Patent application number | Description | Published |
20090047366 | Inorganic Coagulation Accelerators for Individuals taking Platelet Blockers or Anticoagulants - The present invention is a method to accelerate the coagulation of blood through the application of inorganic materials to the wound of a patient on anticoagulant or platelet blocker therapy. The method comprises contacting such wounds with a substance selected from the group consisting of zeolitic molecular sieves and non-zeolitic molecular sieves, diatomaceous earth, glass powder or fibers, precipitated or fumed silica, kaolin and montmorillonite clays and Ca exchanged permutites. | 02-19-2009 |
20090123525 | Adsorbent-Containing Hemostatic Devices - The present invention utilizes a combination of a porous carrier and an adsorbent such as a molecular sieve to make a more effective hemostatic device to treat wounds in mammalian animals. These hemostatic devices contain additives that do not inhibit hemostasis. | 05-14-2009 |
20090291124 | Functional Nano-Layered Hemostatic Material/Device - The present invention utilizes a nano-coating of an oxide such as silica, a silicate or another effective oxide on a surface to accelerate blood clotting in mammalian animals. The hemostatic layer has a thickness that is effective for the hemostasis, yet can be made thin enough to result in a resorbable film which can either be applied to a biocompatible or resorbable device that can be used in surgical applications as well as in topical applications such as trauma. | 11-26-2009 |
20100025628 | Oxidation Processes Using Functional Surface Catalyst Composition - Oxidation processes using a catalyst composition which, preferably comprises a glass substrate, with one or more functional surface active constituents integrated on and/or in the substrate surface. A substantially nonporous substrate has (i) a total surface area between about 0.01 m | 02-04-2010 |
20100041929 | Selective Hydrogenation Processes Using Functional Surface Catalyst Composition - Selective hydrogenation processes using a catalyst composition which, preferably comprises a glass substrate, with one or more functional surface active constituents integrated on and/or in the substrate surface. A substantially nonporous substrate has (i) a total surface area between about 0.01 m | 02-18-2010 |
20100094069 | Dehydrogenation Processes Using Functional Surface Catalyst Composition - Dehydrogenation processes using a catalyst composition which, preferably comprises a glass substrate, with one or more functional surface active constituents integrated on and/or in the substrate surface. A substantially nonporous substrate has (i) a total surface area between about 0.01 m | 04-15-2010 |
20100273645 | Functional Surface Catalyst Composition - A catalyst composition, useful for a diversity of chemical production processes, preferably comprises a glass substrate, with one or more functional surface active constituents integrated on and/or in the substrate surface. A substantially nonporous substrate has (i) a total surface area between about 0.01 m | 10-28-2010 |
20110172088 | Functional Surface Catalyst Composition - A catalyst composition, useful for a diversity of chemical production processes, preferably comprises a glass substrate, with one or more functional surface active constituents integrated on and/or in the substrate surface. A substantially nonporous acid resistant glass substrate has (i) a total surface area between about 0.01 m | 07-14-2011 |
20110232486 | Adsorbent Media with Li Exchanged Zeolite - An adsorbent media composition has a finished media lithium-exchanged zeolite X (LiX) with a finished Li content in a range from 96% to 83%, based on the total cation equivalents in the LiX. The adsorbent media composition is obtained from a slurry comprising water, a LiX precursor having a pre-media production Li content that is greater than the finished media LiX Li content, and another media component material, such as fibers. The water used to produced the media has a specific conductance in a range from 2.2 μSiemens/cm to 150 μSiemens/cm. The finished media LiX has a monovalent cation (Na, K, Rb, Cs and combinations thereof) in a range from 0.05% to 3%, based on the total equivalents of exchangeable cations in the finished media LiX. | 09-29-2011 |
20110281721 | ADSORBENT MEDIA - Disclosed is an adsorbent media for use in adsorption systems and a method of making the same. The media includes a relatively thin support layer such as paper, an adsorbent such as a zeolite and non-activated pitch-based carbon fibers. The relatively thin layer, porous media provides the advantages of faster mass flow. Because the pitch-based carbon fibers are not activated, they retain their high thermal conductivity and, therefore, provide for fast and efficient heat diffusion through the media. | 11-17-2011 |
20120055333 | RAPID CYCLE, GAS PERMEABLE, ADSORBENT-CONTAINING PAPER CONTAINING P-ARAMID FIBRIDS AND ZEOLITE - A rapid cycle, gas permeable, adsorbent-containing (“RCA”) paper suitable for separating at least a portion of a first gas from a second gas in a gas mixture to produce a product stream enriched in the first gas. The RCA paper contains p-aramid fibrids and zeolite. | 03-08-2012 |
20120070468 | REMOVAL OF TOXINS FROM GASTROINTESTINAL FLUIDS - A process for the removal of toxic cations and anions from gastrointestinal fluids is disclosed. A pH-increasing medication is administered prior to or together with a microporous cation exchanger. An additional feature of the invention is the use of a proton form of the microporous cation exchanger. The acidity of the gastrointestinal fluids is decreased to improve the stability of the microporous cation exchangers, which are represented by the empirical formula: | 03-22-2012 |
20130004395 | PROCESSES AND APPARATUSES FOR OXIDIZING ELEMENTAL MERCURY IN FLUE GAS USING OXYCHLORINATION CATALYSTS - Processes for decreasing elemental mercury in flue gas stream are provided. The processes include receiving the flue gas stream containing elemental mercury in an oxidation zone and maintaining the oxidation zone at a temperature of less than about 200° C. In the oxidation zone, the flue gas stream is contacted with an oxychlorination catalyst. As a result, the elemental mercury is oxidized to create oxidized mercury in an oxidized flue gas. The oxidized mercury is then removed from the oxidized flue gas. | 01-03-2013 |
20130004396 | PROCESSES AND APPARATUSES FOR ELIMINATING ELEMENTAL MERCURY FROM FLUE GAS USING DEACON REACTION CATALYSTS AT LOW TEMPERATURES - Processes for decreasing elemental mercury in flue gas stream are provided. The processes include receiving the flue gas stream containing elemental mercury in an oxidation zone and maintaining the oxidation zone at a temperature of less than about 200° C. In the oxidation zone, the flue gas stream is contacted with a Deacon reaction catalyst. As a result, the elemental mercury is oxidized to create oxidized mercury in an oxidized flue gas. The oxidized mercury is then removed from the oxidized flue gas. | 01-03-2013 |
20140056766 | Methane Conversion Apparatus and Process Using a Supersonic Flow Reactor - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140056767 | Methane Conversion Apparatus and Process Using a Supersonic Flow Reactor - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140056768 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140056769 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140056770 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140056771 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058158 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058159 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058160 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058161 | METHANE CONVERSION APPARATUS AND PROCESS WITH IMPROVED MIXING USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A supersonic reactor is used for receiving the methane feed stream and heating the methane feed stream to a pyrolysis temperature. A high temperature carrier stream passes through the reactor chamber at supersonic speeds. According to various aspects, a static mixer is provided for mixing the methane feed stream and the carrier stream. | 02-27-2014 |
20140058165 | Methane Conversion Apparatus and Process with Improved Mixing Using a Supersonic Flow Reactor - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A supersonic reactor is used for receiving the methane feed stream and heating the methane feed stream to a pyrolysis temperature. A high temperature carrier stream passes through the reactor chamber at supersonic speeds. According to various aspects, a static mixer is provided for mixing the methane feed stream and the carrier stream. | 02-27-2014 |
20140058166 | Methane Conversion Apparatus and Process Using a Supersonic Flow Reactor - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058167 | Methane Conversion Apparatus and Process Using a Supersonic Flow Reactor - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058168 | Methane Conversion Apparatus and Process with Improved Mixing Using a Supersonic Flow Reactor - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A supersonic reactor is used for receiving the methane feed stream and heating the methane feed stream to a pyrolysis temperature. A high temperature carrier stream passes through the reactor chamber at supersonic speeds. According to various aspects, a static mixer is provided for mixing the methane feed stream and the carrier stream. | 02-27-2014 |
20140058169 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058170 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058171 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058172 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058173 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058174 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058175 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058176 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |
20140058178 | METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR - Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. | 02-27-2014 |