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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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Форма поиска

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 15092. Отображено 100.
01-08-2019 дата публикации

Адсорбционная ловушка

Номер: RU0000191341U1

Полезная модель относится к устройствам для адсорбционного удаления примесей влаги и специфических химических соединений из газового потока и может быть использована в системах адсорбционной очистки газов, анализаторах хемосорбции и т.п. Адсорбционная ловушка включает корпус, в котором выполнены входной и выходной каналы для газового потока, и расположенную в корпусе трубку с сорбентом, имеющую входной и выходной концы, при этом трубка снабжена держателем с обеспечением его разъемного герметичного соединения с корпусом, где держатель выполнен в виде изолирующего цилиндра с полостью для размещения трубки, заглушенного на одном конце, на котором размещен шестигранник, другой конец изолирующего цилиндра снабжен внешней резьбой для фиксации держателя в корпусе ловушки, при этом ответная часть внутренней поверхности корпуса снабжена внутренней резьбой, корпус выполнен с ложементом для герметичного размещения ответной части трубки, входной конец которой размещен со стороны заглушенного конца цилиндра, а трубка в держателе размещена с обеспечением зазора между внешней поверхностью трубки и внутренней поверхностью изолирующего цилиндра для прохода газа из входного канала корпуса к входному концу трубки с сорбентом и из выходного конца трубки в выходной канал. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 191 341 U1 (51) МПК B01D 53/02 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК B01D 53/02 (2019.02) (21)(22) Заявка: 2018143685, 10.12.2018 (24) Дата начала отсчета срока действия патента: Дата регистрации: 01.08.2019 (45) Опубликовано: 01.08.2019 Бюл. № 22 1 9 1 3 4 1 R U (54) АДСОРБЦИОННАЯ ЛОВУШКА (57) Реферат: Полезная модель относится к устройствам для адсорбционного удаления примесей влаги и специфических химических соединений из газового потока и может быть использована в системах адсорбционной очистки газов, анализаторах хемосорбции и т.п. Адсорбционная ловушка включает корпус, в котором выполнены входной и ...

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02-02-2012 дата публикации

Environmentally-friendly animal litter

Номер: US20120024235A1
Принадлежит: Ceramatec Inc

An animal litter composition that includes geopolymerized ash particulates having a network of repeating aluminum-silicon units is described herein. Generally, the animal litter is made from a quantity of a pozzolanic ash mixed with an alkaline activator to initiate a geopolymerization reaction that forms geopolymerized ash. This geopolymerization reaction may occur within a pelletizer. After the geopolymerized ash is formed, it may be dried and sieved to a desired size. These geopolymerized ash particulates may be used to make a non-clumping or clumping animal litter or other absorbing material. Aluminum sulfate, clinoptilolite, silica gel, sodium alginate and mineral oil may be added as additional ingredients.

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17-05-2012 дата публикации

Attrition resistant hardened zeolite materials for air filtration media

Номер: US20120118160A1
Принадлежит: JM Huber Corp

Environmental control in air handling systems that are required to provide highly effective filtration of noxious gases particularly within filter canisters that are ultrasonically welded enclosures is provided. In one embodiment, a filtration system utilizes a novel zeolite material that has been hardened to withstand ultrasonic welding conditions in order to reduce the propensity of such a material to destabilize and/or dust. Such a hardened zeolite thus enables for trapping and removal of certain undesirable gases (such as ammonia, ethylene oxide, formaldehyde, and nitrous oxide, as examples) from an enclosed environment, particularly in combination with metal-doped silica gel materials. Such a hardened zeolite is acidic in nature and not reacted with any salts or like substances and, as it remains in a hardened state upon inclusion within a welded filter device, the filter medium itself permits proper throughput with little to no dusting, thereby providing proper utilization and reliability for such a gas removal purpose. Methods of using and the application within specific filter apparatuses are also encompassed within this invention.

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12-07-2012 дата публикации

Adsorbent Filter Media For Removal Of Biological Contaminants In Process Liquids

Номер: US20120175805A1
Автор: David P. Yavorsky
Принадлежит: EMD Millipore Corp

Adsorbent filter media particularly suited for removal of biological contaminants in process liquids. A porous fixed bed of adsorbent material is formed, using only a granular adsorbent and a water-insoluble thermoplastic binder. The resulting composite filter allows for a higher amount of adsorbent with smaller adsorbent particles than conventional depth filters. Elimination of cellulose fiber, as well as the elimination of the thermoset binder, results in reduced contamination of the process liquid.

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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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01-11-2012 дата публикации

Process of precious metal recovery and color removal from an organosilicon product-containing liquid reaction medium

Номер: US20120272791A1
Автор: He Bai, Scott FRUM
Принадлежит: Momentive Performance Materials Inc

The present invention relates to a process for recovery of a precious metal catalyst from an organosilicon product-containing liquid reaction medium containing precious metal catalyst.

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06-12-2012 дата публикации

Process for Recovering Molybdate or Tungstate from Aqueous Solutions

Номер: US20120305208A1
Принадлежит: EVONIK DEGUSSA GmbH

Process for recovering molybdate or tungstate from an aqueous solution, in which molybdate or tungstate is bound to a water-insoluble, cationized inorganic carrier material from the aqueous solution at a pH in the range from 2 to 6, the laden carrier material is separated off and the bound molybdate or tungstate is liberated once again into aqueous solution at a pH in the range from 6 to 14. The process is suitable for recovering molybdate or tungstate in the delignification of pulp with hydrogen peroxide in the presence of molybdate or tungstate as catalyst. The recovered molybdate or tungstate can be recycled to the delignification.

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24-01-2013 дата публикации

Compressed Growing Medium

Номер: US20130020738A1
Автор: Patti D. Rubin
Принадлежит: Individual

A growing medium includes a bulking agent and a water-retentive polymer blended together and compressed at a volume-to-volume ratio ranging from about 2:1 to about 10:1, being substantially free of a water-soluble binder material.

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31-01-2013 дата публикации

Fluid Filtration Medium

Номер: US20130026103A1
Принадлежит: Zeotech Corp

The present application relates to improved filtration of fluids. Particularly, a surfactant-treated zeolite material may be utilized for removing turbid particles from a volume of fluid, such as water.

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14-02-2013 дата публикации

Process for separating gases and adsorbent compositions used therein

Номер: US20130036904A1
Принадлежит: Praxair Technology Inc

The present invention relates generally to a composite adsorbent comprising at least a zeolite-containing CO 2 removal adsorbent and 10% or more of a metal oxide having a heat capacity of at least 20 cal/mol-° K (83.7 J/(mol·K). The composite is preferably used in a multi-layered adsorption system in a cyclic adsorption process. The adsorption system comprises two or more layers wherein the first layer is at least a water vapor removal adsorbent, such as activated alumina, and the second layer is the novel composite adsorbent. The adsorption system is preferably used in a PSA prepurification process prior to cryogenic air separation.

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14-02-2013 дата публикации

Composition comprising an activated carbon, a zeolite, and fe ions for a vehicle passenger compartment air filter

Номер: US20130040804A1
Принадлежит: Valeo Systemes Thermiques SAS

The invention relates to a composition ( 1 ) comprising an activated carbon ( 4 ) and a zeolite ( 2 ), the zeolite ( 2 ) comprising Fe ions. The invention also relates to an air filter ( 12 ) for a ventilation, heating, and/or air conditioning system comprising this composition ( 1 ).

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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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21-03-2013 дата публикации

METHOD AND INSTRUMENTATION FOR COMPREHENSIVE MULTIDIMENSIONAL CHROMATOGRAPHY SEPARATIONS USING A MICRO FLOW MODULATOR

Номер: US20130068100A1
Автор: MONDELLO Luigi
Принадлежит:

The present invention refers to a modulator, to be used for comprehensive multidimensional chromatography separations to entrap and release sample solute fractions (entrapped in a capillary loop of fixed or variable volume), deriving from a capillary column with an internal diameter ranging from 0.01 mm to 0.53 mm, onto another capillary column with an internal diameter ranging from 0.01 mm to 0.53 mm. The micro-device has been integrated in a gas chromatographic system, composed of two ovens for the independent temperature control of the two columns; the micro-device is characterized, internally, by a system of channels that enable the controlled splitting of gas flow, entering the second capillary, to generate an optimum gas linear velocity and to release the pressure in excess, with the objective of attaining the maximum separation efficiency in the second column. Furthermore, the system is equipped with a second device, to divide the flow exiting the second column in two different detectors that operate at the same or at different pressures. 1. A device that functions as a modulator for chromatography comprising:a port that receives effluent from a first chromatographic column;either one or two capillary sample loops located externally with respect to said modulator, or either one or two capillary sample loops integrated in said modulator;two independent ports that receive a flow from one or more electronic pressure and/or flow control devices located externally with respect to said modulator;three channels, either integrated or located externally with respect to said modulator, connected to said one or two capillary sample loops and a second column, to split with a needle valve the flow exiting an accumulation capillary loop and to release the pressure in excess within the channels connected to said accumulation capillary loop and in the second column, when emptying said accumulation capillary loop;a needle valve, either integrated or external to the modulator, ...

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02-05-2013 дата публикации

Radioactive-substance-absorbent, radioactive-substance-absorbent production device, decontaminating method, and bag unit

Номер: US20130109902A1
Автор: Masao Yamada
Принадлежит: Seibu Newsaper Co

By fibrillated cellulose fibrillated in fiber form and humidified as a water permeable polymeric substance of botanical origin and a radioactive-substance-absorbent obtained by mixing with zeolite as a granulated inorganic porous crystal, radioactive substances released and spilled in a accident etc. in a nuclear facility etc. may be efficiently and easily collected and removed at a low cost.

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30-05-2013 дата публикации

Combustible Gas Enrichment Apparatus

Номер: US20130136660A1
Принадлежит: OSAKA GAS CO., LTD.

In order to provide a technique for enriching a combustible gas that allows enrichment of the combustible gas to a higher concentration in an efficient manner with minimization of loss of a source material, there are provided an adsorption tower charged with an adsorbent, a feeding/discharging means for feeding a source gas containing a combustible gas and air, a collecting means for desorbing the combustible gas adsorbed to the adsorbent and collecting the desorbed gas, a controlling means for sequentially effecting a combustible gas adsorption process and a combustible gas desorption process, a detecting means for detecting the concentration of the combustible gas in the source gas, and an operation condition setting section for varying an adsorption completion timing for the controlling means to complete the adsorption process, based on the combustible gas concentration detected by the detecting means. 1. A combustible gas enrichment apparatus comprising:an adsorption tower charged with an adsorbent for adsorbing a combustible gas;a feeding/discharging means for feeding a source gas containing the combustible gas and air to the adsorption tower via a feeding passage and discharging an offgas which is the portion of the source gas not adsorbed to the adsorbent to the outside of the adsorption tower via a discharging passage;a collecting means for desorbing the combustible gas adsorbed to the adsorbent by depressurizing the inside of the adsorption tower to a subatmospheric pressure and collecting the desorbed combustible gas through a collecting passage; anda controlling means for sequentially effecting a combustible gas adsorption process for causing the feeding/discharging means to feed the source gas to the adsorption tower and to discharge the offgas from the adsorption tower and a combustible gas desorption process for causing the collecting means to desorb and collect the combustible gas by the collecting means;wherein the enrichment apparatus further ...

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13-06-2013 дата публикации

METHOD FOR PRODUCING REGENERATED CLAY, REGENERATED CLAY, AND METHOD FOR PRODUCING PURIFIED FATS AND OILS

Номер: US20130150603A1
Принадлежит: THE NISSHIN OILLIO GROUP, LTD.

The present invention provides a method for performing regeneration of a decolorization capacity of waste clay that has been used for purification of fats and oils, and production of a thermally recyclable compound as a biofuel from oily ingredients in the waste clay at the same time in a convenient manner. That is, a method for producing purified fats and oils of the invention includes: a method for producing regenerated clay including the steps of mixing waste clay that has been used for purification of fats and oils, lower alcohol, and an acidic catalyst; and performing extraction of oily ingredients from the waste clay, and an esterification reaction between the fats and oils and/or a free fatty acid in the oily ingredients and the lower alcohol at the same time so as to regenerate a decolorization capacity of the waste clay; regenerated clay that is produced by the method for producing the regenerated clay; and a process of decolorizing the fats and oils using the regenerated clay. 1. A method for producing regenerated clay , the method comprising the steps of:mixing waste clay that has been used for purification of fats and oils, lower alcohol, and an acidic catalyst; andperforming extraction of oily ingredients from the waste clay, and an esterification reaction between the fats and oils and/or a free fatty acid in the oily ingredients and the lower alcohol at the same time so as to regenerate a decolorization capacity of the waste clay.2. The method for producing regenerated clay according to claim 1 ,wherein 50 to 900 parts by mass of the lower alcohol is mixed with respect to 100 parts by mass of the waste clay.3. The method for producing regenerated clay according to claim 1 ,wherein the extraction of the oily ingredients, and the esterification reaction between the fats and oils and/or the free fatty acid in the oily ingredients and the lower alcohol are performed at a temperature of 60 to 200° C.4. The method for producing regenerated clay according to ...

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04-07-2013 дата публикации

MOLDABLE DESICCANT AND HYDROGEN GETTERING SYSTEM

Номер: US20130168603A1

A composite useful for both gas gettering and moisture adsorption comprising an organic getter component and a desiccant component homogeneously dispersed in an elastomeric matrix. The getter component comprises an organic material capable of reacting with hydrogen and a hydrogenation catalyst. The desiccant component is a molecular sieve. The composite is a resilient, self-sustaining body that can also function as a shock absorber. A method of forming composites useful for both gas gettering and moisture adsorption is also disclosed, along with a kit to facilitate the same. 1. A composite useful for both gas gettering and moisture adsorption comprising an organic getter component and a desiccant component homogeneously dispersed in an elastomeric matrix.2. The composite of claim 1 , wherein said getter component comprises an organic material capable of reacting with hydrogen and a hydrogenation catalyst.3. The composite of claim 2 , wherein said organic material is 1 claim 2 ,4-bis(phenylethynyl)benzene.4. The composite of claim 2 , wherein said hydrogenation catalyst comprises a metal selected from the group consisting of palladium claim 2 , platinum claim 2 , rhodium claim 2 , ruthenium claim 2 , iridium claim 2 , osmium claim 2 , and combinations thereof.5. The composite of claim 4 , wherein said metal is supported on an inert substrate.6. The composite of claim 5 , wherein said hydrogenation catalyst comprises from about 3 wt % to about 20 wt % palladium supported on activated carbon.7. The composite of claim 2 , wherein the weight ratio of organic material to catalyst in the getter component is from about 50:50 to about 90:10.8. The composite of claim 1 , wherein said desiccant component comprises a molecular sieve having an average pore opening of from about 3 Å to about 10 Å.9. The composite of claim 8 , wherein said molecular sieve is zeolite.10. The composite of claim 1 , wherein said elastomeric matrix is selected from the group consisting of silicone ...

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11-07-2013 дата публикации

METHOD FOR PURIFYING ALKALINE TREATMENT FLUID FOR SEMICONDUCTOR SUBSTRATE AND A PURIFICATION APPARATUS

Номер: US20130174868A1
Принадлежит:

Provided are a purification method and purification apparatus for an alkaline treatment liquid for a semiconductor substrate, which use adsorption purification means that can purify various alkaline treatment liquids to be used for treating semiconductor substrates for various purposes so as to have an ultrahigh purity, in particular, an Fe concentration in a ppq region, and that is excellent in chemical resistance and mechanical strength. The adsorption purification means is purification means for an alkaline treatment liquid for treating a semiconductor substrate for various purposes at the time of producing, for example, a semiconductor substrate or a semiconductor device. In the purification method and purification apparatus for an alkaline treatment liquid for a semiconductor substrate, an alkaline treatment liquid is brought into contact with silicon carbide crystal surfaces in the absorption purification means, for example, an alkaline treatment liquid is allowed to flow through a gap between adsorbing plate laminates () whose both surfaces are CVD silicon carbide surfaces, thereby removing metal impurities contained in the alkaline treatment liquid through adsorption of the metal impurities to the silicon carbide crystal surfaces. 118.-. (canceled)19. A method for purifying an alkaline treatment liquid for a semiconductor substrate , comprising:bringing an alkaline treatment liquid free of alkali metals to be used for treating a semiconductor substrate, into contact with silicon carbide crystal faces in adsorption purification means; andremoving metal impurities contained in the alkaline treatment liquid through adsorption of the metal impurities to the silicon carbide crystal faces,wherein each of the silicon carbide crystal faces is a (0001) crystal face of a silicon carbide single crystal, a (111) crystal face oriented on each crystal of a silicon carbide grain group formed by a chemical vapor deposition (CVD) method, or a crystal face of a silicon ...

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11-07-2013 дата публикации

Non-visible activated carbon in absorbent materials

Номер: US20130177620A1
Принадлежит: Clorox Co

The present invention teaches an absorbent material with powdered activated carbon which is substantially light-colored without using color masking agents or hiding. This invention addresses the need in the field for an absorbent material with improved odor-controlling properties, that maintains such properties for longer periods of time and where the absorbent material maintains a light-colored appearance without the addition of color-masking agents. Suitable methods for creating the absorbent materials include a pan agglomeration process, a high shear agglomeration process, a low shear agglomeration process, a high pressure agglomeration process, a low pressure agglomeration process, a rotary drum agglomeration process, a pan agglomeration process, a roll press compaction process, a pin mixer process, a dry blending process, a spray coating process, an extrusion process, a pelletizing process and a fluid bed process.

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18-07-2013 дата публикации

Treatment Apparatus for Evaporated Fuel

Номер: US20130183207A1
Принадлежит: AISAN KOGYO KABUSHIKI KAISHA

A treatment apparatus for evaporated fuel including tank port, a purge port, an atmosphere port, a channel communicating the tank port or the purge port and the atmosphere port, and plural adsorption chambers having adsorbent therein, which adsorbing and desorbing a fuel component of evaporated fuel, wherein the adsorption chamber closest to the atmosphere port has a major diameter portion filled with the adsorbent over all a cross section of the charmed a projecting portion projecting from the major diameter portion toward the atmosphere port and filled with the adsorbent, and a space portion between the projecting portion and an inner wall of the channel and not filled with the adsorbent, and end surfaces of the major diameter portion and the projecting portion on the atmosphere port side are breathable so as to control temperature drop in activated carbon and to thereby enhance bleed emission performance. 1. A treatment apparatus for evaporated fuel comprising: a tank port; a purge port; an atmosphere port; a channel that communicates the tank port or the purge port and the atmosphere port; and , a plurality of adsorption chambers having adsorbent placed therein , the adsorbent adsorbing and desorbing a fuel component of evaporated fuel ,wherein said adsorption chamber positioned closest to said atmosphere port has: a major diameter portion filled with said adsorbent over all a cross section of said channel; a projecting portion that projects from said major diameter portion toward said atmosphere port and is filled with said adsorbent; and, a space portion that is formed between said projecting portion and an inner wall of said channel and is not filled with said adsorbent, andend surfaces of said major diameter portion and said projecting portion on the atmosphere port side are breathable.2. The treatment apparatus for evaporated fuel according to claim 1 , wherein a partition wall is provided between said projecting portion and said space portion so as to ...

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18-07-2013 дата публикации

INTRODUCTION OF MESOPOROSITY INTO INORGANIC MATERIALS IN THE PRESENCE OF A NON-IONIC SURFACTANT

Номер: US20130183229A1
Принадлежит: Rive Technology, Inc.

Compositions and methods for introducing mesoporosity into inorganic materials in the presence of a non-ionic surfactant are disclosed herein. Mesopores can be introduced into inorganic materials, such as zeolites, by treating the inorganic materials with a non-ionic surfactant. The resulting mesoporous inorganic materials can have a total 20 to 135 Å diameter mesopore volume of at least 0.05 cc/g and a crystalline content of at least 20 weight percent as measured by X-ray diffraction. 1. A method of forming a material comprising a mesoporous inorganic material having long-range crystallinity , said method comprising:contacting an initial inorganic material having long-range crystallinity with a non-ionic surfactant thereby forming said mesoporous inorganic material having long-range crystallinity,wherein said mesoporous inorganic material having long-range crystallinity has a total 20 to 135 Å diameter mesopore volume of at least 0.05 cc/g,wherein said mesoporous inorganic material having long-range crystallinity has a crystalline content of at least 20 weight percent as measured by X-ray diffraction (“XRD”).2. The method of claim 1 , wherein said mesoporous inorganic material having long-range crystallinity has a total 20 to 135 Å diameter mesopore volume of at least 0.1 cc/g.3. The method of claim 1 , wherein said mesoporous inorganic material having long-range crystallinity has a crystalline content of at least at least 40 weight percent as measured by XRD.4. The method of claim 1 , wherein said mesoporous inorganic material having long-range crystallinity has a total 0 to 20 Å diameter micropore volume in the range of from about 0 to about 0.40 cc/g.5. The method of claim 1 , wherein said mesoporous inorganic material having long-range crystallinity has a total 20 to 135 Å diameter mesopore volume that is at least 50 percent greater than the 20 to 135 Å diameter mesopore volume of said initial inorganic material having long-range crystallinity.6. The method of ...

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18-07-2013 дата публикации

INTRODUCTION OF MESOPOROSITY INTO LOW SILICA ZEOLITES

Номер: US20130183230A1
Принадлежит: Rive Technology, Inc.

Mesoporous X and A zeolites and methods for production thereof are disclosed herein. Such mesoporous zeolites can be prepared by contacting an initial zeolite with an acid in conjunction with a mesopore forming agent. The initial zeolite can have a framework silicon-to-aluminum content in the range of from about 1 to about 2.5. Additionally, such mesoporous zeolites can have a total 20 to 135 Å diameter mesopore volume of at least 0.05 cc/g. 1. A method of forming a material comprising a mesoporous zeolite , said method comprising:(a) contacting an initial zeolite with a mesopore forming agent thereby forming a first treatment mixture comprising said initial zeolite and said mesopore forming agent; and(b) introducing an acid into said first treatment mixture thereby forming a second treatment mixture comprising said mesoporous zeolite, said mesopore forming agent, and said acid,wherein said initial zeolite has a framework silicon-to-aluminum ratio (“Si/Al”) in the range of from about 1 to about 2.5.2. The method of claim 1 , wherein said mesoporous zeolite has a total 20 to 135 Å diameter mesopore volume of at least 0.05 cc/g.3. The method of claim 1 , wherein said mesoporous zeolite has a crystalline content of at least 10 weight percent as measured by X-ray diffraction (“XRD”).4. The method of claim 1 , wherein said mesoporous zeolite has a total 20 to 135 Å diameter mesopore volume that is at least 0.02 cc/g greater than the 20 to 135 Å diameter mesopore volume of said initial zeolite.5. The method of claim 1 , wherein said initial zeolite is selected from the group consisting of zeolite A and zeolite X.6. The method of claim 1 , wherein said mesoporous zeolite is a mesostructured zeolite.7. The method of claim 1 , wherein said acid is present in an initial amount in the range of from about 1 to about 10 milliequivalents per gram of said initial zeolite.8. The method of claim 1 , wherein said acid is present in an initial amount in the range of from about 2 to ...

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08-08-2013 дата публикации

ABSORBENT MULTILAYER COATING SYSTEM

Номер: US20130202785A1
Принадлежит: AKZO NOBEL COATINGS INTERNATIONAL B.V.

The invention relates to a peelable multilayer coating system comprising a) a peelable coating layer and b) an absorbent top coating layer pigmented above the critical pigment volume concentration, and wherein the pigment comprises mesoporous inorganic particles. 1. A peelable multilayer coating system comprisinga) a peelable coating layer andb) an absorbent top coating layer pigmented above the critical pigment volume concentration, and wherein the pigment comprises mesoporous inorganic particles.2. The peelable multilayer coating system according to claim 1 , wherein the mesoporous inorganic particles are mesoporous silica particles.3. The peelable multilayer coating system according to claim 1 , wherein the pigment consists essentially of mesoporous inorganic particles.4. The peelable multilayer coating system according to claim 1 , wherein the mesoporous inorganic particles have an oil absorption value of at least 100.5. The peelable multilayer coating system according to claim 1 , wherein layer a) and layer b) have a common layer boundary.6. The peelable multilayer coating system according to claim 1 , wherein the peelable coating layer a) comprises solid particles of an amino resin based polymer.7. A process of temporary protection of a substrate from a contaminant claim 1 , comprising the steps ofa) applying to the substrate a multilayer coating system comprising a peelable coating layer and an absorbent top coating layer pigmented above the critical pigment volume concentration, and wherein the pigment comprises mesoporous inorganic particles, andb) exposing the substrate to a contaminant wherein at least a part of the contaminant is absorbed in the absorbent top coating layer.8. The process according to claim 7 , further comprising the additional step ofc) removing the multilayer coating system from the substrate by peeling.9. The process according to claim 7 , wherein the peelable coating layer is prepared from an aqueous coating composition.10. The ...

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15-08-2013 дата публикации

METHOD FOR OPERATING AN ON-SITE MEDICAL GAS PRODUCTION PLANT AND ASSOCIATED PLANT

Номер: US20130205997A1

The invention relates to a method for operating a plant () for on-site production of medical gas, such as air or oxygen, comprising a main gas line () comprising, in series, a first vessel (A) for storing gas and a second vessel (B) for storing purified gas, and a secondary line () fluidically connected to the main line (), downstream of the first vessel (A) for storing gas, and comprising a third vessel (C) for storing gas, the main gas line () and the secondary line () each supplying at least one gas consumer site (), in particular a network of pipes in a hospital. 1100. An on-site medical gas production plant () , comprising:{'b': '50', 'a gas purification unit () adapted to produce a purified gas from a supply gas,'}{'b': 10', '10, 'a main gas line () supplied with a gas by the gas purification unit () and comprising, in series, a first vessel (A) for storing a less pure gas and a second vessel (B) for storing a purified gas, and'}{'b': 20', '10, 'a secondary line () fluidically connected to the main line (), downstream of the first vessel (A) for storing the less pure gas and comprising a third vessel (C) for storing gas,'}{'b': 1', '2, 'at least one gas analysis device (D; D) arranged so as to determine the level of at least one given impurity in the gas, downstream of the second (B) and third (C) vessels,'}{'b': 1', '10, 'a first solenoid valve (V), arranged on the main gas line () between the first vessel (A) for storing the less pure gas and a second vessel (B) for storing the purified gas,'}{'b': 3', '20, 'a second solenoid valve (V), arranged on the secondary gas line () between the first vessel (A) and the third vessel (C) for storing gas,'}{'b': 2', '10, 'a third solenoid valve (V), arranged on the main gas line () downstream of the second vessel (B) for storing the purified gas,'}{'b': 4', '20, 'a fourth solenoid valve (V), arranged on the secondary gas line () downstream of the third vessel (C) for storing gas, and'}{'b': 4', '1', '4', '1', '2, 'an ...

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14-11-2013 дата публикации

MULTILAYERED MIXED BED FILTER FOR THE REMOVAL OF TOXIC GASES FROM AIR STREAMS AND METHODS THEREOF

Номер: US20130302231A1
Принадлежит:

To achieve the removal of a broad spectrum of chemical hazards, multiple layers of impregnated activated carbon and nanocrystalline materials are incorporated into the adsorbent bed. For optimum performance using the least amount of material, a two-layer configuration is used. The top layer consists of a homogeneous mixture of an MgO/CaO based nanocrystalline material (e.g., Mg/Ca) and Kureha or other petroleum pitch-based bead shaped activated carbon impregnated treated with phosphoric acid. The bottom layer is comprised of a single layer of Calgon URC carbon. The volume ratios of the components are 9:5:11 Mg/Ca, phosphoric acid treated Kureha carbon, and URC, respectively. The new configuration leads to a 30% reduction in size of the existing NIOSH CBRN CAP 1 cartridge. Other embodiments are disclosed and claimed. 1. A filter media , comprising:a first plurality of filter media particles comprising a high surface area substrate comprising at least one acidic impregnant;a second plurality of filter media particles comprising a high surface area substrate comprising at least one metal oxide; and,a third plurality of filter media particles comprising a high surface area substrate containing an amine impregnant.2. The filter media of claim 1 , wherein each of said substrates is essentially free of chromium.3. The filter media of claim 1 , comprising first and second filter media layers;the first and second plurality of filter media are intermixed and are located in the first filter layer; andthe third plurality of filter media particles is located in the second filter layer.4. The filter media of claim 1 , wherein the acidic impregnant is phosphoric acid.5. The filter media of claim 1 , wherein the acidic impregnant has a maximum concentration of 10 percent.6. The filter media of claim 1 , wherein the metal oxide is selected from the list consisting of oxides of magnesium claim 1 , oxides of calcium claim 1 , and combinations thereof.7. The filter media of claim 1 , ...

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14-11-2013 дата публикации

High Capacity Solid Filtration Media

Номер: US20130302234A1
Автор: England William G.
Принадлежит:

A high capacity filtration media, method of preparing the media, and method of treating a fluid stream with the media are provided. The media contain a porous substrate impregnated with high concentrations of a permanganate. Preferably, the media includes a porous substrate impregnated with at least about 8% permanganate by weight. The media can optionally contain sodium bicarbonate. Improved capacity for the removal of undesirable compounds such as ethylene, formaldehyde, hydrogen sulfide and methyl mercaptan are achieved. 133-. (canceled)34. A method of treating a contaminated fluid stream comprising passing the contaminated fluid stream through a solid filtration composition such that at least one contaminant is removed from the fluid stream , wherein:the contaminated fluid stream is passed through the solid filtration composition at a velocity of from 10 to 750 ft/min;the solid filtration composition comprises particles with a nominal ⅛″ particle size, the particles consisting of a dry porous substrate, a permanganate and water;the permanganate is a permanganate salt having a solubility in water greater than that of potassium permanganate;the concentration of permanganate salt in the solid filtration composition is approximately 8-25% permanganate salt by weight; andthe porous substrate comprises activated alumina.35. The method of claim 34 , wherein the permanganate salt is selected from the group consisting of sodium permanganate claim 34 , magnesium permanganate claim 34 , calcium permanganate claim 34 , barium permanganate claim 34 , lithium permanganate and combinations thereof36. The method of claim 34 , wherein the solid filtration composition comprises at least about 13-25% permanganate salt by weight.37. The method of claim 34 , wherein the solid filtration composition comprises at least about 15-20% permanganate salt by weight.38. The method of claim 34 , wherein the permanganate salt comprises sodium permanganate.39. The method of claim 34 , wherein ...

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14-11-2013 дата публикации

ADSORPTION OF VOLATILE ORGANIC COMPOUNDS DERIVED FROM ORGANIC MATTER

Номер: US20130303359A1
Принадлежит:

An article for adsorbing volatile organic compounds (VOCs) derived from organic matter comprising adsorbing the VOCs onto palladium doped ZSM-5, optionally at ambient temperature. The organic matter can be perishable organic goods such as food, including fruit and/or vegetables, horticultural produce, including plants and/or cut flowers, or refuse. The palladium doped ZSM-5 has a Si:Al ratio of less than or equal to 100:1 and preferably has a palladium content of from 0.1 wt % to 10.0 wt % based on the total weight of the doped ZSM-5. 1. An article comprising:palladium doped hydrogen-ZSM-5, wherein the Si:Al ratio of the hydrogen-ZSM-5 is less than or equal to 100:1, and further wherein the article is a label, sachet or ink.2. The article of claim 1 , wherein the palladium comprises from 0.1 wt % to 10.0 wt % based on the total weight of the doped hydrogen-ZSM-5.3. The article of claim 1 , wherein the palladium doped hydrogen-ZSM-5 is particulate matter.4. The article of claim 3 , wherein the particulate matter is in the form of extrudates claim 3 , pellets claim 3 , tablets claim 3 , grains claim 3 , granules claim 3 , powder claim 3 , or a combination thereof.5. The article of claim 1 , further comprising a gas permeable barrier layer.6. The article of claim 5 , wherein the gas permeable barrier layer prevents direct contact of the palladium doped hydrogen-ZSM-5 with another object.7. The article of claim 6 , wherein the gas barrier layer forms at least a part of the label or sachet.8. The article of claim 1 , wherein the article further comprises a water adsorbing material.9. The article of claim 8 , wherein the water adsorbing material includes silica gel.10. The article of claim 1 , wherein the article is a label claim 1 , and further wherein the label includes a substrate configured for insertion or retention within a container claim 1 , package claim 1 , or crate.11. The article of claim 1 , wherein the palladium doped hydrogen-ZSM-5 is incorporated into or ...

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21-11-2013 дата публикации

Materials and methods for environmental contaminant remediation

Номер: US20130306555A1
Автор: Sandip Chattopadhyay
Принадлежит: Tetra Tech Inc

An anthropogenic sorbent material modified for sequestering and/or attenuating multiple chemical and/or biological pollutant species, both organic and inorganic, in an aqueous environment is disclosed as well as a method of sequestering and/or attenuating multiple chemical and/or biological pollutant species, both organic and inorganic, in an aquatic ecosystem by capping at least a portion of a sedimentary basin of the aquatic ecosystem.

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28-11-2013 дата публикации

Gas phase air filtration

Номер: US20130312605A1
Принадлежит: Ticona LLC

An adsorbent medium for removing gaseous contaminants from air comprises a porous self-supporting filter element produced by sintering particles of polyethylene having a molecular weight greater than 400,000 g/mol as determined by ASTM-D 4020 and an adsorbent. In one embodiment, the filter element comprises a body perforated by a plurality of holes extending in the direction of fluid flow in use and having a diameter of less than 10 mm. In another embodiment, the filter element comprises a panel wherein at least the surface of the panel presented, in use, to the incoming air comprises a plurality of projections. In a further embodiment, the filter element comprises a fibrous web having particles of the adsorbent secured to the web by the sintered polyethylene.

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05-12-2013 дата публикации

Methods and Apparatus for Treating a Hydrocarbon Stream

Номер: US20130323134A1
Принадлежит: UOP LLC

Disclosed is an apparatus for removing water, nitrogen compounds, and unsaturated aliphatic compounds from a hydrocarbon feed stream including a water removal zone, a nitrogen removal zone, and an unsaturated aliphatic compound removal zone. By on aspect, the water removal zone includes a water selective adsorbent, the nitrogen removal zone includes a nitrogen selective adsorbent, and the unsaturated aliphatic compound removal zone includes an unsaturated aliphatic compound removal material.

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12-12-2013 дата публикации

RECYCLING CARBON DIOXIDE VIA CAPTURE AND TEMPORARY STORAGE TO PRODUCE RENEWABLE FUELS AND DERIVED PRODUCTS

Номер: US20130331616A1
Принадлежит: UNIVERSITY OF SOUTHERN CALIFORNIA

A method for recycling a carbon-containing greenhouse gas emissions such as carbon dioxide and methane (natural gas) or a hydrocarbon homolog thereof. The method includes the steps of capturing the emissions, sequestering them in an underground or undersea storage area, withdrawing them from the storage area after storage therein, and converting them to carbon-containing compounds such as methanol, dimethyl ether and derived products. Greenhouse gases such as carbon dioxide and methane are chemically recycled to provide a permanent and inexhaustible supply of carbon-containing fuels or products, which subsequently can be combusted or used without increasing the carbon dioxide content of the atmosphere. The method is thus effective in neutralizing or reducing the carbon footprint due to human activities related to combustion or use of carbon-containing fuels while providing a repeatedly sustainable carbon source. 121.-. (canceled)22. A method for controlling , neutralizing or decreasing the human carbon footprint of an entity by recycling carbon-containing gas emissions which have been captured and sequestered in an underground or undersea storage area , which method comprises withdrawing the gas from the storage area after sequestration or storage therein; and converting the gas to carbon-containing compounds to provide a renewable energy source while avoiding any unintended escape or release of the gas from the storage area , thus controlling , neutralizing or decreasing the carbon footprint of the entity.23. The method of claim 22 , wherein the renewed carbon-containing compounds are carbon-containing fuels or synthetic hydrocarbons.24. The method of claim 22 , wherein the carbon-containing compounds are methanol claim 22 , dimethyl ether claim 22 , or products derived therefrom.25. The method of claim 22 , wherein the carbon-containing gas emissions are methane claim 22 , natural gas or hydrocarbon homologs thereof.26. The method of claim 25 , wherein the carbon- ...

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26-12-2013 дата публикации

Composite absorbent for catalyst residues removal from polyolefin solution polymerization mixture

Номер: US20130341563A1
Принадлежит: Reliance Industries Ltd

A solid shaped composite adsorbent for reducing deactivated catalyst residues and contaminants from a post polyolefin solution polymerization mixture is disclosed. The composite adsorbent comprises 70-90 wt % of an alumina component; 30-10 wt % of a clay component; and 0.5-3.5 wt % of at least one alkali metal component selected from the group consisting of elements in Group 1A of the modern periodic table.

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26-12-2013 дата публикации

SOLAR CELL HAVING FAN STRUCTURE AND APPLICATION SYSTEM USING THE SAME

Номер: US20130342153A1

Disclosed are a solar cell having a fan structure that provides a more pleasant life, convenience, and stability by forming, in a fan structure, a flexible colour solar cell applied with a carbon dioxide absorption material, and configuring the formed flexible colour solar cell through convergence of information technology, and an electronic application apparatus using the same. The electronic application apparatus using a solar cell as a power source includes: an application device body portion including a both side supporter fixed to ground, a transmitter including an antenna capable of transmitting power and data, and a data screen to thereby provide a predetermined service; and the solar cell provided in an upper end of the application device body portion, to colour using a predetermined wavelength of light, and to perform solar power generation using a remaining wavelength of light. 1. A solar cell having a fan structure , comprising:at least two solar cell panels to colour using a predetermined wavelength of light, and to perform solar power generation using a remaining wavelength of light, wherein the at least two solar cell panels are spaced apart from each other and thereby are disposed in a fan structure for a venturi effect; anda carbon dioxide absorption material, which is applied on the surface on which the at least two solar cell panels face each other,wherein exterior air flows into a gap space of the fan structure, and carbon dioxide of the in-flown outside air is absorbed by the carbon dioxide absorption material.2. The solar cell of claim 1 , wherein the solar cell panel is any one of a dye-sensitized solar cell (DSSC) claim 1 , an organic photovoltaic cell (OPV) claim 1 , an amorphous silicon solar cell claim 1 , and an inorganic substance of a solar cell.3. An electronic application apparatus that uses a solar cell as a power source claim 1 , the apparatus comprising:an application device body portion including a both side supporter fixed to ...

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16-01-2014 дата публикации

Device and method for enhanced collection and assay of chemicals with high surface area ceramic

Номер: US20140017805A1
Принадлежит: Battelle Memorial Institute Inc

A method and device for enhanced capture of target analytes is disclosed. This invention relates to collection of chemicals for separations and analysis. More specifically, this invention relates to a solid phase microextraction (SPME) device having better capability for chemical collection and analysis. This includes better physical stability, capacity for chemical collection, flexible surface chemistry and high affinity for target analyte.

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06-02-2014 дата публикации

WATER-BLOCKING FILLER AND FILLER FOR MANMADE MULTI-BARRIERS USING SAID WATER-BLOCKING FILLER

Номер: US20140034875A1
Принадлежит:

Provided are a water-blocking filler, the swelling properties of which do not decrease easily even when in contact with water containing calcium ions, and a filler for engineered multi-barriers with said water-blocking filler as the engineered multi-barrier filler. A water-blocking filler mainly comprising sodium bentonite obtained by mixing 30 weight % or less, in terms of inner percentage, of a pozzolan substance such as fly ash or silica fume with said bentonite, and a filler using said water-blocking filler that is used for engineered multi-barriers in radioactive waste disposal facilities. 1. A water-blocking filler mainly comprising sodium type bentonite , wherein 30% by weight or less , in terms of inner percentage , of a pozzolan substance is mixed with said bentonite.2. The water-blocking filler according to claim 1 , wherein said pozzolan substance includes either fly ash or silica fume.3. An engineered multi-barrier filler obtained using the water-blocking filler according to claim 1 , wherein said engineered multi-barrier filler is used for engineered multi-barriers in radioactive waste disposal facilities.4. An engineered multi-barrier filler obtained using the water-blocking filler according to claim 2 , wherein said engineered multi-barrier filler is used for engineered multi-barriers in radioactive waste disposal facilities. This invention relates to a water-blocking filler of non-cement based type mainly comprising bentonite, and also an engineered multi-barrier filler using the above water-blocking filler used for engineered multi-barriers in the radioactive waste disposal facilities.Bentonite is not only some type of material excellent in water absorption performance but also has the functional effect of permitting a decrease in water permeability in such a manner that the bentonite gets swollen to cause water-permeable voids to be decreased. Besides, the bentonite belongs in natural clay minerals and is thus considered to be a stable material ...

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20-02-2014 дата публикации

Mercury sorbents

Номер: US20140050641A1
Принадлежит: ECOLAB USA INC

Disclosed are methods for the on-site manufacture of aqueous-based mercury sorbent compositions prepared using a process water. The sorbent compositions may be aqueous-based materials manufactured from a silica containing precursor, a metal species, and a sulfur-based species, in the presence of a process waters, such as a process water from a coal-fired power plant.

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27-03-2014 дата публикации

GAS STREAM TREATMENT PROCESS

Номер: US20140084209A1
Принадлежит:

A process of treating a gas stream containing mercury and acid gas pollutants is disclosed. The process includes applying a sorbent composition into a gas stream in order to adsorb mercury containing compounds and acid gas pollutants. The sorbent composition includes a compound having the formula (SiO)x(OH)MSF.B. The combination of basic inorganic solids for the adsorption of acid gases, and metal sulfide-doped silica for the adsorption of mercury provides dual sorbent functionality, along with additional benefits for each individual sorbent: silica for moisture retention on the surface of the basic inorganic particle and adsorption of acid gas, which will improve metal sulfide performance at higher operating temperatures. The use of a hygroscopic solid effectively dries the metal sulfide-doped silica slurry without the use of filtration of drying equipment, providing significant economic benefit for the manufacture of metal sulfide-doped silica material. 1. A composition comprising a compound having formula (I) ,{'br': None, 'sub': 2', 'x', 'y', 'z', 'a, '(SiO)(OH)MSF.B\u2003\u2003(I)'}whereinM is a metal or metalloid cation selected from the group consisting of boron, magnesium, aluminum, calcium, titanium, vanadium, manganese, iron, cobalt, nickel, copper, zinc, zirconium, molybdenum, palladium, silver, cadmium, tin, platinum, gold, and bismuth;S is a sulfur-based species selected from the group consisting of at least one of the following: sulfide salts, dithiocarbamates, polymer-based dithiocarbamates, and polysulfide salts;F optionally exists and said F is at least one of the following: a functionalized organosilane, a sulfur-containing organosilane, an amine-containing organosilane, or an alkyl-containing organosilane at a surface area coverage of about 0.01 to about 100%;B is a basic inorganic solid selected from alkali or alkali-earth metal oxides, hydroxides, carbonates, and bicarbonates, said basic inorganic solid containing a metal cation selected from ...

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27-03-2014 дата публикации

ADSORBENT GRANULATE AND METHOD FOR THE MANUFACTURE THEREOF

Номер: US20140086817A1
Принадлежит:

The invention relates to a X-zeolite based adsorbent granulate with faujasite structure and a molar SiO/AlOratio of ≧2.1-2.5, wherein the granulate has an average transport pore diameter of >300 nm and a negligible fraction of meso-pores and wherein the mechanical properties of the granulate are at least the same as or better than the properties of an X-zeolite based granulate formed using an inert binder and the equilibrium adsorption capacities for water, COand nitrogen are identical to those of pure X-zeolite powder with a similar composition. 13-. (canceled)4. A method for producing an adsorption agent granulate , comprising: a X-type zeolite with a molar SiO/AlOratio ≧2.1-2.5 provided as a dry powder , filter cake or slurry being mixed at a weight ratio of 1:1 to 1:5 with a thermally treated kaoline with a mean particle diameter in a range of ≦10 μm which may include <5 mass % non kaolinitic material , the mixture being then mixed with a mixture of sodium hydroxide and sodium silicate solution , the mixture being formed into a granulate with the granulate being subjected to a drying process and subsequently hydrated with completely de-salinated water and treated with a sodium aluminate solution at temperatures in a range of 70° C.-90° C. over a time period of up to 24 hours , and then the granulate thus treated being separated from the solution , washed , dried and tempered.5. A method according to claim 4 , wherein the temperature for thermally treating the kaoline is in a range of 600° C. to 850° C.6. A method according to claim 4 , wherein the ratio of washing water to granulate is in a range of 5:1 to 40:1 claim 4 , preferably in a range of 8:1 to 20:1.7. A method according to claim 4 , wherein the hydrated granulate is treated with a solution including thinned sodium hydroxide solution with an addition of sodium aluminate solution.8. A method according to claim 7 , wherein the ratio of solution to granulate is in a range of 5:1 to 40:1 claim 7 , preferably ...

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03-04-2014 дата публикации

Gas separation adsorbents and manufacturing method

Номер: US20140094359A1
Принадлежит: Praxair Technology Inc

The present invention generally relates to high rate adsorbents and a method for their manufacture involving the steps of component mixing, extrusion, spheronization and calcination. The component mixing can involve both dry mixing in addition to wet mixing of an adsorbent with a binder, if required, and a fluid such as water. The paste so formed from the mixing stage is extruded to produce pellets which are optionally converted to beads by spheronization using in one embodiment, a marumerizer. The product is harvested and calcined to set any binder or binders used and/or burn out any additives or processing aids. This basic manufacturing scheme can be augmented by extra processing steps including ion exchange and activation to alter the composition of the adsorbents, as required.

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10-04-2014 дата публикации

METHOD FOR MANUFACTURING MICROPARTICULATE ANATASE OR RUTILE TITANIUM OXIDE DISPERSION AND COMPONENT HAVING PHOTOCATALYTIC THIN FILM ON SURFACE

Номер: US20140100105A1
Принадлежит: SHIN-ETSU CHEMICAL CO., LTD.

A method for manufacturing a microparticulate anatase or rutile titanium oxide dispersion from a peroxotitanic acid solution optionally containing tin, wherein the method for manufacturing an anatase or rutile titanium oxide dispersion is characterized in that the peroxotitanic acid solution is fed continuously to a flow reactor and subjected to hydrothermal treatment at 150 to 250° C. and 0.5 to 10 MPa. The invention makes it possible to provide a method for manufacturing a microparticulate anatase or rutile titanium oxide dispersion having excellent stability in regard to the titanium oxide microparticles and enabling a high-transparency photocatalytic thin film to be produced, and to provide a member having a photocatalytic thin film formed on the surface using this dispersion. 1. A method for manufacturing an anatase titanium oxide ultrafine particle dispersion from a peroxotitanic acid solution , comprising the steps of continuously feeding a peroxotitanic acid solution to a flow reactor and subjecting it to hydrothermal treatment at 150 to 250° C. and 0.5 to 10 MPa.2. The method of wherein the titanium oxide ultrafine particles in the anatase titanium oxide ultrafine particle dispersion have a 50% particle diameter (D) in the cumulative distribution on volume basis of up to 50 nm as measured by the dynamic scattering method using laser light.3. The method of or wherein the peroxotitanic acid solution continuously fed to the flow reactor is heated to the predetermined hydrothermal reaction temperature within 2 minutes.4. The method of wherein the titanium oxide ultrafine particle dispersion obtained from hydrothermal treatment of the peroxotitanic acid solution is subsequently cooled to or below 40° C. within 2 minutes.5. The method of wherein a reaction time in the flow reactor is adjusted such that the peroxotitanic acid solution may be converted to the titanium oxide ultrafine particle dispersion at a conversion rate of 95 to 99.5%.6. The method of wherein a ...

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07-01-2016 дата публикации

PROCESSES USING MOLECULAR SIEVE SSZ-98

Номер: US20160001273A1
Принадлежит: Chevron U.S.A. Inc

Uses for a new crystalline molecular sieve designated SSZ-98 are disclosed. SSZ-98 has the ERI framework type and is synthesized using a N,N′-dimethyl-1,4-diazabicyclo[2.2.2]octane dication as a structure directing agent. 3. The process of claim 2 , wherein the light olefins are ethylene claim 2 , propylene claim 2 , butylene claim 2 , or mixtures thereof.4. The process of claim 2 , wherein the oxygenate is methanol claim 2 , dimethyl ether claim 2 , or a mixture thereof.7. The process of claim 6 , wherein the molecular sieve contains a metal or metal ions capable of catalyzing the reduction of the oxides of nitrogen.8. The process of claim 7 , wherein the metal is lanthanum claim 7 , chromium claim 7 , manganese claim 7 , iron claim 7 , cobalt claim 7 , rhodium claim 7 , nickel claim 7 , palladium claim 7 , platinum claim 7 , copper claim 7 , zinc claim 7 , or mixtures thereof.9. The process of claim 6 , wherein the gas stream is the exhaust stream of an internal combustion engine.11. The process of claim 10 , wherein the engine is an internal combustion engine.12. The process of claim 11 , wherein the internal combustion engine is an automobile engine.13. The process of claim 10 , wherein the engine is fueled by a hydrocarbon fuel.14. The process of claim 10 , wherein the molecular sieve has deposited on it a metal selected from the group consisting of ruthenium claim 10 , rhodium claim 10 , palladium claim 10 , platinum claim 10 , and mixtures thereof.15. The process of claim 14 , wherein the metal is palladium claim 14 , platinum claim 14 , or a mixture thereof. This application claims the priority benefit of U.S. Provisional Application No. 62/020,638, filed Jul. 3, 2014, which is incorporated herein by reference.This disclosure relates to new crystalline molecular sieve designated SSZ-98, a method for preparing SSZ-98 using a N,N′-dimethyl-1,4-diazabicyclo[2.2.2]octane dication as a structure directing agent (“SDA”), and uses for SSZ-98. These materials have ...

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02-01-2020 дата публикации

Process and System for Treating Waste Water

Номер: US20200001208A1
Принадлежит: Kytolink Tech Pte. Ltd.

The present invention relates to a waste water treatment process and system for treatment of waste water utilizing a diatomite treatment agent containing about 98 to 99.9% by weight of diatomite particles, wherein the diatomite particles comprise unbalanced surface charges and is substantially free of counter ions being electrostatically coupled to the unbalanced surface charges, and wherein the diatomite treatment agent is obtained from the disclosed pre-treatment process. This diatomite treatment agent has posed several advantages in a waste water treatment process, particularly acting as a biomass carrier, physical coagulant and adsorbent in a system for treatment of waste water, the system comprising a specially designed clarifier. 1. A waste water treatment process comprising the steps of:a) contacting microbes with a waste water stream to form a mixed liquor stream comprising activated sludge;b) dosing said mixed liquor stream with at least one diatomite treatment agent;c) separating water from said mixed liquor stream to thereby provide a treated waste water effluent; andwherein optionally, said contacting step and said dosing step are performed concurrently or sequentially,wherein said diatomite treatment agent comprises 98 to 99.9% by weight of diatomite particles, said diatomite particles comprising unbalanced surface charges, andwherein said diatomite treatment agent is obtained from a pre-treatment process comprising: contacting crude diatomite with a treatment solution to form a slurry, the treatment solution comprising, based on the weight of the crude diatomite, about 0.03-0.05 wt. % of at least one xanthine derivative, about 0.1-0.2 wt. % of at least one metal metasilicate, about 0.025-0.05 wt. % of at least one metal phosphate, about 0.01-0.025 wt. % of at least one base and about 0.015-0.035 wt. % of at least one metal carbonate.2. The process of claim 1 , wherein said diatomite treatment agent consists essentially of diatomite cells claim 1 , said ...

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02-01-2020 дата публикации

Gas Sensor and Method for Producing Same

Номер: US20200001223A1
Принадлежит:

The filter of a gas sensor comprises an inorganic porous support supporting both an organic sulfonic acid compound including sulfo group (—SO3H) and a Lewis acid having at least a metal element of transitional metal elements, Al element, Ga element, In element, Ge element, and Sn element. The Lewis acid loaded in the inorganic porous support adsorbs low concentration siloxanes. The organic sulfonic acid compound including sulfo group polymerizes adsorbed siloxanes in the filter so as not to desorb from the filter. 1. A gas sensor comprising a gas sensing element and a filter arranged at a position nearer to atmospheres to be detected than the gas sensing element ,wherein said filter comprises an inorganic porous support supporting both an organic sulfonic acid compound including sulfo group (—SO3H) and a Lewis acid having at least a metal element of transitional metal elements, Al element, Ga element, In element, Ge element, and Sn element.2. The gas sensor according to claim 1 , wherein said inorganic porous support includes at least a member consisting of a group of plate-like mesoporous silica claim 1 , silica-gel other than mesoporous silica claim 1 , and alumina.3. The gas sensor according to claim 2 , wherein said inorganic porous support includes silica-gel other than mesoporous silica.4. The gas sensor according to claim 1 , wherein the metal element is at least one element of elements having atomic number from 21 to 32 claim 1 , Y claim 1 , Zr claim 1 , Nb claim 1 , Mo claim 1 , Hf claim 1 , Ta claim 1 , W claim 1 , In claim 1 , and Sn.5. The gas sensor according to claim 1 , wherein said filter is obtainable by fixing said metal element in the inorganic porous support and then claim 1 , loading said organic sulfonic acid compound in the inorganic porous support.6. The gas sensor according to claim 1 , wherein said Lewis acid includes an oxide of said metal element.7. The gas sensor according to claim 1 , wherein said metal element is solved in said ...

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04-01-2018 дата публикации

VOC AND ODOR REDUCING BUILDING PANELS

Номер: US20180001297A1
Принадлежит:

Described herein is a building panel comprising a substrate and an odor and VOC reducing coating applied to the substrate, the coating comprising a blend of a first component comprising ethylene urea; a second component comprising silica; and a rheology modifier. 1. A method of forming a VOC and odor-reducing building panel comprisingproviding a substrate; ethylene urea;', 'silica gel; and', 'carrier comprising water;, 'applying a wet-state coating to a major surface of the substrate, the wet-state coating comprisingdrying the wet-state coating, thereby evaporating at least 95 wt. % of the carrier to form a dry-state coating.2. The method according to claim 1 , wherein the wet-state coating is applied to a major surface of the substrate in an amount ranging from about 100 g/mto about 1000 g/m.3. The method according to claim 1 , wherein the dry-state coating is present on the substrate in an amount ranging from about 50 g/mto about 400 g/m.4. The method according to claim 1 , wherein the wet-state coating further comprises a rheology modifier selected from silicate mineral claim 1 , alkali-swellable compounds claim 1 , and combinations thereof.5. The method according to claim 4 , wherein the rheology modifier is present in an amount ranging from about 0.5 wt. % to about 55 wt. % based on the total weight of the dry-state coating.6. The method according to wherein the water is present in an amount ranging from about 25 wt. % to about 75 wt. % based on the total weight of the wet-state coating.7. The method according to claim 1 , wherein the wet-state coating has a viscosity ranging from about 200 cps to about 4 claim 1 ,000 cps as measured on a Brookfield viscometer at 10 RPM at room temperature.8. A VOC and odor-reducing coating composition comprising:ethylene urea;silica gel; andwater.9. The building panel according to claim 8 , wherein the wet-state coating further comprises a rheology modifier selected from silicate mineral claim 8 , alkali-swellable compounds ...

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02-01-2020 дата публикации

Multilayer articles including coatings containing metal on microfiltration membrane substrates

Номер: US20200001249A1
Принадлежит: 3M Innovative Properties Co

The present disclosure provides a multilayer article. The multilayer article includes a) a microfiltration membrane substrate, the microfiltration membrane substrate having a first major surface; and b) a first layer having a first major surface and a second major surface disposed opposite the first major surface. The first major surface of the first layer is directly attached to the first major surface of the microfiltration membrane substrate. The first layer includes a first polymeric binder and a plurality of acid-sintered interconnected first silica nanoparticles arranged to form a continuous three-dimensional porous network. The multilayer article further includes c) a second layer attached to the second major surface of the first layer. The second layer includes i) a metal coating or ii) a composite coating comprising a second polymeric binder and at least one of metal nanoparticles or metal nanowires.

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05-01-2017 дата публикации

Egg-shell type hybrid structure of highly dispersed nanoparticle-metal oxide support, preparation method thereof, and use thereof

Номер: US20170001168A1
Принадлежит: Korea Institute of Energy Research KIER

The present invention relates to an egg-shell type hybrid structure of highly dispersed nanoparticles-metal oxide support, a preparation method thereof, and a use thereof. Specifically, the present invention relates to an egg-shell type hybrid structure of highly dispersed nanoparticles-metal oxide support, providing an excellent platform in a size of nanometers or micrometers which can support nanoparticles selectively in the porous shell portion by employing a metal oxide support with an average diameter of nanometers or micrometers including a core of nonporous metal oxide and a shell of porous metal oxides, a preparation method thereof, and a use thereof.

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05-01-2017 дата публикации

PASSIVE NOx ADSORBER

Номер: US20170001169A1
Принадлежит:

A passive NOadsorber is disclosed. The passive NOadsorber is effective to adsorb NOat or below a low temperature and release the adsorbed NOat temperatures above the low temperature. The passive NOadsorber comprises a noble metal and a molecular sieve having an LTL Framework Type. The invention also includes an exhaust system comprising the passive NOadsorber, and a method for treating exhaust gas from an internal combustion engine utilizing the passive NOadsorber. 1. A passive NOadsorber effective to adsorb NOat or below a low temperature and release the adsorbed NOat temperatures above the low temperature , said passive NOadsorber comprising a first noble metal and a molecular sieve having an LTL Framework Type.2. The passive NOadsorber of wherein the first noble metal is selected from the group consisting of platinum claim 1 , palladium claim 1 , rhodium claim 1 , gold claim 1 , silver claim 1 , iridium claim 1 , ruthenium claim 1 , osmium claim 1 , and mixtures thereof.3. The passive NOadsorber of wherein the first noble metal is palladium.4. The passive NOadsorber of wherein the molecular sieve having an LTL Framework Type is selected from the group consisting of aluminosilicate zeolite claim 1 , an aluminophosphate zeolite claim 1 , a silicoaluminophosphate (SAPO) zeolite claim 1 , and a metal-substituted aluminosilicate or aluminophosphate zeolite.5. The passive NOadsorber of wherein the molecular sieve having an LTL Framework Type is selected from the group consisting of zeolite L claim 1 , Linde Type L claim 1 , gallosilicate L claim 1 , LZ-212 claim 1 , LTL-type SAPO claim 1 , and perlialite zeolite.6. The passive NOadsorber of wherein the passive NOadsorber is coated onto a flow-through or filter substrate.7. The passive NOadsorber of wherein the passive NOadsorber is extruded to form a flow-through or filter substrate.8. The passive NOadsorber of further comprising a second molecular sieve catalyst claim 1 , wherein the second molecular sieve catalyst ...

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02-01-2020 дата публикации

ULTRA-HIGH PERFORMANCE AND HIGH PURITY BIOGENIC SILICA FILTRATION MEDIA

Номер: US20200001267A1
Принадлежит: EP MINERALS, LLC

This disclosure relates to ultra-high performance diatomite products possessing very high silica specific volume, a characteristic which provides for high filtration performance, in terms of low unit consumption and long filtration cycle times. These novel products of this disclosure also show very low extractable metals for both the non-acid washed and the high purity (acid washed) grades. These characteristics are of particular value in the separation of solids from high purity liquids in electronic chemical, specialty beverage and life science applications. In addition to outstanding physical and chemical characteristics, these products also contain no detectable levels of cristobalite and have a wide range of permeabilities, and are produced from mineralogically impure ores containing high levels of alumina and iron oxide 1. The filtration product of comprising diatomaceous earth having: (i) a permeability of 85 millidarcy to 14 claim 39 ,000 millidarcy claim 39 , (ii) an aluminum oxide content and an iron oxide content claim 39 , wherein the sum of the aluminum oxide content and the iron oxide content is greater than 7.0 wt % and less than 13 (wt %) claim 39 , and (iii) a silica specific volume greater than 3.5 to 6.2.210-. (canceled)11. The filtration product of claim 39 , in which the diatomaceous earth further has a non-detectable level of cristobalite according to the LH Method.12. The filtration product of claim 39 , in which the diatomaceous earth further has a silica content of greater than 80 wt % and less than 84 wt % on an ignited basis.13. The filtration product of claim 39 , in which the diatomaceous earth further has a silica content of 84 wt % to 87 wt % on an ignited basis.14. The filtration product of claim 39 , in which the diatomaceous earth further has a silica content of greater than 88 wt % to 92 wt % on an ignited basis.15. The filtration product of claim 39 , wherein the iron oxide content is greater than 4 wt % on an ignited basis.16. ( ...

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03-01-2019 дата публикации

CALCIUM ALGINATE ADSORBENTS

Номер: US20190001300A1
Принадлежит:

A method of treating a liquid for removal of organic acid anions which comprises contacting a liquid containing organic acid anions with an adsorbent comprising calcium alginate-kaolinite or calcium alginate-quartz and a method of treating a liquid for removal of organic acid anions, heavy metal ions and thermally degraded organic products which comprises contacting a liquid containing organic acid anions, heavy metal ions and thermally degraded organic products with an adsorbent comprising calcium alginate-activated carbon are described. 1. A method of treating a liquid for removal of organic acid anions which comprises contacting a liquid containing organic acid anions with an adsorbent comprising calcium alginate-kaolinite (CAK) or calcium alginate-quartz (CAQ).2. The method of wherein the adsorbent is prepared by a process comprising adding drop-wise a mixed solution of alginate and kaolinite or quartz to a calcium chloride solution claim 1 , thereby cross linking alginate with calcium ions and finally get the adsorbent.3. The method of or which comprises passing of said liquid containing organic acid anions through a column containing said adsorbent in gel form.4. A method of treating a liquid for removal of organic acid anions claim 1 , heavy metal ions and thermally degraded organic products which comprises contacting a liquid containing organic acid anions claim 1 , heavy metal ions and thermally degraded organic products with an adsorbent comprising calcium alginate-activated carbon (CAC).5. The method of wherein the adsorbent is prepared by a process comprising adding drop-wise a mixed solution of alginate and activated carbon powder to calcium chloride solution to form a carbon impregnated CAC adsorbent.6. The method of or which comprises passing of said liquid containing organic acid anions claim 4 , heavy metal ions and thermally degraded organic products through a column containing said adsorbent in gel form.7. The method of any preceding claim wherein ...

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07-01-2016 дата публикации

METHOD OF PRODUCTION OF GRANULATED MICELLE-CLAY COMPLEXES: APPLICATION FOR REMOVAL OF ORGANIC, INORGANIC ANIONIC POLLUTANTS AND MICROORGANISMS FROM CONTAMINATED WATER

Номер: US20160002068A1
Автор: NIR Shlomo, RYSKIN Marklen
Принадлежит:

The present invention pertains to a complex comprising micelles of organic cation adsorbed on clay in granulated form, to a method for obtaining an aqueous solution substantially free of organic, inorganic anionic pollutants, or microorganisms present therein, comprising contacting the aqueous solution containing said pollutants with such a complex and to a system for obtaining an aqueous solution substantially free of organic, inorganic anionic pollutants, or microorganisms present therein employing the granulated complex. 1. A complex comprising micelles of organic cation adsorbed on clay in granulated form.2. A complex according to claim 1 , wherein the clay is an aggregate of hydrous silicate particles having a diameter of less than about 4 μm.3. A complex according to claim 2 , wherein the clay is selected from the group consisting of kaolinite-serpentine claim 2 , illite claim 2 , and smectite.4. A complex according to claim 1 , wherein the organic cation is an ammonium cation of the type XY wherein X is an R″—N(R′) claim 1 , R′ being each independently a Calkyl group claim 1 , an optionally substituted phenyl or an alkylphenyl group; R″ is C-C-alkyl claim 1 , preferably C-C-alkyl claim 1 , most preferably C-C-alkyl claim 1 , and Y is a counter ion.5. A complex according to claim 1 , further comprising activated carbon in an amount of about 3%-12% claim 1 , preferably 9%.6. A complex according to claim 1 , wherein the ratio of the organic cation and the clay is about 0.3:1 to about 0.6:1 (w/we) claim 1 , preferably about 0.4:1 to about 0.6:1 claim 1 , most preferably about 0.4:1 to about 0.5:1.7. A complex according to claim 6 , wherein the amount of the activated carbon being part of the total amount of the clay.8. A method for obtaining an aqueous solution substantially free of organic claim 6 , inorganic anionic pollutants claim 6 , or microorganisms present therein claim 6 , comprising contacting the aqueous solution containing said pollutants with a ...

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02-01-2020 дата публикации

Removing Arsenic from Water with Acid-Activated Clay

Номер: US20200002189A1
Автор: Fang Mingming
Принадлежит: FUEL TECH, INC.

The description relates to a composition and a method for reducing the concentration of arsenic in water. Contaminated water is contacted with acid-activated clay characterized by a removal efficiency for arsenic of at least 95 wt %. Following sufficient contact, the water is separated from the acid-activated clay. In preferred form, the acid activated clay is characterized by a BET surface area of at least about 200 m/gram. 1. A composition for removing arsenic from contaminated water comprises:a. an acid-activated clay selected from the group consisting of bentonite, montmorillonite, hectorite, talc, vermiculite, saponite, nontronite, kaolinite, halloysite, illite, and chlorite and mixtures thereof;b. a water-soluble oxidizer that can oxidize arsenite to arsenate at the ambient temperature and pressure in water.2. The composition of claim 1 , wherein the acid-activated clay is bentonite.3. The composition of claim 1 , wherein the acid-activated clay is generated by mixing the clay with an acid or acid solution or by incorporating the acid by kneading at a temperature between room temperature (20° C.) and 60° C. for at least 1 hour.4. The composition of claim 1 , wherein the acid activated clay has specific surface area of at least 100 m/g claim 1 , preferably has specific surface area of least 200 m/g.5. The composition of claim 1 , the oxidizer comprises chlorine.6. The composition of claim 5 , the oxidizer is calcium hypochlorite.7. A composition according to any preceding claim in unit dosage form for the batch wise arsenic removal of a relatively small predetermined volume of contaminated water.8. A composition according to any preceding claim in unit dosage form for treating a volume of contaminated water claim 5 , the acid-activated clay dosage to the volume of the contaminated water is in the range from about 1 to about 25 claim 5 , preferably 2 to about 15 claim 5 , more preferably from about 4 to about 10 g/liter of contaminated water.9. A composition ...

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03-01-2019 дата публикации

Synthesis of fibrous nano-silica spheres with controlled particle size, fibre density, and various textural properties

Номер: US20190002297A1
Принадлежит: TATA INSTITUTE OF FUNDAMENTAL RESEARCH

The present disclosure provides a method for synthesizing fibrous silica nanospheres, the method can include, in sequence, the steps of: a) providing a reaction mixture comprising a silica precursor, a hydrolyzing agent, a template molecule, a cosurfactant and one or more solvents; b) maintaining the reaction mixture under stirring for a length of time; c) heating the reaction mixture to a temperature for a length of time; d) cooling the reaction mixture to obtain a solid, and (e) calcinating the solid to pro duce fibrous silica nanospheres, wherein desirable product characteristics such as particle size, fiber density, surface area, pore volume and pore size can be obtained by controlling one or more parameters of the method. The present disclosure further provides a method for synthesizing fibrous silica nanospheres using conventional heating such as refluxing the reactants in an open reactor, thereby eliminating the need for microwave heating in a closed reactor or the need for any pressure reactors.

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03-01-2019 дата публикации

TREATMENT METHOD OF RADIOACTIVE WASTE WATER CONTAINING RADIOACTIVE CESIUM AND RADIOACTIVE STRONTIUM

Номер: US20190006055A1
Принадлежит:

A treatment method of radioactive waste water containing radioactive cesium and radioactive strontium, comprising passing the radioactive waste water containing radioactive cesium and radioactive strontium through an adsorption column packed with an adsorbent for cesium and strontium, to adsorb the radioactive cesium and radioactive strontium on the adsorbent, wherein the adsorbent for cesium or strontium comprises a crystalline silicotitanate having a crystallite diameter of 60 Å or more and having a half width of 0.9° or less of the diffraction peak in the lattice plane (100), the crystalline silicotitanate represented by the general formula: ATiSiO.nHO. 1. A treatment method of radioactive waste water containing radioactive cesium and radioactive strontium , comprising passing the radioactive waste water containing radioactive cesium and radioactive strontium through an adsorption column packed with an adsorbent for cesium and strontium , to adsorb the radioactive cesium and radioactive strontium on the adsorbent ,{'sub': 4', '4', '3', '16', '2, 'wherein the adsorbent for cesium or strontium comprises a crystalline silicotitanate having a crystallite diameter of 60 Å or more and having a half width of 0.9° or less of the diffraction peak in the lattice plane (100), the crystalline silicotitanate represented by the general formula: ATiSiO.nHO wherein A is Na or K or a combination thereof, and n represents a number of 0 to 8,'}wherein the adsorbent for cesium and strontium is a granular adsorbent having a grain size of 250 μm or more and 1200 μm or less,wherein the absorbent is packed to a height of 10 cm or more and 300 cm or less in the adsorption column, and{'sup': '−1', 'wherein the radioactive waste water is passed through the adsorption column at a linear velocity (LV) of 1 m/h or more and 40 m/h or less and a space velocity (SV) of 200 hor less.'}2. The treatment method according to claim 1 , wherein the radioactive waste water is waste water containing a Na ...

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12-01-2017 дата публикации

FRESHNESS RETAINING AGENT, METHOD FOR MANUFACTURING THE SAME, GAS PURIFICATION DEVICE, AND GAS PURIFICATION SYSTEM

Номер: US20170006887A1
Автор: Irie Yasuo
Принадлежит: TANKA CO., LTD.

Provided are a freshness retaining agent that can be obtained by a simple method and exhibits excellent adsorption performance and antibacterial activity, a gas purification device including the freshness retaining agent, and a gas purification system. The freshness retaining agent is formed by adhering tea catechins to a surface and/or an inside of charcoal powders and adhering the charcoal powders to each other with clay interposed between the charcoal powders, thereby exhibiting excellent adsorption performance and antibacterial activity. 1. A freshness retaining agent comprising charcoal powders , tea catechins and a clay , the tea catechins are adhered to a surface or an inside of the charcoal powders , or adhered to the surface and the inside of the charcoal powders , the charcoal powders being adhered with the clay interposed between the charcoal powders.2. The freshness retaining agent according to claim 1 ,wherein the charcoal powders are one or more selected from bamboo charcoals, wood charcoals, or activated charcoals.3. The freshness retaining agent according to claim 1 ,wherein the clay is one or more selected from bentonite, montmorillonite, hectorite, laponite, silica, starch, gelatin, guar gum, gum arabic, methyl cellulose, or ethyl cellulose.4. The freshness retaining agent according to claim 1 ,wherein a silver compound adheres to the surface and/or the inside of the charcoal powder.5. A gas purification device comprising a gas treatment unit that adsorbs gas components contained in a target gas using the freshness retaining agent according to .6. The gas purification device according to claim 5 , further comprising:a titanium oxide treatment unit that is coated with a titanium oxide; anda light source unit that irradiates the titanium oxide treatment unit with light.7. The gas purification device according to claim 6 ,wherein the light source unit is disposed oppositely to the coated surface of the titanium oxide treatment unit, andthe titanium ...

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12-01-2017 дата публикации

Perforated Adsorbent Particles

Номер: US20170007956A1
Принадлежит: AIR PRODUCTS AND CHEMICALS, INC.

An adsorption vessel comprising a packed bed region of adsorbent particles contiguously arranged comprising a perforated adsorbent particles, a gas separation process using the perforated adsorbent particles, and methods for making the perforated adsorbent particles. The perforated adsorbent particles each comprise an adsorbent material where the perforated adsorbent particles each have at least 10 channels extending through the particle. The equivalent diameter of the channels may range from 0.05 mm to 1.5 mm, and the void fraction of the channels may range from 0.05 to 0.5. 1. An adsorption vessel comprising:a packed bed region of adsorbent particles contiguously arranged, comprising a plurality of perforated adsorbent particles,wherein each perforated adsorbent particle comprises an adsorbent material capable of preferentially adsorbing at least one more strongly adsorbable gaseous component in a mixture comprising at least two gaseous components comprising the at least one more strongly adsorbable component and at least one less strongly adsorbable component, wherein the adsorbent material is a material selected from the group consisting of activated alumina, activated carbon, zeolites, mesopore-structured materials, carbon molecular sieve, metal-organic framework materials, silica gel, and combinations thereof; and{'b': '10', 'wherein each perforated adsorbent particle defines a respective plurality of channels numbering at least , the respective plurality of channels extending through each perforated adsorbent particle in a lengthwise direction from a first end to a second end.'}2. The adsorption vessel of wherein the plurality of perforated adsorbent particles number at least 100; andwherein the packed bed region has an interparticle void fraction ranging from 0.09 to 0.5.3. The adsorption vessel of wherein the adsorbent particles are irregularly arranged in the packed bed region.4. The adsorption vessel of wherein the adsorbent particles are contiguously ...

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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

METHOD FOR SELECTIVELY ISOLATING HYDROGEN OR HELIUM USING A NATROLITE-BASED ZEOLITE, AND NOVEL NATROLITE-BASED ZEOLITE

Номер: US20160008789A9
Автор: HONG Suk Bong
Принадлежит: POSTECH ACADEMY-INDUSTRY FOUNDATION

The present invention relates to selectively isolating gases using a natrolite-based zeolite, and more particularly, to a novel natrolite-based zeolite and to selectively isolating hydrogen and/or helium gas using a natrolite-based zeolite. The present invention is characterized in that gas containing hydrogen is brought into contact with a natrolite-based zeolite to selectively isolate the hydrogen. The present invention provides a sorbent which can selectively isolate hydrogen and/or helium, and provides a method for isolating the hydrogen and/or helium at room temperature or at a high temperature. 5. The method of claim 3 , wherein the compound of formula (2) is transferred into a Teflon reactor which is then placed in a stainless steel reactor in which the compound is heated. This application is a divisional of co-pending U.S. application Ser. No. 13/148,078 filed Sep. 6, 2011, which is a national phase entry of International Application Serial No. PCT/KR2009/005350 filed Sep. 21, 2009, which claims priority to Korean Application Serial Nos. 10-2009-0009716 filed Feb. 6, 2009 and 10-2009-0085610 filed Sep. 10, 2009, each of which is incorporated by reference herein in its entirety.The present invention relates to a novel natrolite-based zeolite and the selective separation of gases using the same, and more particularly to a process of selectively separating hydrogen or helium using a natrolite-based zeolite.Molecular sieves, including zeolites, have very small pores, the size of which is uniform within a variation of 0.1 Å and the shape of which varies depending on the framework structure of the molecular sieves, and thus these molecular sieves show unique shape-selective properties which are not observed in amorphous oxides. Accordingly, these nanoporous materials have been used as ion exchangers, separating agents, catalysts or catalyst supports, in the fine chemical industry, the petrochemical industry, and the like [Kirk Othmer Encyclo. Chem. Technol., 1996, ...

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11-01-2018 дата публикации

ZEOLITE ADSORBENTS HAVING A HIGH EXTERNAL SURFACE AREA AND USES THEREOF

Номер: US20180008955A1
Принадлежит: Arkema France

The present invention concerns the use, for gas separation, of at least one zeolite adsorbent material comprising at least one FAU zeolite, said adsorbent having an external surface area greater than 20 m·g, a non-zeolite phase (PNZ) content such that 0 Подробнее

14-01-2021 дата публикации

METHOD OF MANUFACTURING HIGH PACKING COMPOSITE ADSORBENT BED

Номер: US20210008523A1
Принадлежит:

An adsorbent bed, including at least one elementary composite structure that includes adsorbent particles in a polymer matrix, wherein the adsorbent bed has a bed packing, ρ, defined as a volume occupied by the at least one elementary composite structure Vdivided by a volume of the adsorbent bed Vwhere ρis greater than 0.60. 1. A method of manufacturing an adsorbent bed , comprising the steps of:forming at least one elementary composite polymer/adsorbent structure through diffusion induced phase inversion of a dope composition that comprises adsorbent particles, a solvent, and a polymeric binder dissolved in the solvent;forming an intermediate bed of the at least one elementary composite polymer/adsorbent structure; andcompressing the intermediate bed so as to immobilize the at least one elementary composite polymer/adsorbent structure against itself or each other and form a product bed.2. The method of claim 1 , wherein said steps of forming an intermediate bed and compressing the intermediate bed are repeated so as to form two or more of the product beds and said method further comprises the step of stacking the two or more of the product beds.3. The method of claim 1 , wherein the at least one elementary composite polymer/adsorbent structure comprises a plurality of elementary composite polymer/adsorbent beads or extrudates having an average major dimension Dmaj and an average minor dimension Dmin claim 1 , wherein a ratio of Dmaj:Dmin is in the range of 1:1 to less than 20:1.4. The method of claim 3 , wherein:The at least one elementary composite polymer/adsorbent structure is wetted with a liquid swelling agent causing the polymeric binder to soften and swell;said step of compressing the intermediate bed comprises the step of forcing a ram onto the intermediate bed during; andsaid method further comprises the step of allowing the product bed to dry.5. The method of claim 3 , wherein said step of compressing the intermediate bed comprises the steps of placing a ...

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10-01-2019 дата публикации

Self-Formaldehyde-scavenging heat-resistant ABS material and preparation method therefor

Номер: US20190009249A1
Принадлежит:

Disclosed are a self-formaldehyde-scavenging heat-resistant ABS material and a preparation method therefor. The material includes following components in parts by weight: 75-95 parts of an ABS resin, 4-20 parts of a heat-resistant agent, 0.5-5 parts of a formaldehyde-scavenging masterbatch, 0.1-1 part of a formaldehyde-scavenging agent and 0.5-1 part of other auxiliaries. During preparation, the ABS resin, the heat-resistant agent and the other auxiliaries are mixed and fed through a main feeding port of a twin-screw extruder; and the formaldehyde-scavenging masterbatch and the formaldehyde-scavenging agent are fed to a rear section of the extruder, extruded and pelletized. By the method of the present invention, the content of formaldehyde in particles can be reduced by 40%, and the content of formaldehyde in a closed space can be reduced by 50% or more. Moreover, the content of other volatile organic compounds is reduced by 10% to 20%. Thus, the effects of controlling the formaldehyde emission from a material for a long time and inhibiting the content of formaldehyde in a space are achieved. 3. The self-formaldehyde-scavenging heat-resistant ABS material composition according to claim 2 , wherein the physical adsorbent is one or two of diatomaceous earth and porous montmorillonite.4. The self-formaldehyde-scavenging heat-resistant ABS material composition according to claim 2 , wherein the formaldehyde capture agent is one or more members selected from a group consisting of melamine claim 2 , 2-imidazolidinone claim 2 , and carbohydrazide.5. The self-formaldehyde-scavenging heat-resistant ABS material composition according to claim 2 , wherein both the auxiliary A and the auxiliary B are one or more members selected from a group consisting of a hindered phenol antioxidant claim 2 , a phosphite antioxidant claim 2 , and a lubricant.6. The self-formaldehyde-scavenging heat-resistant ABS material composition according to claim 1 , wherein the formaldehyde-scavenging ...

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14-01-2021 дата публикации

Bayer Process

Номер: US20210009435A1
Принадлежит: Rio Tinto Alcan International Ltd

A Bayer process increases oxalate removal in the red side of the Bayer process and at least substantially minimises, for example by at least substantially suppressing, precipitation of oxalates in the white side of the Bayer process.

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14-01-2021 дата публикации

GETTER MATERIAL, METHOD FOR MANUFACTURING GETTER MATERIAL, METHOD FOR MANUFACTURING GETTER-MATERIAL-CONTAINING COMPOSITION, AND METHOD FOR MANUFACTURING GLASS PANEL UNIT

Номер: US20210009471A1
Принадлежит:

A method for manufacturing a glass panel unit, which reduces the amount of a getter material to enable a gettering ability to be realized at a relatively low temperature less likely to cause damage. The method includes a step of producing a getter material by heating an unprocessed getter material at a temperature higher than a prescribed temperature Te; a step of producing a preassembled component including a first and second glass pane, a heat-fusible sealing material, an internal space, and a gas adsorbent containing the getter material, and an evacuation port; a step of forming a frame body hermetically bonding the first glass pane and the second glass pane together by melting the heat-fusible sealing material with heat; and a step of heating the gas adsorbent at the prescribed temperature Te while the internal space is evacuated by exhausting air in the internal space through the evacuation port. 1. A method for manufacturing glass panel unit , the method comprising:a step of producing a getter material by heating an unprocessed getter material at a temperature higher than a prescribed temperature; a first glass pane,', 'a second glass pane facing the first glass pane,', 'a heat-fusible sealing material disposed between the first glass pane and the second glass pane, being in contact with the first glass pane and the second glass pane, and having a frame shape,', 'an internal space surrounded by the first glass pane, the second glass pane, and the heat-fusible sealing material having the frame shape,', 'a gas adsorbent containing the getter material and disposed in the internal space, and', 'an evacuation port connecting the internal space to an outside space;, 'a step of producing a preassembled component including'}a step of forming a frame body by melting the heat-fusible sealing material with heat such that the frame body hermetically bonds the first glass pane and the second glass pane together; anda step of heating the gas adsorbent at the prescribed ...

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10-01-2019 дата публикации

Metal-carrying zeolite for alcoholic beverages and alcoholic beverage manufacturing method

Номер: US20190010434A1

The metal-supported zeolite for alcoholic beverages of the present invention is a zeolite that carries a metal component, wherein the metal component is silver, and the zeolite is at least one selected from a beta-type one and a Y-type one. The metal-supported zeolite is for removing unwanted components contained in alcoholic beverages.

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09-01-2020 дата публикации

PROCESS FOR REMOVING ALKENE AND/OR ALKYNE FROM A HYDROCARBON FEEDSTOCK

Номер: US20200010385A1
Автор: SURIYE Kongkiat
Принадлежит: SCG Chemicals Co., Ltd.

The present invention relates to a process for purifying a hydrocarbon feedstock, said process comprising the steps: (a) providing the hydrocarbon feedstock comprising an aromatic compound and at least one compound, selected from the group consisting of alkene, alkyne, nitrogen-containing compound or mixtures thereof; and (b) contacting the hydrocarbon feedstock with an acidic montmorillonite adsorbent at a temperature in the range from 10 to 60° C. 1. A process for purifying a hydrocarbon feedstock , said process comprising the steps:(a) providing the hydrocarbon feedstock comprising an aromatic compound and at least one compound, selected from the group consisting of alkene, alkyne, nitrogen-containing compound or mixtures thereof; and(b) contacting the hydrocarbon feedstock with an acidic montmorillonite adsorbent at a temperature in the range from 10 to 60° C.2. The process according to claim 1 , wherein the aromatic compound is an aromatic hydrocarbon compound selected from benzene claim 1 , toluene claim 1 , xylene claim 1 , ethylbenzene claim 1 , their derivatives claim 1 , and mixtures thereof.3. The process according to claim 1 , wherein the alkene is C4 to C10 alkene.4. The process according to claim 1 , wherein the alkyne is C4 to C10 alkyne.5. The process according to claim 1 , wherein the nitrogen-containing compound is N-formyl morpholine.6. The process according to claim 1 , wherein contacting of the hydrocarbon feedstock with the acidic montmorillonite adsorbent is carried out at a gauge pressure in the range from 0 to 6×10Pascal.7. The process according to claim 1 , wherein the acidic montmorillonite adsorbent comprises a content of H per gram of adsorbent of at least 1 μmol.8. The process according to claim 7 , wherein the acidic montmorillonite adsorbent is obtainable by treating a montmorillonite with an acid.9. The process according to claim 8 , wherein the acid is selected from the group consisting of ammonium sulfate claim 8 , sulfuric acid ...

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12-01-2017 дата публикации

MATERIAL FOR RAPID GAS SORPTION IN LOUDSPEAKERS

Номер: US20170013350A1
Принадлежит:

An assemblage of substantially round particles with a mean diameter between 0.1 and 4 mm, more preferable between 0.3 to 2 mm and most preferable between 0.8 to 1.2 mm, wherein the density of the assemblage determined by ISO 697 is between 250 kg/m3 and 400 kg/m3 is disclosed. The substantially round particles comprise at least one microporous material and optionally at least one binder, wherein the assemblage comprises a pore volume, wherein the pore volume comprises pores resulting from void space between different ones of the substantially round particles and pores within the substantially round particles. 1. An assemblage of substantially round particles with a mean diameter between 0.1 and 4 mm , more preferable between 0.3 to 2 mm and most preferable between 0.8 to 1.2 mm , wherein the density of the assemblage determined by ISO 697 is between 250 kg/m3 and 400 kg/m3 and wherein the substantially round particles comprise at least one microporous material and optionally at least one binder , wherein the assemblage comprises a pore volume , wherein the pore volume comprises pores resulting from void space between different ones of the substantially round particles and pores within the substantially round particles.2. The assemblage of claim 1 , wherein the pores have different radii claim 1 , and wherein claim 1 , if the pore volume has pores larger than 0.002 μm and smaller 100 μm in diameter claim 1 , at least 25% is comprised by pores having radii between 0.4 and 90 μm claim 1 , more preferable between 1 and 40 μm and most preferable between 2 and 203. The assemblage of claim 1 , wherein the assemblage is substantially monodisperse.4. The assemblage of claim 1 , wherein at least one of the substantially round particles contains at least one inside cavity within the substantially round particle claim 1 , wherein the at least one cavity occupies at least 3% and not more than 50% of the substantially round particle by volume.5. The assemblage of wherein the ...

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10-01-2019 дата публикации

TREATMENT METHOD OF RADIOACTIVE WASTE WATER CONTAINING RADIOACTIVE CESIUM AND RADIOACTIVE STRONTIUM

Номер: US20190013107A1
Принадлежит:

The present invention provides a treatment method of radioactive waste water containing radioactive cesium and radioactive strontium, comprising passing the radioactive waste water containing radioactive cesium and radioactive strontium through an adsorption column packed with an adsorbent for cesium and strontium, to adsorb the radioactive cesium and radioactive strontium on the adsorbent, wherein the adsorbent for cesium and strontium comprises: at least one selected from crystalline silicotitanates represented by the general formulas: NaTiSiO.nHO, (NaK)TiSiO.mHO and KTiSiO.lHO wherein x represents a number of more than 0 and less than 1, and n, m and l each represents a number of 0 to 8; and at least one selected from titanate salts represented by the general formulas: NaTiO.qHO, (NaK)TiO.rHO and KTiO.tHO wherein y represents a number of more than 0 and less than 1, and q, r and t each represents a number of 0 to 10; wherein the adsorbent is a granular adsorbent having a grain size of 250 μm or more and 1200 μm or less, wherein the absorbent is packed to a height of 10 cm or more and 300 cm or less in the adsorption column, and wherein the radioactive waste water is passed through the adsorption column at a linear velocity (LV) of 1 m/h or more and 40 m/h or less and a space velocity (SV) of 200 hor less. 1. A treatment method of radioactive waste water containing radioactive cesium and radioactive strontium , comprising passing the radioactive waste water containing radioactive cesium , radioactive strontium , a Na ion , a Ca ion and a Mg ion through an adsorption column packed with an adsorbent for cesium and strontium , to adsorb the radioactive cesium and radioactive strontium on the adsorbent , [{'sub': 4', '4', '3', '16', '2', 'x', '(1-x)', '4', '4', '3', '16', '2', '4', '4', '3', '16', '2, 'at least one selected from crystalline silicotitanates represented by the general formulas: NaTiSiO.nHO, (NaK)TiSiO.mHO and KTiSiO.lHO wherein x represents a number of ...

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03-02-2022 дата публикации

COLORED ZEOLITE ADSORBENT

Номер: US20220032263A1
Автор: Serge Nicolas
Принадлежит: Arkema France

The present invention concerns a zeolitic adsorbent comprising a zeolitic agglomerate comprising at least one zeolite and at least one agglomeration binder, said agglomerate being coated with a coating comprising at least one pigment. 1. A zeolitic adsorbent material comprising:a zeolitic agglomerate comprising at least one zeolite and at least one agglomeration binder,the agglomerate being coated with a coating comprising at least one pigment.2. The material as claimed in claim 1 , having a color whose component L* is between 0 and 80.3. The material as claimed in claim 1 , wherein the coating has a thickness of between 10 μm and 1000 μm.4. The material as claimed in claim 1 , wherein the one zeolitic agglomerate comprises a zeolite selected from LTA-type zeolites and FAU-type zeolites.5. The material as claimed in claim 1 , wherein the amount of zeolite(s) is more than 65% relative to the total weight of the adsorbent material claim 1 , and is less than 99% by weight relative to the total weight of the material.6. The material as claimed in claim 1 , wherein the agglomeration binder is selected from clays and inorganic binders.7. The material as claimed in claim 1 , wherein the pigment is selected from peach black claim 1 , lamp black claim 1 , wine black claim 1 , vine black claim 1 , mineral black claim 1 , Dead Sea black clay claim 1 , and organic dyes from the lignosulfonate class.8. The material as claimed in claim 1 , wherein the amount of pigment is between 0.01% and 10% by weight relative to the total weight of the material.9. A process for preparing a zeolitic adsorbent material as claimed in claim 1 , comprising:a) mixing an agglomeration binder and at least one zeolite, and agglomerating and shaping the mixture to give a zeolitic agglomerate;b) coating the agglomerate prepared and shaped in step a) using a coating composition comprising at least one pigment;c) drying the coated agglomerate obtained in step b) at a temperature generally of between 80° C. ...

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19-01-2017 дата публикации

Composite absorbent particles

Номер: US20170013798A1
Принадлежит: Clorox Co

Composite particles and methods for making the same. An absorbent material is formed into a particle. An optional performance-enhancing active is coupled to the absorbent material before, during, or after the particle-forming process, homogeneously and/or in layers. Additionally, the composite absorbent particle may include a core material. Preferred methods for creating the absorbent particles include a pan agglomeration process, a high shear agglomeration process, a low shear agglomeration process, a high pressure agglomeration process, a low pressure agglomeration process, a rotary drum agglomeration process, a mix muller process, a roll press compaction process, a pin mixer process, a batch tumble blending mixer process, an extrusion process, and a fluid bed process.

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03-02-2022 дата публикации

ZEOLITE AND PREPARATION METHOD THEREFOR

Номер: US20220033269A1
Принадлежит:

Disclosed is a method of producing zeolite that includes obtaining a lithium residue including aluminosilicate from lithium ore including lithium oxide; washing the lithium residue to adjust the pH of the lithium residue; adjusting a molar ratio of silicon to aluminum (Si/Al) included in the lithium residue; preparing a hydrogel by adding an alkali material to the lithium residue; and preparing crystals by crystallizing the lithium residue in the form of a hydrogel. 1. A method of producing zeolite , comprisingobtaining a lithium residue including aluminosilicate from lithium ore including lithium oxide;washing the lithium residue to adjust the pH of the lithium residue;adjusting a molar ratio of silicon to aluminum (Si/Al) included in the lithium residue;preparing a hydrogel by adding an alkali material to the lithium residue; andpreparing crystals by crystallizing the lithium residue in the form of a hydrogel.2. The method of claim 1 , whereinthe obtaining of the lithium residue comprisesheat-treating the lithium ore;pulverizing the heat-treated lithium ore;precipitating lithium sulfate from the pulverized lithium ore; andleaching and separating the lithium sulfate into water.3. The method of claim 2 , whereinIn the heat-treating of the lithium ore,the lithium ore is heat-treated at a temperature of 900 to 1200° C.4. The method of claim 1 , whereinin the obtaining of the lithium residue,the lithium residue comprises{'sub': 2', '3', '2', '2', '3', '2', '2, '20 to 30 wt % of alumina (AlO), 60 to 70 wt % of silica (SiO), 10 wt % or less of at least one of iron oxide (FeO), calcium oxide (CaO), sodium oxide (NaO), and potassium oxide (KO) based on total 100 wt %.'}5. The method of claim 1 , whereinin the adjusting of the pH of the lithium residue,{'sub': '4', 'sup': '2−', 'the lithium residue is washed to remove the sulfate ion (SO) from the lithium residue.'}6. The method of claim 1 , whereinin the adjusting of the pH of the lithium residue,the pH of the lithium ...

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19-01-2017 дата публикации

SODIUM-CALCIUM-ALUMINOSILICATE COLUMN FOR ADSORBING CO2

Номер: US20170014799A1

A new adsorbent CO-ONE for removal of acidic gases such as carbon dioxide and hydrogen sulfide was developed from hydrothermal reaction of natural limestone with natural kaolin via sodium hydroxide. Several synthesis conditions were employed such as initial concentration of NaOH, weight ratio of limestone to kaolin, reaction temperature and pressure. The produced Ca—Na—SiO—AlOsamples were characterized using XRD and EDS and showed that a mixture of Gehlenite CaAl(ASiO)OHand Stilbite NaCa(AlSiO) with percentage of 43 and 57 was successfully produced, respectively. Another produced sample showed the presence of Gehlenite CaAl(AlSiO)OH, Stilbite NaCa(AlSiO) and Lawsonite CaAlSiOOH(HO) with percentage of 4.1 and 7.4 and 88, respectively. 19-. (canceled)10: A COadsorption column , comprising: [{'sub': '2', 'a COinlet,'}, 'a gas outlet, and', {'sub': '2', 'a fixed bed column disposed inside the column between the COinlet and the gas outlet,'}], 'an gas adsorption column having{'sub': 2', '2', '3, 'wherein the fixed bed column comprises a Ca—Na—SiO—AlO/Sodium-Calcium-Aluminosilicate composition comprising 3-6% gehlenite, 5-9% stilbite, and 86-92% lawsonite.'}11: The COadsorption column of claim 10 , wherein the Ca—Na—SiO—AlO/Sodium-Calcium-Aluminosilicate composition comprises 4-5% gehlenite claim 10 , 6-8% stilbite claim 10 , and 87-91% lawsonite.12: The COadsorption column composition of claim 10 , wherein the Ca—Na—SiO—AlO/Sodium-Calcium-Aluminosilicate composition comprises 4.1% gehlenite claim 10 , 7.4% stilbite claim 10 , and 88% lawsonite.1315-. (canceled)16: The COadsorption column of claim 10 , wherein the fixed bed column has an acidic gas adsorption capacity of 0.10 mol/g to 0.2 mol/g after a 1regeneration cycle.17: The COadsorption column of claim 10 , wherein the fixed bed column has an acidic gas adsorption capacity of 2.0 mol/g to 2.5 mol/g after a 5regeneration cycle. This application is a continuation of Ser. No. 14/167,460, allowed.Technical FieldThe ...

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19-01-2017 дата публикации

ISOTHERMAL CO2 ADSORPTION COLUMN

Номер: US20170014800A1

A new adsorbent CO-ONE for removal of acidic gases such as carbon dioxide and hydrogen sulfide was developed from hydrothermal reaction of natural limestone with natural kaolin via sodium hydroxide. Several synthesis conditions were employed such as initial concentration of NaOH, weight ratio of limestone to kaolin, reaction temperature and pressure. The produced Ca—Na-SiO2-Al2O3 samples were characterized using XRD and EDS and showed that a mixture of Gehlenite CaAl(AlSiO)OHand Stilbite NaCa(AlSiO) with percentage of 43 and 57 was successfully produced, respectively. Another produced sample showed the presence of Gehlenite CaAl(AlSiO)OH, Stilbite NaCa(AlSiO) and Lawsonite CaAlSiOOH(HO) with percentage of 4.1 and 7.4 and 88, respectively. 1. An isothermal COadsorption column , comprising: [{'sub': '2', 'a COinlet at a first end,'}, 'a gas outlet at a second end, and', 'a fixed bed column disposed inside the column,, 'an gas adsorption column having{'sub': 2', '2', '3, 'wherein the fixed bed column comprises a Ca—Na—SiO—AlO/Sodium-Calcium-Aluminosilicate composition comprising40-45% gehlenite and 55-60% stilbite.2. The isothermal COadsorption column of claim 1 , wherein the fixed bed column further comprises one or more acidic gases adsorbed on the Ca—Na—SiO—AlO/Sodium-Calcium-Aluminosilicate composition.3. The isothermal COadsorption column of claim 1 , wherein the Ca—Na—SiO—AlO/Sodium-Calcium-Aluminosilicate composition comprises 42-44% gehlenite and 56-58% stilbite.4. The isothermal COadsorption column of claim 1 , wherein the Ca—Na—SiO—AlO/Sodium-Calcium-Aluminosilicate composition comprises 43% gehlenite and 57% stilbite.57-. (canceled)8. The isothermal COadsorption column of claim 1 , having an acidic gas adsorption capacity of 0.10 mol/g-0.2 mol/g after a 1regeneration cycle.9. The isothermal COadsorption column of claim 1 , having an acidic gas adsorption capacity of 2.0 mol/g-2.5 mol/g after a 5regeneration cycle.1017-. (canceled) This application is a ...

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19-01-2017 дата публикации

Method Of Remediation Of Organic Toxins Using Supported Lipid Bilayer Nanoparticles

Номер: US20170014878A1

The present invention relates to methods and compositions for water treatment and environmental remediation using nanoparticle supported lipid bilayers (NP-SLBs). In one embodiment, the NP-SLBs are single or multilayer lipid bilayers of 1,2-dimyristoyl-sn-glycero-3-phosphocholine (DMPC) supported by silica.

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18-01-2018 дата публикации

High-purity composite materials, methods of making high-purity composite materials, and methods of using high-purity composite materials

Номер: US20180016190A1
Автор: BO Wang
Принадлежит: Imerys Filtration Minerals Inc

A composite filter aid may include acid-washed diatomaceous earth and a low extractable metal mineral. A method for making a composite material may include blending an acid-washed diatomaceous earth and a low extractable metal mineral, adding a binder to the blended diatomaceous earth and low extractable metal mineral, and forming the composite material from the acid-washed diatomaceous earth, the low extractable metal mineral, and the binder. A method for filtering a liquid may include providing a liquid for filtering and filtering the liquid through a composite filter aid that includes an acid-washed diatomaceous earth and a low extractable metal mineral.

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21-01-2021 дата публикации

COMPOSITION FOR PURIFICATION OF BIOFLUIDS

Номер: US20210015844A1
Автор: Jiang Chen, SUN TAO
Принадлежит:

Disclosed is a composition for the purification of biofluids, for example, for hemodialysis and peritoneal dialysis, comprising an osmotic agent and a toxin-removal reagent, wherein the toxin-removal reagent can remove a toxin from a biofluid under a condition for osmosis. Provided are a dialysis solution and a kit comprising the aforementioned composition, a method for removing a toxin from a biofluid using the aforementioned composition, and a method for treating a toxin-related disease. 1. A composition comprising an osmotic agent and a toxin-removal reagent , wherein the osmotic agent provides an osmotic pressure substantially equal to or higher than that of a biofluid , and the toxin-removal reagent reduces a toxin in the biofluid under a condition for osmosis.2. The composition according to claim 1 , wherein the toxin-removal reagent reduces free amount claim 1 , non-free amount claim 1 , and/or total amount of the toxin in the biofluid.3. (canceled)4. (canceled)5. The composition according to claim 1 , wherein the toxin-removal reagent has one or more characteristics selected from the group consisting of: 1) having a porous structure; 2) capable of forming a charged structure; 3) capable of binding to the toxin through a non-covalent bond or a covalent bond or an ionic bond; and 4) capable of degrading the toxin.6. The composition according to claim 5 , wherein the toxin-removal reagent has a porous structure claim 5 , and the porous structure has one or more of the following characteristics:{'sup': 2', '2, '1) having a specific surface area of 70 cm/g−1000 m/g;'}2) having a pore size in a range of 0.1 nm-10 μm;3) having a pore size distribution of 0.1 nm-100 μm;4) having a porosity of about 5-95%; and5) capable of adsorbing the toxin at an adsorption rate of at least 0.2 mg/g.7. The composition according to claim 6 , wherein the toxin-removal reagent having a porous structure is selected from the group consisting of a silicon-based porous material claim 6 , ...

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17-01-2019 дата публикации

Road surface covering system

Номер: US20190016637A1
Автор: Russell Matthew F.
Принадлежит: RJSK, LLC

A road surface covering system includes a road surface covering of concrete or asphalt, water permeable tiles disposed adjacent to an outer edge of the road surface covering and having a water conductivity of at least 7 inches of water per hour, and a subgrade bed of fill material including a porous sand. The porous sand includes at least 70% of a naturally occurring micaceous arkose rock material having at least 30 wt % of mica, and at least 50 vol % of the micaceous arkose rock material having a mean diameter of between 0.060 mm and 0.65 mm. The micaceous arkose rock material being previously kilned at a temperature of between 1100° C. and 1300° C. 1. A road surface covering system , comprising:a road surface covering comprising at least one of concrete or asphalt, the road surface covering being define by a first outer edge;a plurality of water permeable tiles disposed adjacent to the first outer edge of the road surface covering, the water permeable tiles having a water conductivity, based on a constant water column of 30 inches, of at least 7 inches of water per hour; anda subgrade bed of fill material disposed beneath the plurality of water permeable tiles and at least a portion of the road surface covering, the subgrade bed of fill material comprising a porous sand, the porous sand comprising at least 70% by weight of a naturally occurring micaceous arkose rock material, the micaceous arkose rock material comprising at least 30% by weight of mica, at least about 50% by volume of the micaceous arkose rock material having a mean diameter of between about 0.060 mm and about 0.65 mm, and the micaceous arkose rock material having been previously kilned at of temperature of between 1100° C. and 1300° C. to transform at least 30% by weight of micaceous components in the micaceous arkose rock material into feldspar containing metal sulfides.2. The road surface covering system of and wherein the plurality of water permeable tiles are each defined by an upper surface ...

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21-01-2021 дата публикации

CHARACTERISTICS OF TUNABLE ADSORBENTS FOR RATE SELECTIVE SEPARATION OF NITROGEN FROM METHANE

Номер: US20210016218A1
Принадлежит:

The present invention generally relates to a process that utilizes tunable zeolite adsorbents in order to reduce the bed size for nitrogen removal from a methane (or a larger molecule) containing stream. The adsorbents are characterized by the rate of adsorption of nitrogen and methane and the result is a bed size that is up to an order of magnitude smaller with these characteristics (in which the rate selectivity is generally 30) than the corresponding bed size for the original tunable zeolite adsorbent that has a rate selectivity of >100x. 1. A pressure swing adsorption process for kinetic separation of Nfrom a feed stream comprising at least methane and N , said process comprising feeding the feed stream to an adsorbent bed comprising adsorbent having:{'sub': '2', 'a rate of adsorption of at least 0.036 mmol/g/min for Nas determined by the Hiden method and'}{'sup': th', 'th, 'sub': '2', "a rate of adsorption of methane that is ⅙to 1/10000the adsorbent's adsorption rate for Nas determined by the Hiden method"}{'sub': '2', 'and recovering a product stream containing said at least methane gas with a reduced level of N.'}2. The process of wherein the adsorbent has an adsorption rate of at least 0.143 mmol/g/min for Nimpurity as determined by the Hiden method and an adsorption rate for methane that is 1/10to 1/1000of the adsorption rate for Nas determined by the Hiden method.3. The process of wherein said adsorbent comprises zeolite A claim 1 , X claim 1 , Y claim 1 , chabazite claim 1 , mordenite claim 1 , faujasite claim 1 , clinoptilolite claim 1 , ZSM-5 claim 1 , L claim 1 , Beta claim 1 , or combinations thereof.4. The process of wherein said adsorbent is a zeolite exchanged with at least one cation selected from Li claim 3 , Na claim 3 , K claim 3 , Mg claim 3 , Ca claim 3 , Sr claim 3 , Ba claim 3 , Cu claim 3 , Ag claim 3 , Zn claim 3 , NH4+ and combinations or mixtures thereof5. The process of wherein said adsorbent is zeolite A.6. The process according to ...

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16-01-2020 дата публикации

PASSIVE NOx ADSORBER

Номер: US20200016571A1
Принадлежит:

A passive NOadsorber is disclosed. The passive NOadsorber is effective to adsorb NOat or below a low temperature and release the adsorbed NOat temperatures above the low temperature. The passive NOadsorber comprises a noble metal and a molecular sieve having an LTL Framework Type. The invention also includes an exhaust system comprising the passive NOadsorber, and a method for treating exhaust gas from an internal combustion engine utilizing the passive NOadsorber. 1. An exhaust system for internal combustion engines comprising a passive NOadsorber and at least one additional after-treatment device(s) selected from the group consisting a selective catalytic reduction (SCR) catalyst , a particulate filter , a SCR filter , a NOadsorber catalyst , a three-way catalyst , an oxidation catalyst , and combinations thereof:{'sub': x', 'x, 'wherein the passive NOadsorber is located close to the engine and the additional after-treatment device(s) are located downstream of the passive NOadsorber; and'}{'sub': x', 'x', 'x', 'x, 'wherein the passive NOadsorber is effective to adsorb NOat or below a low temperature and release the adsorbed NOat temperatures above the low temperature, said passive NOadsorber comprising a first noble metal and a molecular sieve having an LTL Framework Type.'}2. The exhaust system of wherein the first noble metal is selected from the group consisting of platinum claim 1 , palladium claim 1 , rhodium claim 1 , gold claim 1 , silver claim 1 , iridium claim 1 , ruthenium claim 1 , osmium claim 1 , and mixtures thereof.3. The exhaust system of wherein the first noble metal is palladium.4. The exhaust system of wherein the molecular sieve having an LTL Framework Type is selected from the group consisting of aluminosilicate zeolite claim 1 , an aluminophosphate zeolite claim 1 , a silicoaluminophosphate (SAPO) zeolite claim 1 , and a metal-substituted aluminosilicate or aluminophosphate zeolite.5. The exhaust system of wherein the molecular sieve having ...

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17-04-2014 дата публикации

Lithium Extraction Composition and Method of Preparation Thereof

Номер: US20140102946A1
Принадлежит: Simbol Inc.

This invention relates to a particulate extraction material for the extraction of lithium from a geothermal brine or lithium containing solution. The particulate material includes an inorganic or polymer based substrate that includes a lithium aluminum intercalate layer applied to the exterior of the substrate, wherein the lithium aluminum intercalate layer is operable to capture lithium ions from solution. 1. A composition for the recovery of lithium from a lithium containing solution comprising:a substrate having a lithium aluminum intercalate coating applied to the surface thereof, wherein the coating is applied by contacting a polyaluminum hydroxyl halide solution and the substrate in the presence of alkali metal hydroxide, thereby precipitating the lithium aluminum intercalate onto the substrate surface.2. The composition of wherein the substrate is selected from the group consisting of an inorganic material or a polymeric material claim 1 ,3. The composition of wherein the substrate is porous.4. The composition of wherein the substrate has an average particle size of less than about 500 μm and an average pore size of less than about 5 μm.5. The composition of wherein the ratio of alumina to lithium is between about 1:0.1 and 1:0.6.6. The composition of wherein the substrate is diatomaceous earth.7. A method for preparing a composition for the recovery of lithium from a lithium containing solution claim 1 , wherein the method comprises the steps of:providing a particle substrate;contacting the substrate with poly aluminum hydroxyl halide to form an alumina coated particle substrate; andintercalating a lithium salt into the alumina coating on the particle substrate to form a lithium aluminum intercalate.8. The method of claim 7 , wherein the particle substrate is selected from the group consisting of inorganic and polymeric material claim 7 ,9. The method of claim 7 , wherein the particle substrate is porous.10. The method of claim 7 , wherein the particle ...

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26-01-2017 дата публикации

FILTER AND METHOD FOR PRODUCING SAME

Номер: US20170021296A1
Принадлежит:

A filter for binding constituents of a gas stream includes a supporting member and a filter layer applied to surfaces of the supporting member. The filter layer includes a component for the physisorption of constituents, a component for the chemisorption of constituents, and a component for dissolving oil constituents which comprises ionic liquids. 1. A filter for binding constituents of a gas stream , the filter comprising:a supporting member; anda filter layer applied to the surfaces of the supporting member, a) a component for the physisorption of constituents,', 'b) a component for the chemisorption of constituents, and', 'c) a component for dissolving oil constituents which comprises ionic liquids., 'wherein the filter layer includes2. The filter as claimed in claim 1 , wherein the supporting member is at least one of a ceramic supporting member or a metal supporting member.3. The filter as claimed in claim 1 , wherein the supporting member has a cell density of from 50 to 1600 cpsi.4. The filter as claimed in claim 1 , wherein claim 1 , under application conditions claim 1 , the filter has a pressure drop of 10 mbar or less.5. The filter as claimed in claim 1 , wherein the component for the physisorption includes at least one of activated carbon claim 1 , bentonite claim 1 , siliceous earths claim 1 , or zeolites.6. The filter as claimed in claim 1 , wherein the component for the chemisorption comprises at least one of peptides or proteins.7. The filter as claimed in claim 1 , wherein the component for the chemisorption comprises keratin-containing fibers.8. The filter as claimed in claim 1 , wherein the ionic liquids comprise cations selected from the group consisting of: optionally alkylated imidazolium claim 1 , pyridinium claim 1 , pyrrolidinium claim 1 , guanidinium claim 1 , uronium claim 1 , thiouronium claim 1 , piperidinium claim 1 , morpholinium claim 1 , ammonium and phosphonium ions and anions selected from the group consisting of ...

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10-02-2022 дата публикации

MATERIAL TO SEPARATE AND PUMP OXYGEN

Номер: US20220040666A1

A material for separating and pumping oxygen is disclosed. The material is a zeolite doped with a chemical element having an electron density of between 30 kJ/mol and 150 kJ/mol. The material is configured for controllable oxygen desorption between 150° C. and 300° C. and pumping the released oxygen into an area having an ambient pressure of less than 100 pascals. 1. A material for separating and pumping oxygen , the material comprising a zeolite doped/substituted with a chemical element having an electron density to donate after substitution providing an exothermic Oadsorption energy between 30 kJ/mol and 390 kJ/mol.2. The material of claim 1 , wherein the chemical element is a metal.3. The material of wherein the metal is tungsten.4. The material of wherein the metal is zirconium.5. The material of claim 2 , wherein the metal is tin.6. The material of claim 2 , wherein the metal is chromium.7. The material of claim 2 , wherein the metal is cerium.8. The material of claim 2 , wherein the metal is praseodymium.9. The material of claim 2 , wherein the metal is manganese.10. The material of claim 2 , wherein the metal is titanium.11. The material of claim 2 , wherein the metal is molybdenum.12. The material of claim 2 , wherein the metal is hafnium.13. The material of claim 2 , wherein the metal is palladium.14. The material of claim 2 , wherein the metal is platinum.15. The material of claim 1 , wherein the chemical element has an adsorption energy of between 40 kJ/mol and 60 kJ/mol.16. The material of claim 1 , wherein the chemical element has an adsorption energy of between 40 kJ/mol and 50 kJ/mol.17. The material of claim 1 , wherein the chemical element has an adsorption energy of between 80 kJ/mol and 120 kJ/mol.18. The material of claim 1 , wherein the chemical element is a metalloid.19. The material of claim 18 , wherein the metalloid is gallium.20. The material of claim 18 , wherein the metalloid is silicon.21. The material of claim 1 , wherein pores within ...

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25-01-2018 дата публикации

High Purity Ethylenediamine for Semiconductor Applications

Номер: US20180022691A1
Принадлежит: Versum Materials US, LLC

Ethylenediamine (EDA) compositions and methods for making the EDA that is suitable for use in thin-film semiconductor processing applications, are disclosed. The EDA is purified to remove water and trace metals. Water levels below about 50 ppm by weight are achieved by passing liquid through 3A type molecular sieve in a packed bed. Metallic impurities are removed by distillation and the resulting product is packaged in specially dried and optionally pre-conditioned containers. 1. Ethylenediamine wherein the ethylenediamine is greater than about 99.9 weight percent pure and contains less about 50 ppm water and less than about 100 ppb trace metals.2. The ethylenediamine of wherein the ethylenediamine contains less than about 50 ppb of aluminum claim 1 , chromium claim 1 , copper claim 1 , iron claim 1 , magnesium claim 1 , manganese claim 1 , molybdenum claim 1 , nickel claim 1 , titanium and zinc.3. The ethylenediamine of wherein the ethylenediamine contains less than about 10 ppm of water.4. The ethylenediamine of wherein the ethylenediamine contains less than about 5 ppm of water.5. The ethylenediamine of wherein the ethylenediamine contains less than about 1 ppm of water.6. The ethylenediamine of wherein the ethylenediamine contains less than about 5 ppm of halides.7. The ethylenediamine of wherein the halide is chlorine.8. The ethylenediamine of wherein the ethylenediamine contains less than about 5 ppb of alkali metals.9. The ethylenediamine of wherein the alkali metal is sodium.10. A composition comprising the ethylenediamine of .11. A method for treating ethylenediamine comprising contacting ethylenediamine with a molecular sieve comprising type 3A zeolite under conditions sufficient to reduce the amount of water in the ethylenediamine to less than about 50 ppm; and claim 1 , distilling the ethylenediamine under conditions sufficient to reduce the amount of trace metals to less than about 100 ppb.12. The method of wherein the ethylenediamine is greater than ...

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23-01-2020 дата публикации

Adsorbent for contaminant removal from c4 hydrocarbons

Номер: US20200023341A1
Принадлежит: UOP LLC

A process is provided for removing contaminants from olefin containing C 4 streams. The streams are contacted with an X based zeolite adsorbent comprising greater than 88% X zeolite at a SiO 2 /Al 2 O 3 ratio of less than 2.5 and an alkali metal salt present in excess of an amount required to achieve full exchange of cation sites on the X based zeolite. The resulting alkali oxide on a volatile free basis is less than 1% (by mass) of the X based adsorbent. The contaminants that are removed include sulfur, oxygenate, and nitrogen based contaminants.

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24-01-2019 дата публикации

Use of Fly Ash in Biological Process of Wastewater Treatment Systems

Номер: US20190024309A1
Принадлежит:

The spent liquor (SL) of a thermomechanical pulping (TMP) process introduces a high load to the wastewater system of this process. To reduce this load, fly ash from a biomass boiler is used and the application of fly ash improves the performance of biological process. Three different alternatives are introduced to apply fly ash to treat spent liquor. 1. A method of treating spent liquor from a pulping process of a pulp mill , said method comprising obtaining wastewater from the pulping process that contains both fly ash and said spent liquor , and subjecting said wastewater to biological wastewater treatment while said fly ash and said spent liquor are both present within said wastewater.2. The method of comprising adding said fly ash to the spent liquor at a wastewater pretreatment stage upstream from the biological wastewater treatment to create pre-treated wastewater containing both said spent liquor and said fly ash claim 1 , and directing said pre-treated wastewater to the biological wastewater treatment stage without separating said fly ash from the pre-treated wastewater.3. The method of comprising claim 1 , prior to adding the fly ash to the spent liquor claim 1 , making leachate by mixing said fly ash with water claim 1 , thereby leaching metals from said fly ash before adding said fly ash to the spent liquor.4. The method of comprising adding the fly ash from which the metals have been leached to the spent liquor for use as an adsorbent in the biological wastewater treatment stage.5. The method of comprising adding the fly ash to the spent liquor at the biological wastewater treatment stage.6. The method of comprising administering the leachate to the spent liquor as a coagulant at a coagulation stage upstream of the biological wastewater treatment stage.7. The method of comprising separating coagulates from the spent liquor at a separation stage between the coagulation stage and the biological wastewater treatment stage.8. The method of comprising using ...

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23-01-2020 дата публикации

WASTEWATER FILTRATION METHOD AND SYSTEM

Номер: US20200024163A1
Автор: Jasti Shravya
Принадлежит:

The invention is a method of and system for removing bacteria and other contaminants in water by utilizing bentonite clay impregnated with metal ion, such as silver or copper ion. The method and system may alternatively or additionally include a cation exchange resin impregnated with metal ion, such as silver or copper ion. 1. A system for removing contaminants in water comprising substrates of bentonite clay impregnated with metal ion.2. The system of wherein the bentonite is impregnated with silver.3. The system of wherein the bentonite is impregnated with copper.4. The system of wherein the bentonite is impregnated with silver and copper.5. The system of comprising a cation exchange resin impregnated with metal ion.6. The system of comprising a cation exchange resin impregnated with metal ion.7. The system of comprising a cation exchange resin impregnated with metal ion.8. The system of comprising a cation exchange resin impregnated with metal ion.9. The system of wherein the resin is impregnated with silver.10. The system of wherein the resin is impregnated with silver.11. The system of wherein the resin is impregnated with silver.12. The system of wherein the resin is impregnated with silver.13. The system of wherein the resin is impregnated with copper.14. The system of wherein the resin is impregnated with copper.15. The system of wherein the resin is impregnated with copper.16. The system of wherein the resin is impregnated with copper.17. The system of wherein the resin is impregnated with silver and copper.18. The system of wherein the resin is impregnated with silver and copper.19. The system of wherein the resin is impregnated with silver and copper.20. The system of wherein the resin is impregnated with silver and copper. This application claims priority to and the benefit of U.S. Provisional Application No. 62/702,333 filed Jul. 23, 2018, which is hereby incorporated by reference in its entirety.None.The present invention relates to a wastewater ...

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04-02-2016 дата публикации

Supported Sulfides for Mercury Capture

Номер: US20160030915A1
Принадлежит: Novinda Corporation

Herein are described methods and materials for capturing mercury from, for example, the gases produced by the combustion of coal. The composition for the removal of mercury from the fluid includes a polysulfide selected from the group consisting of a calcium sulfide and a bromosulfide; the polysulfide supported by or carried on a surface of a silicate particulate. Disclosed methods include a process for manufacturing the bromosulfide or calcium-sulfide mercury-removal composition and a process of capturing mercury from a fluid, the process can include admixing a bromosulfide or calcium-sulfide mercury-removal composition and a fluid that includes mercury; wherein the bromosulfide mercury removal composition includes a bromosulfide supported by or carried on a surface of a silicate particulate; wherein the calcium-sulfide mercury-removal composition includes a calcium sulfide supported by or carried on a surface of a silicate particulate. 1. A composition for the removal of mercury from a fluid , the composition comprising:a polysulfide that is a calcium sulfide;supported by or carried on a surface of a silicate particulate;{'sub': '2', 'wherein the calcium sulfide is the reaction product of Ca(OH)and elemental sulfur.'}2. The composition of claim 1 , wherein the composition includes a weight percentage of the silicate particulate and a weight percentage of the polysulfide; and wherein the composition includes less than 25 wt. % claim 1 , of the polysulfide.3. (canceled)4. A method for manufacturing a calcium-sulfide mercury-removal composition comprising a two-step process selected from the group consisting of:{'sub': 2', '2, 'admixing Ca(OH)with a silicate support and then admixing elemental sulfur with the Ca(OH)-silicate admixture; and'}{'sub': '2', 'admixing Ca(OH)and elemental sulfur to produce a calcium sulfide and then admixing the calcium sulfide with a silicate support.'}5. A process of capturing mercury from a fluid claim 1 , the process comprising: ...

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04-02-2016 дата публикации

Method of scavenging hydrogen sulfide and mercaptans using well treatment composites

Номер: US20160030916A1
Принадлежит: Baker Hughes Inc

Hydrogen sulfide and mercaptans may be removed from a fluid or gaseous stream by introducing a composite to the fluid or gaseous stream containing a hydrogen sulfide scavenger adsorbed onto a water-insoluble adsorbent.

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01-02-2018 дата публикации

Materials, methods, and devices for siloxane contaminant removal

Номер: US20180028960A1
Принадлежит: Donaldson Co Inc

Adsorbent materials are disclosed, along with filter elements containing the adsorbent materials methods of using adsorbents to remove slioxane contaminants from a gas stream. The method includes providing an adsorbent material that has been washed with an acid and passing a gas through the adsorbent material so as to reduce siloxane levels in the gas. A filter element for reducing siloxane levels in a gas includes a first adsorbent material, the first adsorbent material comprising an acid-washed adsorbent; and a second adsorbent material, the second adsorbent material comprising an acid-impregnated adsorbent.

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17-02-2022 дата публикации

Scalable preparation of oxygen carriers for chemical looping

Номер: US20220048007A1
Автор: Kyle O&#39;Malley
Принадлежит: Kyle O&#39;Malley

Oxygen carriers for chemical looping and scalable methods of preparation thereof. Wet impregnation of active metal precursors into porous substrates, together with selective adsorption of the precursors on the pore surfaces, enables transition metal oxides derived from the precursors to disperse throughout the substrate, even at the nanoscale, without increased sintering or agglomeration. The porous substrate can be an oxide, for example SiO 2 . The oxygen carriers can comprise relatively large oxide loadings of over about 20 wt % and exhibit high reactivity over many regeneration cycles with substantially no loss in oxygen transport capacity or decrease in kinetics. The use of multiple transition metals, for example NiO in addition to CuO, can greatly enhance chemical looping performance.

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17-02-2022 дата публикации

MINERAL COMPOSITION

Номер: US20220048008A1
Принадлежит:

Compositions suitable for the purification of liquids, methods for making said compositions, and the uses of said compositions. 1. A composition comprising:a smectite, palygorskite, or sepiolite mineral;a second mineral; andsynthetic amorphous silica;wherein the synthetic amorphous silica is dispersed on the surface of at least one of the smectite, palygorskite, or sepiolite mineral and the second mineral.2. The composition of claim 1 , wherein the synthetic amorphous silica is dispersed on the surface of both the smectite claim 1 , palygorskite claim 1 , or sepiolite mineral and the second mineral.3. The composition of claim 1 , wherein the synthetic amorphous silica is silica gel.4. The composition of claim 1 , wherein the smectite claim 1 , palygorskite claim 1 , or sepiolite mineral is a smectite mineral.5. The composition of claim 1 , wherein the second mineral is selected from the group consisting of diatomite claim 1 , perlite claim 1 , moler claim 1 , kaolin claim 1 , talc claim 1 , or any combination of one or more thereof.6. The composition of claim 1 , wherein the smectite mineral and the second mineral are moler.7. The composition of claim 1 , wherein:at least about 60 wt % of particles in the composition are equal to or smaller than 75 μm; and/or{'sub': '50', '#text': 'the composition has a dranging from about 10 μm to about 60 μm; and/or'}{'sub': '90', '#text': 'the composition has a dranging from about 40 μm to about 150 μm; and/or'}{'sub': '10', '#text': 'the composition has a dranging from about 1 μm to about 10 μm.'}8. The composition of claim 1 , wherein the composition comprises:from about 60 wt % to about 98 wt % of the smectite, palygorskite, or sepiolite mineral; and/orfrom about 1 wt % to about 35 wt % of the second mineral; and/orfrom about 1 wt % to about 15 wt % of the synthetic amorphous silica.9. The composition of claim 1 , wherein the ratio of the smectite claim 1 , palygorskite claim 1 , or sepiolite mineral to the second mineral in ...

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17-02-2022 дата публикации

HIGHLY EFFECTIVE FUNCTIONAL ADDITIVE PRODUCTS

Номер: US20220048009A1
Принадлежит: EP MINERALS, LLC

This invention concerns highly effective functional additive products that comprise diatomite. More particularly, it concerns such functional additive products possessing particle size distributions which make them more effective as functional additives in filled systems. Higher effectiveness is demonstrated through lower Standard Sheen and/or reduced unit consumption relative to diatomite functional additives already in the public domain. Such products may also possess high brightness, low tint and/or an absence of detectable crystalline silica. 1. A product comprising diatomite , wherein the product is powdered and has(a) Standard Sheen of 0.4 to 0.5 and Hegman of 1.0 to 2.0, or (b) Standard Sheen of 0.6 to 0.7 and Hegman of 2.5 to 3.5.2. The product of claim 1 , wherein the Standard Sheen is 0.4 to 0.5 and the Hegman is 1.0 to 2.0 claim 1 , wherein the product further has a Ratio (R) of 0.35 to 0.52.3. The product of claim 1 , wherein the Standard Sheen is 0.6 to 0.7 and the Hegman is 2.5 to 3.5 claim 1 , wherein the product further has a Ratio (R) of 0.34 to 0.45.4. The product of claim 1 , wherein the product further has a Y value of 79 to 91 claim 1 , and an L* value of 91 to 97.5. The product of claim 1 , wherein the product further has an a* value of −0.1 to 1.2.6. The product of claim 1 , wherein the product further has a b* value of 1.0 to 5.0.7. The product of claim 1 , wherein the product further has a Standard Contrast Ratio of 0.90 to 0.92.8. The product of claim 1 , wherein the product is free of a total crystalline silica content as measured according to an LH Method.9. The product of claim 2 , wherein the product is free of a total crystalline silica content as measured according to an LH Method.10. The product of claim 3 , wherein the product is free of a total crystalline silica content as measured according to an LH Method.11. The product of claim 1 , wherein the product is free of a cristobalite content as measured according to an LH method.12. ...

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01-05-2014 дата публикации

Sorbent article for co2 capture

Номер: US20140116250A1
Принадлежит: Corning Inc

A sorbent article having a substrate having porous channel walls defining open channels, and an organic-inorganic hybrid sorbent material distributed on a surface of the porous channel walls, wherein the sorbent material is derived from an amino-functionalized alkoxysilane and a polyamine, wherein the sorbent material is present in an amount equal to or greater than 10 g/l, wherein at least some of the sorbent material resides in the porous channel walls and forms CO 2 adsorption sites within the interior of the porous channel walls. The article may be useful, for example, for removing CO 2 from a gas.

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30-01-2020 дата публикации

Fuel filter with organoclay, cleaning cartridge with organoclay, and use

Номер: US20200030727A1
Принадлежит: Mann and Hummel GmbH

A fuel filter has a separating device separating, from a medium flow comprising a first medium and a second medium, the first medium as a separated first medium contaminated with the second medium. The fuel filter has a cleaning device receiving a proportion of the second medium contained in the separated first medium. The cleaning device is arranged upstream of a discharge opening for discharging the first medium from the fuel filter. The cleaning device is provided with an absorbent/adsorbent cleaning material. The cleaning material contains or is made of an organoclay as an active component. The organoclay is a bulk material, wherein at least 50 wt. % of the organoclay has an average particle diameter of greater than 50 Φm and smaller than 1,000 Φm.

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30-01-2020 дата публикации

SELECTIVELY FUNCTIONALIZED POROUS MATERIAL

Номер: US20200030784A1
Принадлежит:

A porous substrate susceptible to one or both of hydroxylation and alkoxylation by a first protic solvent is exposed to a first relative pressure of the first protic solvent. The porous substrate includes a first plurality of pores having a first average pore diameter and a second plurality of pores having a second average pore diameter that is greater than the first average pore diameter. The first relative pressure is effective to one or both of hydroxylate or alkoxylate substantially only pores of the first average pore diameter to form a first modified porous substrate. The first modified porous substrate is reacted with a first functionalizing reagent that is effective to functionalize one or both of hydroxylated or alkoxylated surfaces, thereby functionalizing substantially only the first plurality of the pores, to form a first functionalized porous substrate. 1. A method , comprising:exposing a porous substrate susceptible to one or both of hydroxylation and alkoxylation by a first protic solvent to a first relative pressure of the first protic solvent, wherein the porous substrate comprises a first plurality of pores having a first average pore diameter and a second plurality of pores having a second average pore diameter that is greater than the first average pore diameter, wherein the first relative pressure is effective to one or both of hydroxylate or alkoxylate substantially only pores of the first average pore diameter to form a first modified porous substrate; andreacting the first modified porous substrate with a first functionalizing reagent that is effective to functionalize one or both of hydroxylated or alkoxylated surfaces, thereby functionalizing substantially only the first plurality of the pores, to form a first functionalized porous substrate, wherein in the first functionalized substrate, the second plurality of pores is substantially free of the first predetermined functional group and the first plurality of pores is functionalized with ...

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01-05-2014 дата публикации

Oxygen absorber

Номер: US20140117280A1
Принадлежит: Mitsubishi Gas Chemical Co Inc

An oxygen absorber is provided that contains at least one of compounds each having a particular structure, and the oxygen absorber exhibits an oxygen absorbing capability without a metal contained, and is suitable for removing oxygen inside a packaging material packaging foods or the like.

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04-02-2021 дата публикации

ADSORBER

Номер: US20210031168A1
Принадлежит:

An adsorbent bed, including at least one elementary composite structure that includes adsorbent particles in a polymer matrix, wherein the adsorbent bed has a bed packing, ρ, defined as a volume occupied by the at least one elementary composite structure Vdivided by a volume of the adsorbent bed Vwhere ρis greater than 0.60. 1. An adsorber , comprising an adsorbent bed structure containing an adsorbent bed of at least one elementary composite structure that comprises adsorbent particles in a polymer matrix , wherein the adsorber is adapted and configured to separate gas through adsorption and the adsorbent bed has a bed packing , ρ , defined as a volume occupied by the at least one elementary composite structure , V , divided by a volume of the adsorbent bed structure V , where ρis greater than 0.60.2. The adsorber of claim 1 , wherein the at least one elementary composite polymer/adsorbent structure comprises a plurality of elementary composite polymer/adsorbent structures configured as beads or extrudates having an average major dimension Dand an average minor dimension D claim 1 , wherein a ratio of Dmaj:Dis in the range of 1:1 to less than 20:1.3. The adsorber of claim 2 , wherein the adsorbent bed is configured as a radial adsorbent bed claim 2 , the adsorber further comprising a cylindrical pressure vessel having an inlet and an outlet claim 2 , a first annular porous grid concentrically disposed within the cylindrical pressure vessel claim 2 , a second annular porous grid concentrically disposed within the first annular porous grid wherein a first annulus is formed between an inner surface of the cylindrical pressure vessel and an outer surface of the annular porous grid and a second annulus is formed between an inner surface of the first annular porous grid and an outer surface of the second annular porous grid claim 2 , a gas-tight annular floor sealing a bottom of the second annulus in gas-tight fashion claim 2 , and a gas-tight annular ceiling sealing a ...

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11-02-2016 дата публикации

COMPOSITIONS AND METHODS FOR REDUCING ATMOSPHERIC OZONE LEVELS

Номер: US20160038931A1
Автор: Duke Christopher
Принадлежит:

Disclosed herein are ozone reactive polymers comprising a structural repeat unit represented by the following formula XLI: 28-. (canceled)9. A method of decomposing ozone comprising contacting ozone with the ozone decomposing composition of .1016-. (canceled)18. The polymer of claim 17 , wherein said structural repeat unit comprises at least 50% by weight of said polymer.1920-. (canceled)23. (canceled)24. The polymer of claim 17 , wherein a primary by-product upon reaction with ozone is a non-volatile compound.25. The polymer of claim 24 , wherein the non-volatile compound is a sugar.26. The polymer of claim 17 , wherein a primary by-product upon reaction with ozone is a compound that emits a scent.27. The polymer of claim 26 , wherein the primary by-product is vanillin.28. A method of decomposing ozone comprising contacting ozone with the ozone decomposing composition of .2931-. (canceled)34. The method of claim 28 , wherein said polymer has a weight average molecular weight of 9 claim 28 ,000 to 30 claim 28 ,000 Daltons.35. The method of claim 28 , wherein a primary by-product upon reaction with ozone is a non-volatile compound.36. The method of claim 35 , wherein said non-volatile compound is a sugar.37. The method of claim 28 , wherein a primary by-product upon reaction with ozone is a compound that emits a scent.38. The method of claim 37 , wherein the primary by-product is vanilla.39. A coating comprising a solvent and the ozone reactive polymer of .40. The coating of claim 39 , wherein said coating is a spray coating. The present application claims priority to the U.S. Provisional Application Ser. No. 62/034,864 filed on Aug. 8, 2014, entitled “COMPOSITIONS AND METHODS FOR REDUCING ATMOSPHERIC OZONE LEVELS,” the entire disclosure of which is incorporated herein by reference, including all the drawings.The present disclosure is in the field of compositions and methods for controlling air pollution; and more particularly, the invention relates to compositions ...

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08-02-2018 дата публикации

METHOD FOR PRODUCING METAL-SUPPORTED ZEOLITE FOR ALCOHOLIC BEVERAGES, METAL-SUPPORTED ZEOLITE FOR ALCOHOLIC BEVERAGES, AND METHOD FOR PRODUCING ALCOHOLIC BEVERAGES

Номер: US20180036711A1
Принадлежит:

The invention is to provide a method for producing a metal-supported zeolite for alcoholic beverages capable of efficiently removing unwanted components contained in alcoholic beverages to thereby reduce silver release, and the metal-supported zeolite for alcoholic beverages, and to provide a method for producing alcoholic beverages using the metal-supported zeolite for alcoholic beverages. For solution to problem, the production method for the metal-supported zeolite for alcoholic beverages of the invention is a production method for a metal-supported zeolite for alcoholic beverages for removing unwanted components contained in alcoholic beverages, and includes a first ion-exchange treatment step of processing a zeolite carrying a metal ion with an ammonium ion-containing aqueous solution to thereby exchange the metal ion in the zeolite for an ammonium ion, the zeolite containing a Y-type zeolite as the main ingredient, and a second ion-exchange treatment step of processing the ammonium ion-supported zeolite obtained in the previous ion-exchange treatment step with a silver ion-containing acidic aqueous solution to thereby exchange the ammonium ion therein with a silver ion. 1. A method for producing a metal-supported zeolite , comprising:performing a first ion-exchange treatment comprising processing a zeolite carrying a metal ion with an ammonium ion-containing aqueous solution to thereby exchange the metal ion in the zeolite for an ammonium ion, the zeolite comprising a Y-type zeolite as the main ingredient, andperforming a second ion-exchange treatment comprising processing the ammonium ion-supported zeolite obtained in the previous ion-exchange treatment with a silver ion-containing acidic aqueous solution to thereby exchange the ammonium ion therein with a silver ion.2. The method according to claim 1 , wherein the ammonium ion-containing aqueous solution is selected from the group consisting of an aqueous ammonium nitrate solution claim 1 , an aqueous ...

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12-02-2015 дата публикации

HYDROCARBON OIL DESULFURIZATION ADSORBING AGENT, PRODUCTION AND USE THEREOF

Номер: US20150041366A1
Принадлежит:

This disclosures provides an adsorbent which, on the basis of the total weight of the adsorbent, comprises: 1) a Si—Al molecular sieve having an A-FAU structure, wherein A represents a monovalent cation, in an amount of 1-20 wt %, 2) at least one binder selected from the group consisting of titanium dioxide, stannic oxide, zirconium oxide and alumina, in an amount of 3-35 wt %, 3) a silica source, in an amount of 5-40 wt %, 4) zinc oxide, in an amount of 10-80 wt %, and 5) at least one promoter metal selected from the group consisting of cobalt, nickel, iron and manganese, based on the metal, in an amount of 5-30 wt %, wherein at least 10 wt % of the promoter metal is present in a reduced valence state. This adsorbent exhibits improved activity and stability, and at the same time, is capable of significantly improving the octane number of the product gasoline. 1. A desulfurization adsorbent for hydrocarbon oil , on the basis of the total weight of the adsorbent , comprising the following components ,1) a Si—Al molecular sieve having an A-FAU structure, wherein A represents a monovalent cation, in an amount of 1-20 wt %,2) at least one binder selected from the group consisting of titanium dioxide, stannic oxide, zirconium oxide and alumina, in an amount of 3-35 wt %,3) a silica source, in an amount of 5-40 wt %,4) zinc oxide, in an amount of 10-80 wt %, and5) at least one promoter metal selected from the group consisting of cobalt, nickel, iron and manganese, based on the metal, in an amount of 5-30 wt %, wherein at least 10 wt % of the promoter metal is present in a reduced valence state.2. The adsorbent according to claim 1 , wherein the Si—Al molecular sieve having an A-FAU structure is in an amount of 2-15 wt % claim 1 , the binder is in an amount of 5-25 wt % claim 1 , the silica source is in an amount of 10-30 wt % claim 1 , the zinc oxide is in an amount of 25-70 wt % claim 1 , the promoter metal is in an amount of 8-25 wt %.3. The adsorbent according to claim ...

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12-02-2015 дата публикации

MODIFIED ADSORBENT FOR CAPTURING HEAVY METALS IN AQUEOUS SOLUTION

Номер: US20150041706A1
Принадлежит:

A method and adsorbent composition for removing heavy metals from contaminated water, comprising passing a stream of water having a concentration of one or more heavy metals through an adsorbent comprising granules of a mixture of from about 1 wt % to about 15 wt % clay and a thermoplastic polymer matrix; and collecting water having a reduced concentration of said heavy metal(s) downstream of said adsorbent. 1. An adsorbent composition for metal ions , comprising a granulated mixture of from about 1 wt % to about 15 wt % clay and a thermoplastic polymer matrix.2. The adsorbent composition of claim 1 , having less than about 1 wt % of additional adsorbents.3. The adsorbent composition of claim 1 , wherein the thermoplastic polymer has a melting or softening point above about 180° C.4. The adsorbent composition of claim 3 , wherein the thermoplastic polymer is polyethylene terephthalate or polystyrene.5. The adsorbent composition of claim 1 , wherein the clay is present at a concentration between about 3 wt % and 10 wt %.6. The adsorbent composition of claim 5 , wherein the clay is present at a concentration between about 4 wt % and 7 wt %.7. The adsorbent composition of claim 1 , wherein the clay has a naturally-occurring ion-exchange capacity.8. The adsorbent composition of claim 1 , wherein the clay is an Illite clay.9. The adsorbent composition of claim 1 , wherein the granulated mixture comprises granules in the size range from about 0.5 mm to about 3 mm. The invention relates to an adsorbent for removing heavy metals from contaminated water, and more particularly, to a continuous process for decontaminating a heavy metal contaminated stream of water.In the area of water treatment, such as ground water or industrial waste water treatment, there is an ever-increasing need to remove undesirable and even toxic contaminants, particularly heavy metal contaminants, from water. Many industrial processes utilize aqueous solutions of heavy metals, such as lead in ...

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24-02-2022 дата публикации

Organic-Halogen-Compound-Absorbing Agent, Method for Removing Organic Halogen Compound from Hydrocarbon Gas in which said Agent is used, Device for Absorbing Halogen Compound in which said Method is used, and method for Producing Hydrocarbon Gas

Номер: US20220055011A1
Принадлежит:

A process for treating a petroleum fraction and for efficiently absorbing an organic halogen compound from a fluid mixture of the organic halogen compound and an inorganic halogen compound derived from crude oil. Also disclosed is an improvement in absorption performance of a halogen-compound-absorbing material, thereby reducing the frequency with which the absorbing material is exchanged. The absorbing agent includes attapulgite (palygorskite) having high absorption performance with respect to organic halogen compounds. Also disclosed is an absorption column in which the aforementioned absorbing agent and a halogen-compound-absorbing agent, that includes zinc oxide, are disposed in series, thereby making it possible to raise the treatment performance with respect to a fluid that contains, in high concentrations, the organic halogen compound in addition to the inorganic halogen compound. 1. An organohalogen compound absorbent comprising attapulgite.2. The absorbent of claim 1 , wherein the content of attapulgite is at least 40% by weight claim 1 , based on the total weight of the absorbent.3. The absorbent of claim 1 , wherein the absorbent is in the form of a molded body.4. The absorbent of claim 1 , wherein the absorbent is for removing an organohalogen compound contained in a hydrocarbon gas.5. The absorbent of claim 1 , wherein the absorbent is for removing an organohalogen compound from a hydrocarbon gas previously treated with an inorganic halogen compound absorber comprising a zinc oxide and a calcium oxide.6. The absorbent of claim 1 , wherein the organohalogen compound comprises a chlorohydrocarbon.7. A method of removing an organohalogen compound from a hydrocarbon gas claim 1 , wherein the method comprises:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'contacting the hydrocarbon gas with the absorbent of .'}8. A method of removing an organohalogen compound and an inorganic halogen compound from a hydrocarbon gas claim 1 , wherein the method comprises: ...

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