary side of a dense membrane ( 52 ), heating the dense membrane( 52 ) to a temperature at which it is permeable for oxygen, generating an oxygen flow through the dense membrane ( 52 ) to its secondary side, thereby separating the oxygen from the enriched oxygen comprising gas and forming a stream of oxygen. According to the invention, the invention further comprises the step of guiding at least a part of the generated oxygen through the at least one adsorption chamber ( 12 ) being in desorption mode. The method according to the invention allows generating oxygen in a high purity, thereby being energy saving, cost saving and being performable in a compact device.

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19-12-2013 дата публикации

Hydrogen separation device

Номер: US20130333569A1

The hydrogen separation device comprises a laminate formed by laminating and integrating a hydrogen separation layer, a mixed gas layer kept adjacent to one surface of the hydrogen separation layer and having a mixed gas flow path, and a transmitted gas layer kept adjacent to the other surface of the hydrogen separation layer and having a transmitted gas flow path, and a vessel containing the laminate therein and filled with a buffer gas, wherein a buffer space is provided between the laminate and the inner wall of the vessel in which a buffer gas can reach at least one end face of the laminate in the lamination direction, and wherein the pressure in the buffer space is equal to or higher than the higher one of the pressure in the mixed gas flow path and the pressure in the transmitted gas flow path.

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26-12-2013 дата публикации

Capture mass composed of elemental sulphur deposited on a porous support for capturing heavy metals

Номер: US20130341564A1
Принадлежит: IFP Energies Nouvelles IFPEN

The present invention concerns the elimination of heavy metals, in particular mercury and possibly arsenic and lead, present in a dry or moist gaseous effluent ( 1 ) by means of a capture mass ( 2 ) comprising a porous support at least part of which is of low mesoporosity and an active phase based on sulphur. The invention is advantageously applicable to the treatment of gas of industrial origin, synthesis gas or natural gas.

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02-01-2014 дата публикации

Gas scrubber and related processes

Номер: US20140005352A1
Принадлежит: Invista North America LLC

The invention relates to a method for producing a high molecular weight polyethylene terephthalate (PET) via a solid state polymerization system. The method comprises using an acid catalyst to effectuate the conversion of acetaldehyde present within the system to 2-methyl-1,3-dioxolane, which can be readily removed. The invention also relates to PET prepared via this process, which can advantageously exhibit low levels of acetaldehyde.

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16-01-2014 дата публикации

Thermal Conditioning for Air Separation Modules

Номер: US20140013951A1
Принадлежит: Carleton Life Support Systems Inc

Thermal conditioning for an area surrounding one or more air separation canisters includes directing the exhaust gas of the thermal conditioning unit to the area surrounding the canisters. The area may be defined by a housing in which the canisters are positioned.

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16-01-2014 дата публикации

Oxygen tank unit for oxygen enricher

Номер: US20140013954A1
Автор: Michiya Sato
Принадлежит: FUJIKURA RUBBER LTD

An oxygen-enricher oxygen tank unit includes a single oxygen tank body, to which a pair of nitrogen absorption containers, which alternately receive a supply of compressed air, are connected; a check valve provided between each of the pair of nitrogen absorption containers and the oxygen tank body, wherein each check valve allows gas to flow from an associated nitrogen absorption container to the oxygen tank body, and does not allow gas to flow in a reverse direction thereto; and a pressure-reducing valve, having an oxygen outlet, which is connected to the oxygen tank body. At least one of the pressure-reducing valve and a pair of nitrogen absorption container connector-cylinders, which is provided with the check valve, is directly attached to a body-wall surface of the oxygen tank body. Hence, the structure around the oxygen tank body is simplified and unitized.

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23-01-2014 дата публикации

Method of removing heavy hydrocarbons

Номер: US20140021094A1

Heavy hydrocarbons contained in FT off gas of a GTL process are removed by bringing the FT off gas into contact with absorption oil, by introducing the FT off gas into a distillation tower, by cooling the FT off gas or by driving the FT off gas into an adsorbent. A burner tip for heating a reformer tube, using FT off gas as fuel, is prevented from being plugged by the deposition of heavy hydrocarbons contained in the FT off gas.

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06-02-2014 дата публикации

Methods of Removing Contaminants from Hydrocarbon Stream by Swing Adsorption and Related Apparatus and Systems

Номер: US20140033919A1
Принадлежит: ExxonMobil Upstream Research Co

A pressure swing adsorption process for removal of C02 from natural gas streams through a combination of a selective adsorbent material containing an effective amount of a non-adsorbent filler, adsorbent contactor design, and adsorption cycle design. The removal of contaminants from gas streams, preferably natural gas streams, using rapid-cycle swing adsorption processes, such as rapid-cycle pressure swing adsorption (RC-PSA). Separations at high pressure with high product recovery and/or high product purity are provided through a combination of judicious choices of adsorbent material, gas-solid contactor, system configuration, and cycle designs. For example, cycle designs that include steps of purge and staged blow-down as well as the inclusion of a mesopore filler in the adsorbent material significantly improves product (e.g., methane) recovery. An RC-PSA product with less than 10 ppm H2S can be produced from a natural gas feed stream that contains less than 1 mole percent H2S.

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13-02-2014 дата публикации

Process for the purification of crude gas from solids gasification

Номер: US20140044601A1
Автор: Johannes Kowoll
Принадлежит: UHDE GMBH

A process and device is provided for the generation and purification of a crude gas for synthesis gas generation from a solid carbon-containing fuel by a coal gasification reaction. The fuel is mixed with a quenching medium directly after generation to dissipate the internal energy and is then brought into contact with a compound or a sorbent in the mixing chamber or downstream of the mixing chamber such that the acidic or basic or sulphur-containing or halogen-containing constituents contained in the crude gas and originating from the gasification reaction are absorbed. A solids-separating device removes the solid or solidified constituents from the system. The sorbent can be regenerated and returned to the process such that an energy-intensive cooling of the crude gas is not required for its purification and the synthesis gas thus purified can be used in a subsequent process without any further heating.

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27-02-2014 дата публикации

Removal of nitrogen containing compounds and methane conversion process using a supersonic flow reactor

Номер: US20140058150A1
Принадлежит: UOP LLC

Methods and systems are provided for converting methane in a feed stream to acetylene. The method includes removing at least a portion of nitrogen contaminants from a hydrocarbon stream. The hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. The method according to certain aspects includes controlling the level of amines in the hydrocarbon stream.

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01-01-2015 дата публикации

AIRCRAFT FUEL TANK FLAMMABILITY REDUCTION METHODS AND SYSTEMS

Номер: US20150000523A1
Принадлежит:

An aircraft fuel tank flammability reduction method includes feeding pressurized air into an air separation module containing an oxygen separation membrane. The method includes contacting the separation membrane with the air feed, permeating oxygen from the air feed through the separation membrane, and producing nitrogen-enriched air from the air separation module as a result of removing oxygen from the air feed. The NEA from the air separation module is substantially cooled in a NEA flow heat exchanger and the substantially cooled, nitrogen-enriched air is fed into the fuel tank on board the aircraft. An aircraft fuel tank flammability reduction system includes a NEA flow heat exchanger configured to cool substantially the nitrogen-enriched air from the air separation module and a fuel tank on board the aircraft configured to receive the cooled nitrogen-enriched air. 1. An aircraft fuel tank flammability reduction method comprising:feeding pressurized air into an air separation module containing an oxygen separation membrane;contacting the separation membrane with the air feed, permeating oxygen from the air feed through the separation membrane, and producing nitrogen-enriched air from the air separation module as a result of removing oxygen from the air feed;substantially cooling the nitrogen-enriched air (NEA) from the air separation module in a NEA flow heat exchanger; andfeeding the substantially cooled, nitrogen-enriched air into the fuel tank on board the aircraft.2. The method of wherein the separation membrane comprises a hollow fiber membrane and the air feed exhibits a normal operating temperature of at least about 100° C. (212° F.).3. The method of further comprising a feed flow heat exchanger receiving the pressurized air from a source for the pressurized air and substantially cooling the air feed upstream from the air separation module.4. The method of further comprising directing a same cooling flow to the NEA flow heat exchanger and the feed flow ...

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01-01-2015 дата публикации

Oxygen selective adsorbent for easy desorption and preparation method thereof

Номер: US20150001443A1
Принадлежит: Korea Institute of Energy Research KIER

The present invention provides an oxygen selective adsorbent containing Ba x Sr (1−x) Mg y (CO 3 ) (1+y) or Ba x Sr (1−x) CO 3 particles, increasing transition oxygen partial pressure, and representing high thermal stability and excellent oxygen sorption cavity, by adding another metal such as Sr to Ba which is active element for oxygen adsorption, so as to be capable of desorbing oxygen under lower vacuum even at the same operating temperature as existing oxygen selective adsorbents, and a preparation method thereof.

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04-01-2018 дата публикации

OXYGEN GAS CONCENTRATOR WITH OUTLET ACCUMULATOR

Номер: US20180001048A1
Автор: Allum Todd
Принадлежит:

An oxygen concentrator comprises a product tank that is fluidly coupled to at least one sieve bed, and a product gas accumulator tank that is fluidly coupled to the product tank via a first conduit and to an outlet port via a second conduit, wherein the first conduit and the second conduit are disposed to allow at least a portion of product gas to flow from the product tank to the outlet port. 1. An apparatus , comprising:a product tank that is fluidly coupled to at least one sieve bed; anda product gas accumulator tank that is fluidly coupled to the product tank via a first conduit and to an outlet port via a second conduit,wherein the first conduit and the second conduit are disposed to allow at least a portion of product gas to flow from the product tank to the outlet port.2. The apparatus of claim 1 , wherein the product tank is fluidly coupled to the at least one sieve bed via a check valve that allows flow from the at least one sieve bed to the product tank.3. The apparatus of claim 1 , further comprising a filter that is disposed inline in the first conduit claim 1 , wherein the accumulator tank is disposed between the filter and an outlet of the apparatus.4. The apparatus of claim 1 , further comprising a flow control orifice that is disposed inline in the first conduit claim 1 , wherein the accumulator tank is disposed between the flow control orifice and an outlet of the apparatus.5. The apparatus of claim 1 , further comprising an oxygen sensor that is disposed inline in the first conduit claim 1 , wherein the accumulator tank is disposed between the oxygen sensor and an outlet of the apparatus.6. The apparatus of claim 1 , further comprising a pressure regulator that is disposed inline in the first conduit and regulates a pressure in a first portion of the first conduit down to a target pressure in a second portion of the first conduit.7. The apparatus of claim 6 , wherein the second portion of the first conduit is fluidly coupled to the accumulator tank ...

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04-01-2018 дата публикации

AIR PURIFIER APPARATUS

Номер: US20180001049A1
Автор: Schuller Carmen
Принадлежит:

The invention relates to a modular, portable, air purifier device capable of supplying filtered or otherwise conditioned airflow to an individual. More specifically, the present invention provides an air purification system that allows for the remote detection and analysis of local ambient air quality and transmit that information to wirelessly connected devices. 1. A portable air purification apparatus comprising:a power module;a first air compression module;at least one selectable activation state filtering module, wherein the activation state of the filtering module is in response to a signal received by one or more processors; wherein the modules are configured to connect to with one another so that the power module distributes electrical energy to the air compression module and the air compression module distributes compressed air to the filtering module;a nasal mask configured to connect to the filtering module and direct compressed air into the nasal passages of a user,a plurality of air quality sensors configured to communicate with the one or more processors, the one or more processors configured to execute code residing therein; wherein upon detecting one of a pre-determined plurality of air contaminants, the sensors are configured to send a signal to the processor; wherein upon receipt of a signal by the processor, the processor is configured to change activate the selectable filtering module.2. The portable air purification apparatus of claim 1 , wherein the processor is a remote computing device.3. The portable air purification apparatus of claim 2 , wherein the processor is configured to communicate with the plurality of sensors using RF frequencies.4. The portable air purification apparatus of claim 1 , wherein the processor is further configured to alert the user to the air quality conditions sensed.5. The portable air purification apparatus of claim 4 , further comprising a display device claim 4 , wherein the processor is configured to provide a ...

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07-01-2021 дата публикации

OZONE GENERATING APPARATUS AND OZONE GENERATING METHOD

Номер: US20210001264A1
Принадлежит:

An ozone generating apparatus includes a first flow channel provided with a humidifying section that imparts moisture to oxygen gas and configured to discharge oxygen gas that has passed through the humidifying section, a second flow channel configured to discharge oxygen gas having a moisture content of 10 ppb or less, a confluence channel in which the oxygen gas discharged via the first flow channel and the oxygen gas discharged via the second flow channel join together, an ozone generator configured to generate ozone gas using, as a material, mixed oxygen gas of the oxygen gases that have joined in the confluence channel, and a flow rate ratio adjustment section configured to adjust a ratio between respective flow rates of the oxygen gas discharged from the first flow channel to the confluence channel and the oxygen gas discharged from the second flow channel to the confluence channel. 110-. (canceled)11. An ozone generating apparatus , comprising:a first flow channel provided with a humidifying section that imparts moisture to oxygen gas and configured to discharge oxygen gas that has passed through the humidifying section;a second flow channel configured to discharge oxygen gas having a moisture content of 10 ppb or less;a confluence channel in which the oxygen gas discharged via the first flow channel and the oxygen gas discharged via the second flow channel join together;an ozone generator configured to generate ozone gas using, as a material, mixed oxygen gas of the oxygen gases that have joined together in the confluence channel; anda flow rate ratio adjustment section configured to adjust a ratio between a flow rate of the oxygen gas discharged from the first flow channel to the confluence channel and a flow rate of the oxygen gas discharged from the second flow channel to the confluence channel.12. The ozone generating apparatus of claim 11 , further comprising:a dehumidifying section configured to remove moisture in oxygen gas supplied from an oxygen gas ...

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07-01-2021 дата публикации

OXYGEN SUPPLYING APPARATUS

Номер: US20210001265A1
Принадлежит: OXUS CO., LTD.

An oxygen supplying apparatus includes: an oxygen enriching module including a plurality of oxygen enriching units; a pressure boosting module which receives the oxygen-enriched gas from the oxygen enriching module and boosts pressure of the oxygen-enriched gas; and a controller controlling operations of the oxygen enriching module and the pressure boosting module. The pressure boosting module includes: a low-pressure tank which receives and stores the oxygen-enriched gas from the oxygen enriching module; a pressure booster which boosts pressure of the oxygen-enriched gas discharged from the low-pressure tank; a high-pressure tank stores the oxygen-enriched gas pressure-boosted by the pressure booster; and at least one bypass valve which is provided to a bypass passage for bypassing a portion of the pressure-boosted oxygen-enriched gas stored in the high-pressure tank to the low-pressure tank to regulate bypassing of the oxygen-enriched gas from the high-pressure tank to the low-pressure tank. 1. An oxygen supplying apparatus comprising:an oxygen enriching module including a plurality of oxygen enriching units which respectively generate oxygen-enriched gas and are respectively configured to be selectively operated;a pressure boosting module which receives the oxygen-enriched gas from the oxygen enriching module and boosts pressure of the oxygen-enriched gas; anda controller controlling operations of the oxygen enriching module and the pressure boosting module,wherein the pressure boosting module comprises:a low-pressure tank which receives and stores the oxygen-enriched gas from the oxygen enriching module;a pressure booster which boosts pressure of the oxygen-enriched gas discharged from the low-pressure tank;a high-pressure tank stores the oxygen-enriched gas pressure-boosted by the pressure booster; andat least one bypass valve which is provided to a bypass passage for bypassing a portion of the pressure-boosted oxygen-enriched gas stored in the high-pressure ...

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07-01-2021 дата публикации

Method of preparing co2-selective membranes by controlling calcination process including rapid thermal processing and membranes produced thereby

Номер: US20210001285A1

Disclosed are a method of preparing carbon-dioxide-selective separation membranes by controlling calcination conditions including rapid thermal processing and separation membranes produced thereby. More particularly, disclosed are a method of preparing carbon-dioxide-selective separation membranes that can improve CO2 permselectivity, particularly, exhibit excellent CO2 permselectivity in the presence of water in the feed gas, by controlling the size of defects in the separation membranes using rapid thermal processing, separation membranes produced thereby, and a method of capturing and removing carbon dioxide using the separation membranes.

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07-01-2016 дата публикации

Oxygen separator and method of generating oxygen

Номер: US20160001216A1
Принадлежит: Koninklijke Philips NV

The invention relates to an oxygen separator ( 10 ), comprising at least one oxygen separation device ( 12, 14 ) comprising an oxygen separation sorbent ( 16, 18 ) for separating oxygen from an oxygen comprising gas, wherein the oxygen separation device ( 12, 14 ) comprises a gas inlet ( 24, 28 ) at a primary side being connected to an inlet conduct ( 20 ) for guiding a flow of oxygen comprising gas into the oxygen separation device ( 12, 14 ) and having a gas outlet ( 34, 36 ) at a secondary side being connected to an outlet conduct ( 30, 32 ) for guiding a flow of oxygen enriched gas out of the oxygen separation device ( 12, 14 ), wherein the secondary side of the oxygen separation device ( 12, 14 ) is further connected to a source of purging gas for guiding purging gas through the oxygen separation device ( 12, 14 ) and wherein the primary side of the oxygen separation device ( 12, 14 ) is connected to an exhaust conduct ( 70, 72 ) for guiding exhaust gas out of the oxygen separator ( 10 ), wherein the oxygen separator ( 10 ) further comprises a pressure adjusting device ( 40 ) for creating a pressure difference between the primary side and the secondary side of the oxygen separation device ( 12, 14 ), and wherein a gas sensor ( 82 ) is provided in the exhaust conduct ( 70, 72, 73 ) for determining the concentration of at least one component of the exhaust gas. Such an oxygen separator ( 10 ) provides an improved controlling behavior. The invention further relates to a method of generating oxygen from an oxygen comprising gas.

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07-01-2016 дата публикации

SEPARATION PROCESS OF GASEOUS COMPOUNDS FROM NATURAL GAS WITH LOW EXERGY LOSSES

Номер: US20160001218A1
Автор: Rota Renato
Принадлежит:

The present invention relates to a separation process of natural gas from gaseous compounds present at the wellhead by means of at least two adsorption columns, each containing an adsorbing solid and one operating at a higher pressure than the other, said process being characterized in that: —the compression ratio is within the range of 1.1 to 10; —the ratio between the characteristic convective time through the column and the characteristic diffusive time in the adsorbing solid is higher than 1. 1. A process for separating natural gas from gaseous compounds present at the wellhead , said gaseous compounds being selected from the group consisting of helium , nitrogen , carbon dioxide , hydrogen sulphide and combinations thereof , by means of at least two adsorption columns , each containing an adsorbing solid and one operating at a higher pressure than the other , wherein the column operating at higher pressure has an operating pressure close to that of the wellhead , said process being characterized in that:a. a compression ratio is within the range of 1.3 to 3, the compression ratio being defined as the ratio between the maximum and minimum pressure value at which the process operates;b. the ratio between a characteristic convective time through the column and a characteristic diffusive time in the adsorbing solid is higher than 1, the characteristic convective time through a column being defined as the ratio between the empty volume of the column and the volumetric flow-rate, the characteristic diffusive time in the adsorbing solid being defined as the ratio between the square of the equivalent radius of the particles of the adsorbing solid and the effective diffusivity of the gas.2. (canceled)3. The process according to claim 1 , wherein the ratio between the characteristic convective time through the column and the characteristic diffusive time in the adsorbing solid ranges from 10to 10.4. The process according to claim 1 , wherein the gaseous compounds are ...

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07-01-2016 дата публикации

METHODS AND SYSTEMS OF ENHANCED CARBON DIOXIDE RECOVERY

Номер: US20160001219A1
Принадлежит: APACHE CORPORATION

Methods and systems of enhanced carbon dioxide recovery from an inlet gas stream are provided, by introducing the gas stream to one or more membrane-based separation units to produce a permeate byproduct gas stream having increased concentration of carbon dioxide compared to the inlet gas stream and then introducing the permeate byproduct gas stream to one or more pressure swing adsorption units or trains to enhance recovery of hydrocarbons, such as methane, lost in the byproduct stream and to produce a substantially pure carbon dioxide stream, while minimizing process compression and eliminating process heat for process regeneration. The methods introduced herein are for enhancing product recovery by enhancing carbon dioxide recovery from gas streams with pressures greater than atmospheric conditions. Further refinement to the methods would be the introduction of hydrogen sulfide polishing units within the process to produce product that meets or exceeds sales quality specifications. 1. A method of enhanced carbon dioxide recovery from an inlet gas stream , the method comprising the steps of:introducing an inlet gas stream, having carbon dioxide and hydrogen sulfide, to one or more hydrogen sulfide polishing units;operating the one or more hydrogen sulfide polishing units to produce an outlet gas stream with a reduced concentration of hydrogen sulfide compared to the inlet gas stream;introducing the outlet gas stream to one or more membrane-based separation units;operating the one or more membrane-based separation units to produce a permeate byproduct gas stream having increased concentration of carbon dioxide compared to the carbon dioxide concentration in the outlet gas stream;introducing the permeate byproduct gas stream to one or more pressure swing adsorption units; andoperating the one or more pressure swing adsorption units to produce a substantially pure carbon dioxide stream.2. The method of claim 1 , further comprising the steps of:operating the one or ...

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07-01-2021 дата публикации

Method for Producing Silicoaluminophosphate Sorbent

Номер: US20210001308A1
Принадлежит:

The invention relates to a method for synthesizing silicoaluminophosphate sorbents such as SAPO-56 and SAPO-47 comprising the use of a specific structure directing agent (SDA) comprising a mixture of different types of amines The structure providing agent (SDA) comprises N,N,N′,N′-tetramethyl-1,6-hexanediamine (TMHD) and a co-structure providing agent (co-SDA) selected among primary, secondary and tertiary amines comprising up to 15 carbon atoms and mixtures thereof. A preferred SDA comprises isopropylamine, dibutylamine and tripropylamine The sorbents are particularly suitable for up-grading biogas such as separating carbon dioxide from methane. 1. A method for preparing a silicoaluminophosphate sorbent comprising:providing a reaction mixture, said mixture comprising: a silicon-containing composition, an aluminum-containing composition, a phosphorous-containing composition, and a structure directing agent (SDA);crystallization of the reaction mixture thereby providing crystallized silicoalum inophosphate;recovering crystalline silicoaluminophosphate from the mixture;wherein the structure providing agent (SDA) comprises N,N,N′,N′-tetramethyl-1,6-hexanediamine (TMHD) and a co-structure providing agent (co-SDA) selected among primary, secondary and tertiary amines comprising up to 15 carbon atoms and mixtures thereof.2. The method according to claim 1 , wherein the co-SDA is selected among primary amines comprising a saturated hydrocarbon comprising up to 6 carbon atoms.3. The method according to claim 1 , wherein the silicoaluminophosphate sorbent is selected among SAPO-47 and SAPO-56.4. The method according to claim 1 , wherein the silicoaluminophosphate sorbent is SAPO-56.5. The method according to claim 1 , wherein the SDA comprises up to about 75% wt of the co-SDA.6. The method according to claim 1 , wherein the primary claim 1 , secondary and tertiary amines comprise saturated hydrocarbons.7. The method according to claim 6 , wherein the saturated hydrocarbons ...

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02-01-2020 дата публикации

PROCESS FOR SEPARATION OF PROPYLENE FROM A LIQUEFIED PETROLEUM GAS STREAM

Номер: US20200001198A1
Принадлежит:

Process for separating a highly pure propylene product from a liquefied petroleum gas stream is disclosed, which eliminates a C3 splitter having over 120 trays and the additional equipment that a C3 splitter requires. The process includes passing a feed stream to a dividing wall column to produce an overhead stream, a first side draw stream, a second side draw stream, and a product stream. The first side draw stream is passed to a treatment unit to produce a treated stream. The treated stream is passed to a membrane unit and a permeate stream is passed from the membrane unit to produce a polymer grade propylene stream. 1. A process , comprising:passing a feed stream to a dividing wall column to produce an overhead stream; a first side draw stream; a second side draw stream on the opposite side of the dividing wall from the feed stream; and a product stream;flashing the overhead stream to produce an off gas stream and an overhead liquid stream;passing the overhead liquid stream back to the dividing wall column;passing the first side draw stream to a treatment unit to produce a treated stream;passing a first portion of the second side draw stream back to the dividing wall column and passing a second portion of the second side draw stream as a propane product;passing the treated stream to a membrane unit; andpassing a retentate stream from the membrane unit back to the dividing wall column and passing a permeate stream from the membrane unit to produce a polymer grade propylene stream.2. The process of claim 1 , wherein the feed stream may be is a treated liquid petroleum gas stream from a caustic mercaptan oxidation process.3. The process of claim 1 , wherein the dividing wall column comprises about 40 to about 80 trays.4. The process of claim 1 , wherein the membrane unit comprises a plurality of membranes wherein said membranes are facilitated transport membranes comprising a nanoporous support membrane claim 1 , a hydrophilic polymer inside the nanopores on a skin ...

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04-01-2018 дата публикации

Metallopolyimide precursor fibers for aging-resistant carbon molecular sieve hollow fiber membranes with enhanced selectivity

Номер: US20180001270A1

Metallopolyimide precursor fibers for aging-resistant carbon molecular sieve hollow fiber membranes having enhanced selectivity include transition metal cations complexed with electronegative regions of a polyimide. CMS membranes are made by pyrolyzing the metallopolyimide precursor fibers. The cations are introduced by including, in the bore fluid used to extrude the fibers, either a salt of the transition metal and an inorganic anion or a transition metal/organic ligand complex.

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02-01-2020 дата публикации

Temperature-Vacuum Swing Adsorption Process for Capture of CO2

Номер: US20200001225A1
Принадлежит: UNIVERSITY OF SOUTH CAROLINA

Methods and systems for capture of CO2 from a hydrated gaseous stream are described. Systems can be utilized for direct air capture of CO2 and incorporate a low energy temperature-vacuum swing adsorption (TVSA) process. A TVSA process can include a multi-step CO2 capture bed regeneration process that includes depressurization of the bed, heating of the bed, venting and purging of the bed, and cooling of the bed. Multiple beds can be cycled between CO2 capture and regeneration, during which captured CO2 is recovered. Off-gas from a CO2 capture bed can be used in regenerating a parallel bed for increased efficiency.

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02-01-2020 дата публикации

ELECTROCHEMICAL CELL, METHOD AND APPARATUS FOR CAPTURING CARBON DIOXIDE FROM FLUE GAS AND DECOMPOSING NITROSAMINE COMPOUNDS

Номер: US20200001231A1
Принадлежит:

An apparatus for capturing COfrom flue gas includes (a) an absorber, (b) a stripper, (c) a heat exchanger, (d) an amine absorbent circulating through the absorber, the stripper and the heat exchanger, (e) a water washing unit downstream from the flue gas outlet of the absorber, and (f) an electrochemical cell. The electrochemical cell is connected to the water washing unit and is adapted to adsorb and decompose nitrosamine compounds present in liquid separated by the water washing unit. 1. An electrochemical cell , comprising:an anode including a first carbon xerogel electrode and a first current collector;a cathode including a second carbon xerogel electrode and a second current collector;a separator made from an insulating material; anda current source applying an electrical current to said anode and said cathode.2. The electrochemical cell of claim 1 , including a first endplate including a solution inlet and a second endplate including a solution outlet.3. The electrochemical cell of claim 2 , wherein said first current collector and said second current collector are made of titanium.4. The electrochemical cell of claim 3 , wherein said anode is adjacent said first endplate claim 3 , said cathode is adjacent said second endplate and said separator is porous.5. The electrochemical cell of claim 3 , wherein said cathode is adjacent said first endplate claim 3 , said anode is adjacent said second endplate and said separator is porous.6. The electrochemical cell of claim 1 , including a first endplate having a first solution inlet and a first solution outlet and a second endplate having a second solution inlet and a second solution outlet wherein said first endplate is adjacent said anode claim 1 , said second endplate is adjacent said cathode and said separator is nonporous.7. An apparatus for capturing COfrom flue gas claim 1 , comprising:{'sub': 2', '2, 'an absorber including a flue gas inlet, a flue gas outlet, a CO-lean amine absorbent inlet and a CO-rich amine ...

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04-01-2018 дата публикации

Structured Adsorbent Beds, Methods of Producing the Same and uses Thereof

Номер: US20180001301A1
Принадлежит:

Structured adsorbent beds comprising a high cell density substrate, such as greater than about 1040 cpsi, and a coating comprising adsorbent particles, such as DDR and a binder, such as SiOare provided herein. Methods of preparing the structured adsorbent bed and gas separation processes using the structured adsorbent bed are also provided herein. 1. A structured adsorbent bed for purification of a gas feedstream comprising:a substrate having a cell density greater than 1040 cells per square inch (cpsi); anda coating on the substrate, wherein the coating comprises adsorbent particles and a binder.2. The structured adsorbent bed of claim 1 , wherein the adsorbent particles have an average diameter of about 2 μm to about 40 μm.3. The structured adsorbent bed of claim 1 , wherein the adsorbent particles have an average diameter greater than about 20 μm.4. (canceled)5. The structured adsorbent bed of claim 1 , wherein the adsorbent particles comprise a microporous material.6. The structured adsorbent bed of claim 5 , wherein the microporous material comprises a zeolite.7. The structured adsorbent bed of claim 6 , wherein the zeolite is DDR.8. The structure adsorbent bed of claim 7 , wherein the zeolite is selected from the group consisting of Sigma-1 and ZSM-58.9. The structured adsorbent bed of claim 1 , wherein the binder comprises particles having an average diameter of about 25 nm to about 200 nm.10. The structured adsorbent bed of claim 1 , wherein the binder comprises particles having an average diameter of about 100 nm to about 200 nm.11. The structured adsorbent bed of claim 1 , wherein the binder has a pH greater than 7.12. The structured adsorbent bed of claim 1 , wherein the binder comprises SiO.13. The structured adsorbent bed of claim 1 , wherein the substrate has a cell density of about 1500 cpsi to about 4000 cpsi.14. The structured adsorbent bed of claim 1 , wherein the substrate has a cell density of about 1400 cpsi or greater.15. The structured ...

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03-01-2019 дата публикации

ADSORPTION COLUMN SET FOR SEPARATING TWO OR MORE GASES OF A GAS MIXTURE FROM EACH OTHER USING PRESSURE SWING ADSORPTION

Номер: US20190001254A1
Принадлежит: BioGTS Oy

The invention relates to a set for separating two or more gases from each other, including: 2. An adsorption column set according to claim 1 , wherein the volume of each adsorption column is 0.01-5 m3.3. An adsorption column set according to claim 1 , wherein the volume of each adsorption column is 0.05 and 2 m3.4. An adsorption column set according to claim 1 , said adsorption column set further including a frame for supporting the first adsorption column set in a place of use claim 1 , the frame including connection means connecting the additional adsorption columns to the frame with a dedicated additional frame.5. An adsorption column set according to claim 4 , wherein the frame comprises anchoring members connecting the dedicated additional frame to the frame for increasing capacity.6. An adsorption column set according to claim 1 , wherein the connecting connection is a T-branch.7. An adsorption column set according to claim 1 , wherein said auxiliary equipment is also adapted for operating the additional adsorption columns.8. An adsorption column set according to claim 1 , wherein the dimensions of the auxiliary equipment are such that capacity of the auxiliary equipment corresponds to the aggregated need of the adsorption column and 1-10 additional adsorption columns connected thereto.9. An adsorption column set according to claim 1 , wherein the dimensions of the auxiliary equipment are such that capacity of the auxiliary equipment corresponds to the aggregated need of the adsorption column and 2-4 additional adsorption columns connected thereto.10. An adsorption column set according to claim 1 , wherein the auxiliary equipment includes for each adsorption column of the first adsorption column seta feed line connected to the feed connection feeding a gas mixture to the adsorption columns,a discharge line connected to said discharge connection discharging gases from the adsorption columns.11. An adsorption column set according to claim 10 , wherein the ...

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03-01-2019 дата публикации

SYSTEMS FOR CLOSED LOOP REGENERATION OF GAS DEHYDRATION UNITS USING LIQUID PETROLEUM GAS

Номер: US20190001255A1
Принадлежит:

A system is disclosed in which water-saturated desiccant in a dehydration unit, having previously been used to dehydrate natural gas, is regenerated in a closed loop process using liquid petroleum gas (LPG). LPG is pumped from a storage tank, vaporized and superheated. The superheated LPG gas enters the dehydration unit such that the hot gas passes over the desiccant thereby regenerating the desiccant. An overhead stream from the dehydration unit passes to a condenser where the temperature of the hot gas from the dehydration unit is dropped to form a fluid stream containing LPG, water and non-condensable gases. The fluid stream passes to a three phase separator for separating the fluid stream into a gas stream, a water stream, and a liquid stream containing LPG which is then returned to the storage tank for reuse in the closed loop process. 1. A system for regenerating a gas dehydration unit containing saturated mole sieve used in a process for dehydrating a natural gas feed stream , comprising:a. a storage tank for storing liquid propane and/or butane;b. a pump for pumping the liquid propane and/or butane from the storage tank;c. at least two heat exchangers in series for receiving the liquid propane and/or butane and converting the liquid propane and/or butane to a hot propane gas and/or butane gas;d. a regeneration gas inlet in the gas dehydration unit containing the saturated mole sieve to be regenerated for receiving the hot propane and/or butane gas such that the hot propane gas and/or butane gas passes across the saturated mole sieve thereby regenerating the mole sieve;e. a condenser in communication with a regeneration gas outlet in the gas dehydration unit for receiving an overhead stream containing the hot propane gas and/or butane gas from the gas dehydration unit and dropping the temperature to form a fluid stream containing liquid propane and/or butane, and containing water and non-condensable gas;f. a three phase separator in communication with the ...

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03-01-2019 дата публикации

GAS SEPARATION MEMBRANE USING FURAN-BASED POLYMERS

Номер: US20190001262A1
Принадлежит:

Disclosed herein is a gas separation membrane comprising a furan-based polymer, an apparatus comprising the gas separation membrane, and a process for separating a mixture of gases using said gas separation membrane. The process comprises contacting one side of a gas separation membrane comprising a furan-based polymer with a mixture of gases having different gas permeances, whereby at least one gas from the mixture of gases permeates preferentially across the gas separation membrane, thereby separating the at least one gas from the mixture of gases. 1. A process for separating a mixture of gases comprising:contacting one side of a gas separation membrane comprising a furan-based polymer with a mixture of gases having different gas permeabilities,whereby at least one gas from the mixture of gases permeates preferentially across the gas separation membrane,thereby separating the at least one gas from the mixture of gases.2. The process of claim 1 , further comprising using a pressure differential across the gas separation membrane to separate the at least one gas from the mixture of gases.3. The process of claim 1 , wherein the furan-based polymer is selected from the group consisting of furan-based polyesters and copolyesters claim 1 , furan-based polyamides and copolyamides claim 1 , furan-based polyimides claim 1 , furan-based polycarbonates claim 1 , furan-based polysulfones claim 1 , and furan-based polysiloxanes.4. The process of claim 1 , wherein the furan-based polymer is derived from 2 claim 1 ,5-furan dicarboxylic acid or a derivative thereof and a Cto Caliphatic diol.5. The process of claim 1 , wherein the furan-based polymer is derived from 2 claim 1 ,5-furan dicarboxylic acid or a derivative poly(trimethylene furandicarboxylate) thereof and 1 claim 1 ,3-propanediol.6. The process of claim 1 , wherein the furan-based polymer is a polymer blend comprising 0.1-99.9% by weight of poly(trimethylene furandicarboxylate) and 99.9-0.1% by weight of a poly( ...

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02-01-2020 дата публикации

ADSORPTION PROCESS FOR TREATING NATURAL GAS

Номер: US20200002633A1
Принадлежит:

A process of treating a natural gas stream is provided comprising sending natural gas stream through a first adsorbent bed to remove water and heavy hydrocarbons (C8+) to produce a partially treated gas stream in which the first adsorbent bed is regenerated by a temperature swing adsorption process and then sending the partially treated gas stream through a second adsorption bed to remove carbon dioxide and lighter hydrocarbons (C7−) to produce a purified natural gas stream wherein said second adsorption bed is regenerated by a temperature pressure swing adsorption process. 1. A process of treating a natural gas stream comprisingsending said natural gas stream through a first adsorbent bed to remove water and heavy hydrocarbons (C8+) to produce a partially treated gas stream wherein said first adsorbent bed is regenerated by a temperature swing adsorption process; andsending said partially treated gas stream through a second adsorption bed to remove carbon dioxide and lighter hydrocarbons (C7−) to produce a purified natural gas stream wherein said second adsorption bed is regenerated by a temperature pressure swing adsorption process.2. The process of wherein said natural gas stream comprises less than about 3 vol % carbon dioxide.3. The process of wherein a closed loop or semi-closed loop regeneration gas stream is used to regenerate said second adsorbent bed.4. The process of wherein a semi-closed loop regeneration gas stream is used to regenerate said second adsorbent bed.5. The process of wherein said temperature pressure swing adsorption process comprises a series of steps in order comprising adsorption claim 1 , co-current depressurization claim 1 , closed-loop heating claim 1 , a purge with heating claim 1 , a purge without heating claim 1 , repressurization of the adsorbent bed and cooling with feed and then withdrawal of product.6. The process of wherein said temperature pressure swing adsorption process comprises a series of steps in order comprising ...

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08-01-2015 дата публикации

Nitrogen-enriched gas manufacturing method, gas separation method and nitrogen-enriched gas manufacturing apparatus

Номер: US20150007724A1
Принадлежит: Taiyo Nippon Sanso Corp

A nitrogen-enriched gas manufacturing method and a nitrogen-enriched gas manufacturing apparatus which minimize variations in the compressor load in order to ensure satisfactory utilization of the performance of the compressor. Specifically, a nitrogen-enriched gas manufacturing method for separating a nitrogen-enriched gas from a raw material air containing nitrogen gas using a plurality of adsorption tanks packed with an adsorbent the method including a pressurization and adsorption step, a depressurization and equalization step, a depressurization and regeneration step, and a pressurization and equalization step, wherein in the pressurization or depressurization and equalization step, the raw material air which has been compressed by the compressor is stored in a compressed raw material air tank provided on a branch line between the compressor and the adsorption tanks, and in the pressurization and adsorption step, the raw material air stored in the compressed raw material air tank is introduced into the adsorption tank and used as a portion of the gas that pressurizes the inside of the adsorption tank.

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08-01-2015 дата публикации

CARBON DIOXIDE SEPARATION USING ADSORPTION WITH STEAM REGENERATION

Номер: US20150007727A1
Принадлежит:

A process for separating a carbon dioxide from a gas stream is disclosed. The process can include passing the gas stream over a sorbent that adsorbs the carbon dioxide by concentration swing adsorption and adsorptive displacement. The sorbent can be regenerated and the carbon dioxide recaptured by desorbing the carbon dioxide from the sorbent using concentration swing adsorption and desorptive displacement. A carbon dioxide separation system is also disclosed. Neither the system nor the process rely on temperature swing or pressure swing adsorption. 2. The process of claim 1 , wherein step a) includes adsorption of COby concentration swing adsorption and adsorptive displacement.3. The process of claim 1 , wherein step b) includes desorption of the COfrom the sorbent with by a combination of concentration swing desorption and desorptive displacement.4. The process of claim 1 , wherein step b) comprises treating the sorbent with steam to displace the COfrom the sorbent.5. The process of claim 1 , wherein steps a) and b) are conducted at a constant pressure.6. The process of claim 1 , wherein steps a) and b) are conducted at approximately isothermal conditions.7. The process of claim 1 , wherein the temperature of the sorbent decreases during step a) by no more than about 20° C.8. The process of claim 1 , wherein the temperature of the sorbent increases during step b) by no more than about 20° C.9. The process of claim 1 , wherein the sorbent comprises an alkalized substrate.10. The process of claim 1 , wherein the sorbent comprises an alkalized alumina.11. A sorbent based COadsorption process claim 1 , comprising the steps ofa) preparing a sorbent comprising an alkalized substrate,{'sub': 2', '2, 'b) passing a gas stream containing COacross the sorbent to adsorb the COonto the alkalized substrate.'}{'sub': '2', 'c) recovering the COfrom the sorbent by passing steam across the alkalized substrate to displace the carbon dioxide adsorbed on the alkalized substrate with ...

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08-01-2015 дата публикации

Aqueous solution which efficiently absorbs and recovers carbon dioxide in exhaust gas, and method for recovering carbon dioxide using same

Номер: US20150007728A1

Disclosed is an aqueous solution for absorbing and recovering carbon dioxide from a carbon dioxide-containing gas, the aqueous solution containing an amino alcohol compound represented by Formula I and an amine compound represented by Formula 2, wherein R represents an alkyl group having 1 to 5 carbon atoms; and n represents 1 or 2, wherein X represents —NR1R2; Y represents —NR3R4; R1, R2, R3 and R4 may be the same or different, and each represents an alkyl group having 1 to 3 carbon atoms; and m represents an integer of 3 to 7.

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20-01-2022 дата публикации

SYSTEM AND METHOD FOR CONCENTRATING GAS

Номер: US20220016563A1
Принадлежит:

Gas concentrating systems and methods are provided. In one embodiment, a gas concentrating system and method is provided that includes component heat management. The heat management system can include, for example, one or more air cooling paths. The air cooling paths direct cooling air into and out of component spaces having heat-generating mechanisms. In other embodiments, the heat management system can also include component spaces that are insulated against the heat of heat-generating components. By cooling heat-generating components and insulating other components from heat, reduced wear and extended component life can be achieved. This reduces component failure and costly service to repair or replace failed or worn components. Also, gas concentrating systems and methods are provided for mounting system components with or without the use fasteners and in combination with or without component heat management. 1. A mounting body for a gas concentrating system comprising:a plurality of spaces including a compressor space for housing a compressor and a fan space for housing at least one fan;the compressor comprising a motor portion and a head portion; the first air inlet substantially aligned with the compressor head portion;', 'the second air inlet substantially aligned with the compressor motor portion; and', 'the outlet substantially aligned with the compressor head portion; and, 'the compressor space comprising at least first and second air inlets and an outlet;'}wherein cooling air is drawn through the at least first and second inlets into the compressor space and out the outlet.2. The mounting body of claim 1 , wherein the compressor space includes an air cooling path between the first inlet and the outlet and across the compressor head portion.3. The mounting body of claim 1 , wherein the compressor space includes an air cooling path between the second inlet and the outlet and across the compressor motor portion.4. The mounting body of claim 1 , wherein the ...

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20-01-2022 дата публикации

Systems and Methods for Concentrating Gas

Номер: US20220016566A1
Принадлежит:

Systems and methods are provided that obtain the same or better level of performance by using lower operating flow rates, pressures and/or optimized flow distributions within the system. This extends the life of system components and lower energy consumption. In one embodiment, gas separation (or sieve) beds that are used to separate gaseous components are provided that have lower flow and pressure requirements compared to conventional beds. The sieve beds include, for example, a diffuser having low solid area in cross-section and maximum open area for flow while providing adequate mechanical properties to contain sieve material and support filter media. In another embodiment, systems and methods are provided having an indicator when a component has been serviced or repaired. This provides an indication whether the component has been tampered with in any manner. This allows the manufacturer to determine if the component was serviced, repaired, or tampered with outside the manufacturer's domain. 1. An input interface for a sieve bed comprising: at least one gas feed port;', 'a chamber receiving gas from the port; and', 'at least one flow modifying structure extending from a chamber wall into the chamber, the flow modifying structure positioned appositional to the gas feed port., 'a body having2. The interface of claim 1 , wherein the at least one flow modifying structure comprises a baffle.3. The interface of claim 1 , wherein the at least one flow modifying structure comprises a rib.4. The interface of claim 1 , wherein the at least one flow modifying structure comprises a gap.5. The interface of claim 1 , wherein the at least one flow modifying structure comprises first and second baffles and a gap therebetween.6. The interface of claim 1 , wherein the at least one flow modifying structure comprises first and second rows of baffles.7. The interface of claim 1 , wherein the at least one flow modifying structure comprises first claim 1 , second and third rows of ...

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20-01-2022 дата публикации

GAS RECOVERY METHOD

Номер: US20220016568A1
Автор: Grant Rob
Принадлежит:

The invention provides a process of purifying a fluid useful in a manufacturing process, particularly in the manufacture of silicon wafers, by removing one or more impurities; and apparatus for use in the process. 1. A process for purifying a fluid , the process comprising the steps of:{'b': '1', '1.1 Providing an insulated adsorption vessel () comprising an adsorptive media;'}{'b': '1', '1.2 Providing a first fluid F;'}{'b': 1', '1', '1, '1.3 Cooling the insulated adsorption vessel () and/or cooling the first fluid, F, to an operating temperature T in the range of from −40° C. to −130° C.;'}{'b': 1', '1', '1, '1.4 Contacting the fluid F with the insulated adsorption vessel () to remove one or more impurities G;'}{'b': '2', '1.5 Collecting the resulting purified fluid F; and'}{'b': 1', '1', '1, '1.6 Regenerating the insulated adsorption vessel () by vacuum whilst maintaining the temperature of the vessel at a temperature in the range T to T+50° C. (i.e. in the range +10° C. to −130° C.).'}3. A process for purifying a fluid according to claim 1 , the process comprising the steps of{'b': 0', '0, 'sub': 2', '2, '0.1 Contacting a fluid F with an oxidation reactor to oxidise impurities in F to COand HO;'}{'b': '0', 'sub': 2', '2, '0.2 Contacting the resulting fluid F′ with an adsorption vessel, A, to remove COand with an additional adsorption vessel, B, to remove HO; or'}{'b': '0', 'sub': 2', '2, '0.3 Contacting the resulting fluid F′ with a combined adsorption vessel AB to remove COand HO;'}{'b': '1', '0.4 Collecting the resulting Fluid F;'}{'b': '1', 'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, '1.1 Providing an insulated adsorption vessel () as defined in ;'}{'b': 1', '1', '1, '1.3 Cooling the insulated adsorption vessel () and/or the fluid F to an operating temperature T in the range of from −40° C. to −130° C.;'}{'b': 1', '1, '1.4 Contacting the optionally cooled fluid F with the insulated adsorption vessel to remove one or more impurities G;'}{'b': '2', '1.5 ...

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20-01-2022 дата публикации

System and Method for Concentrating Gas

Номер: US20220016571A1
Автор: Haneen Y. YEHYA
Принадлежит: Invacare Corp

Embodiments of gas concentrating systems and methods are provided. These systems and methods comprise configuration of hardware and software components to monitor various sensors associated the systems and methods of concentrating gas as described herein. These hardware and software components are further configured to utilize information obtained from sensors throughout the system to perform certain data analysis tasks. Through analysis, the system may, for example, calculate a time to failure for one or more system components, generate alarms to warn a user of pending component failure, modify system settings to improve functionality in differing environmental conditions, modify system operation to conserve energy, and/or determine optimal setting configurations based on sensor feedback.

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20-01-2022 дата публикации

METHOD AND SYSTEM FOR TISSUE TREATMENT WITH CRITICAL/SUPERCRITICAL CARBON DIOXIDE

Номер: US20220017868A1
Автор: DeCaro Mark, Wei Guobao
Принадлежит: Warsaw Orthopedic, Inc.

Methods of decontaminating bone tissue and an apparatus or system for the same are provided. The methods can be multi-batch processes and include contacting the bone tissue having contaminants with carbon dioxide to decontaminate the bone tissue and to form carbon dioxide having contaminants. The contaminated carbon dioxide is collected and the contaminants are removed to obtain purified carbon dioxide which can be recycled to treat contaminated bone tissue. The contaminated carbon dioxide can be purified by bubbling it through water and/or an organic solvent followed by acid treatment, filtering and liquefying the carbon dioxide. Contaminants that can be removed from contaminated bone tissue, and in turn, from contaminated carbon dioxide include infectious organisms, bacteria, viruses, protozoa, parasites, fungi and mold or a mixture thereof 118.-. (canceled)19. A system for treating contaminated bone tissue with purified carbon dioxide , the system comprising a bone tissue chamber configured for holding contaminated bone tissue and receiving purified carbon dioxide into the bone tissue chamber and evacuating contaminated carbon dioxide from the bone tissue chamber; a purified carbon dioxide supply configured for supplying purified carbon dioxide to the bone tissue chamber to decontaminate the bone tissue; a collection chamber configured to receive contaminated carbon dioxide from the bone tissue chamber and evacuate contaminated carbon dioxide from the collection chamber; and a purification chamber configured to receive contaminated carbon dioxide from the collection chamber and to remove contaminants from the contaminated carbon dioxide by a purification material to obtain purified carbon dioxide , the purification chamber configured to evacuate the purified carbon dioxide and supply it to the bone tissue chamber.20. A system for treating contaminated bone tissue with purified carbon dioxide of claim 19 , further comprising a controller and a signal transmission ...

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20-01-2022 дата публикации

System and method for managing medical devices

Номер: US20220020480A1
Принадлежит: Invacare Corp

Systems and methods are provided for managing medical devices. In one embodiment, medical device usage data is stored on the medical device to indicate the usage, health, and alarm or error codes. The usage data is electronically read and assessed against one or more thresholds to determine if the medical device is operating properly and, hence, can be inventoried for reuse, or is need of service or repair. Other embodiments are also disclosed wherein the medical device wirelessly scan its environment to ensure, for example, the device is used with approved accessories or components and personnel. In yet other embodiments, medical devices are provided that can configure themselves for operation by scanning any connected components for component-specific operational data. The operational data is then used to configure the medical device to operate with the component.

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14-01-2016 дата публикации

Separation and Storage of Fluids Using ITQ-55

Номер: US20160008753A1

This invention refers to a microporous crystalline material of zeolitic nature that has, in its calcined state and in the absence of defects in its crystalline matrix manifested by the presence of silanols, the empirical formula 2. The method of claim 1 , wherein the zeolite ITQ-55 has claim 1 , in calcined state and in absence of defects in its crystalline matrix manifested by the presence of silanols claim 1 , an empiric formula{'br': None, 'sub': 1/n', '2', '2', '2', '2, 'i': '−g', 'x(MXO):yYO:gGeO:(1)SiO'}in which{'sup': '+', 'M is selected between H, at least one inorganic cation of charge +n, and a mixture of both,'}X is at least one chemical element of oxidation state +3,Y is at least one chemical element with oxidation state +4 different from Si,x takes a value between 0 and 0.2, both included,y takes a value between 0 and 0.1, both included,g takes a value between 0 and 0.5, both included.3. The method of claim 2 , wherein x takes a value of essentially zero claim 2 , y takes a value of essentially zero claim 2 , and g takes a value of essentially zero.4. The method of claim 2 , wherein a) x takes a value of greater than zero claim 2 , b) y takes a value of greater than zero claim 2 , c) g takes a value of greater than zero claim 2 , or d) a combination thereof.5. The method of claim 1 , wherein forming an adsorbed product fluid stream comprises modifying at least one of a temperature or a pressure of the adsorbent.6. The method of claim 1 , wherein forming an adsorbed product fluid stream comprises exposing a fluid stream comprising a third component to the adsorbent comprising zeolite ITQ-55 claim 1 , at least a portion of the third component being adsorbed by the adsorbent comprising zeolite ITQ-55.7. The method of claim 1 , wherein exposing the input fluid stream to an adsorbent comprises exposing the input fluid stream to an adsorbent in a swing adsorption vessel.8. The method of claim 7 , wherein exposing the input fluid stream to an adsorbent ...

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14-01-2016 дата публикации

Separation and Storage of Fluids Using ITQ-55

Номер: US20160008754A1

This invention refers to a microporous crystalline material of zeolitic nature that has, in its calcined state and in the absence of defects in its crystalline matrix manifested by the presence of silanols, the empirical formula 2. The method of claim 1 , wherein the zeolite ITQ-55 has claim 1 , in calcined state and in absence of defects in its crystalline matrix manifested by the presence of silanols claim 1 , an empiric formula{'br': None, 'i': x', 'y', ':g', '−g, 'sub': 1/n', '2', '2', '2', '2, '(MXO):YOGeO:(1)SiO'}in which{'sup': '+', 'M is selected between H, at least one inorganic cation of charge +n, and a mixture of both,'}X is at least one chemical element of oxidation state +3,Y is at least one chemical element with oxidation state +4 different from Si,x takes a value between 0 and 0.2, both included,y takes a value between 0 and 0.1, both included,g takes a value between 0 and 0.5, both included.3. The method of claim 2 , wherein x takes a value of essentially zero claim 2 , y takes a value of essentially zero claim 2 , and g takes a value of essentially zero.4. The method of claim 2 , wherein a) x takes a value of greater than zero claim 2 , b) y takes a value of essentially zero claim 2 , c) g takes a value of essentially zero claim 2 , or d) a combination thereof.5. The method of claim 1 , wherein exposing the input fluid stream to an adsorbent comprises exposing the input fluid stream to an adsorbent in a swing adsorption vessel.6. The method of claim 1 , wherein the first temperature and the second temperature are the same claim 1 , wherein the first pressure and the second pressure are the same claim 1 , or a combination thereof.7. The method of claim 1 , wherein forming an adsorbed product fluid stream comprises modifying the second temperature of the adsorbent.8. The method of claim 1 , wherein forming an adsorbed product fluid stream comprises exposing a fluid stream comprising a third component to the adsorbent comprising zeolite ITQ-55 claim 1 ...

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14-01-2016 дата публикации

Separation and Storage of Fluids Using ITQ-55

Номер: US20160008756A1

This invention refers to a microporous crystalline material of zeolitic nature that has, in its calcined state and in the absence of defects in its crystalline matrix manifested by the presence of silanols, the empirical formula 2. The method of claim 1 , wherein the zeolite ITQ-55 has claim 1 , in calcined state and in absence of defects in its crystalline matrix manifested by the presence of silanols claim 1 , an empiric formula{'br': None, 'i': x', 'y', ':g', 'g, 'sub': 1/n', '2', '2', '2', '2, '(MXO):YOGeO:(1−)SiO'}in which{'sup': '+', 'M is selected between H, at least one inorganic cation of charge +n, and a mixture of both,'}X is at least one chemical element of oxidation state +3,Y is at least one chemical element with oxidation state +4 different from Si,x takes a value between 0 and 0.2, both included,y takes a value between 0 and 0.1, both included,g takes a value between 0 and 0.5, both included.3. The method of claim 2 , wherein x takes a value of essentially zero claim 2 , y takes a value of essentially zero claim 2 , and g takes a value of essentially zero.4. The method of claim 2 , wherein a) x takes a value of greater than zero claim 2 , b) y takes a value of essentially zero claim 2 , c) g takes a value of essentially zero claim 2 , or d) a combination thereof.5. The method of claim 1 , wherein the membrane comprises particles of crystalline zeolite ITQ-55 having a mean particle size of about 20 nm to about 1 micron.6. The method of claim 1 , wherein the particles of crystalline molecular sieve zeolite ITQ-55 comprise a contiguous layer of particles.7. The method of claim 1 , wherein the particles of crystalline zeolite ITQ-55 comprise a layer of particles of crystalline zeolite ITQ-55 on a support.8. The method of claim 7 , wherein the support comprises glass claim 7 , fused quartz claim 7 , silica claim 7 , silicon claim 7 , clay claim 7 , metal claim 7 , porous glass claim 7 , sintered porous metal claim 7 , titania claim 7 , cordierite claim 7 ...

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14-01-2016 дата публикации

METHOD FOR PRODUCING ACID GAS SEPARATION COMPOSITE MEMBRANE, AND ACID GAS SEPARATION MEMBRANE MODULE

Номер: US20160008766A1
Принадлежит: FUJIFILM Corporation

A solution is to produce an acid gas separation composite membrane provided with an acid gas separation facilitated membrane on a porous support, including; arranging of a coating liquid for acid gas separation formed through dispersing or dissolving into water a polyvinyl acetal compound formed through crosslinking, by an acetal bond, block copolymers formed through bonding of a polymer block formed of polyvinyl alcohol and a polymer block formed of polyacrylate through a linking group, an acid gas carrier and at least one kind of anion other than hydroxide ion, carboxyl ion, carbonate ion and bicarbonate ion, and coating of the coating liquid for acid gas separation onto a hydrophobic surface of the porous support having hydrophobicity at least on one surface to form the acid gas separation facilitated transport membrane thereon. 1. A method for producing an acid gas separation composite membrane provided with an acid gas separation facilitated transport membrane on a porous support , comprising;arranging of a coating liquid for acid gas separation formed through dispersing or dissolving into water a polyvinyl acetal compound formed through crosslinking, by an acetal bond, block copolymers formed through bonding of a polymer block formed of polyvinyl alcohol and a polymer block formed of polyacrylate through a linking group,an acid gas carrier, andat least one kind of anion other than hydroxide ion, carboxyl ion, carbonate ion and bicarbonate ion, andcoating of the coating liquid for acid gas separation onto the surface of the porous support having hydrophobicity at least on one surface to form the acid gas separation facilitated transport membrane thereon.2. The method for producing the acid gas separation composite membrane according to claim 1 , wherein the linking group is a sulfide group.3. The method for producing the acid gas separation composite membrane according to claim 1 , wherein viscosity of the coating liquid for acid gas separation is 0.4 Pa·s or ...

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14-01-2016 дата публикации

METHOD OF PRODUCING COMPOSITE FOR ACID GAS SEPARATION

Номер: US20160008767A1
Автор: YONEYAMA Satoshi
Принадлежит: FUJIFILM Corporation

An art is provided for preparing a coating liquid for formation of an acid gas separation facilitated transport membrane, the coating liquid containing a hydrophilic compound, an acid gas carrier and water, using as a porous support a laminated membrane between a hydrophobic porous membrane and an auxiliary support membrane, coating onto a surface of the hydrophobic porous membrane of the laminated membrane the coating liquid for formation at a liquid membrane thickness of 0.3 mm or more and 1.0 mm or less, and drying the coated liquid membrane to form a first acid gas separation facilitated transport membrane, and further coating the coating liquid for formation of the acid gas separation facilitated transport membrane onto the previously formed acid gas separation facilitated transport membrane, and drying the coated liquid membrane to form a next acid gas separation facilitated transport membrane. 1. A method of producing a composite for acid gas separation , the composite provided with an acid gas separation facilitated transport membrane having a function of separating an acid gas in a raw material gas on a porous support , comprising:a coating liquid preparation step for preparing a coating liquid for formation of the acid gas facilitated transport membrane, the coating liquid containing a hydrophilic compound, an acid gas carrier and water;an initial layer formation step for forming a first acid gas separation facilitated transport membrane by using as the porous support a laminated membrane between a hydrophobic porous membrane and an auxiliary support membrane, coating on a surface of the hydrophobic porous membrane of the laminated membrane the coating liquid for formation at a liquid membrane thickness of 0.3 mm or more and 1.0 mm or less, and drying the coated liquid membrane; anda next layer formation step one or more times for forming a next acid gas separation facilitated transport membrane by further coating on the previously formed acid gas ...

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14-01-2016 дата публикации

METHOD OF PRODUCING COMPOSITE FOR ACID GAS SEPARATION

Номер: US20160008768A1
Принадлежит: FUJIFILM Corporation

Preparing forming coating liquid for an acid gas separation facilitated transport membrane which includes a hydrophilic compound, an acid gas carrier, and water, coating the forming coating liquid, using a layered film layered in the order of a hydrophilic porous film, a hydrophobic porous film, and an auxiliary support film as a porous support, on a surface of the hydrophilic porous film of the layered film with a liquid film thickness of 0.3 mm to 1.0 mm and drying the coated liquid to form a first acid gas separation facilitated transport membrane, and further coating the forming coating liquid for the acid gas separation facilitated transport membrane on the surface of the hydrophilic porous film with the previously formed acid gas separation facilitated transport membrane and drying the coated liquid to form a next acid gas separation facilitated transport membrane. 1. A method of producing a composite for acid gas separation with an acid gas separation facilitated transport membraned having a function of separating an acid gas in a raw gas on a porous support , the method comprising:a coating liquid preparation step in which a forming coating liquid for the acid gas separation facilitated transport membrane is prepared, the forming coating liquid including a hydrophilic compound, an acid gas carrier, and water;an initial layer forming step in which a first acid gas separation facilitated transport membrane is formed by coating the forming coating liquid, using a layered film layered in the order of a hydrophilic porous film, a hydrophobic porous film, and an auxiliary support film as the porous support, on a surface of the hydrophilic porous film of the layered film with a liquid film thickness of 0.3 mm to 1.0 mm and drying the coated coating liquid; anda next layer forming step in which a next acid gas separation facilitated transport membrane is formed by further coating the forming coating liquid for the acid gas separation facilitated transport membrane ...

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12-01-2017 дата публикации

APPARATUS FOR PRECOOLING AND PURIFYING HYDROGEN

Номер: US20170008763A1
Принадлежит:

Disclosed herein is an apparatus for precooling and purifying hydrogen including a body which includes a first chamber and a second chamber disposed in the first chamber with the second chamber being filled with a liquid cooling medium, a first cyclone chamber disposed in the second chamber and connected to a hydrogen supply pipe on an upper of one side thereof to allow the hydrogen which flows therein to move downward rotating to perform thermal exchange with the cooling medium and separation of impurities therefrom, a first hydrogen discharge pipe to allow hydrogen to flow from the first cyclone chamber to the outside, and an ortho-para hydrogen converting catalyst disposed on a path through which hydrogen which flows in the first hydrogen discharge pipe moves to allow ortho-para hydrogen conversion to be performed. 1. An apparatus for precooling and purifying hydrogen comprising:a body which comprises a first chamber and a second chamber installed in the first chamber with an insulating layer between an outer circumferential surface of the second chamber and an inner circumferential surface of the first chamber, wherein the second chamber is filled with a liquid cooling medium;a first cyclone chamber installed in the second chamber and connected to a hydrogen supply pipe through which hydrogen is supplied from the outside on an upper portion of one side of the first cyclone chamber, wherein the hydrogen introduced on the inside moves downward rotating to perform thermal exchange with the cooling medium and separation of impurities therefrom;a first hydrogen discharge pipe disposed in a central portion of the first cyclone chamber, wherein the hydrogen which has moved downward in the first cyclone chamber flows through a lower end of the first hydrogen discharge pipe;an ortho-para hydrogen converting catalyst disposed in a path in the second chamber, wherein the hydrogen which flows in the first hydrogen discharge pipe moves through the path to allow ortho-para ...

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