Patent application number | Description | Published |
20080260621 | Preparation of Complex Metal Oxides - The present invention provides a process for making a complex metal oxide comprising the formula A | 10-23-2008 |
20080300130 | Catalyst For Improving The Adiabatic Steam Reforming Of Natural Gas - A catalyst for adiabatically prereforming a feedstock wherein the catalyst comprises 1 to 20 wt. % nickel and 0.4 to 5 wt. % potassium on a calcium aluminate support. The overall catalyst porosity is greater than 40% with greater than 70% of the overall catalyst porosity contributed by pores having pore diameters of at least 500 Å, and having a median pore diameter greater than 2600 Å, and having a nitrogen BET area less than 6.5 m | 12-04-2008 |
20090130466 | Deposition Of Metal Films On Diffusion Layers By Atomic Layer Deposition And Organometallic Precursor Complexes Therefor - Organometallic precursor complexes containing a metal and ligands containing electron withdrawing groups are disclosed. The complexes are adapted to undergo exothermic adsorption on a fully passivated diffusion barrier layer and on a metal layer deposited on the diffusion barrier layer and to undergo exothermic reduction on the diffusion barrier layer and the metal layer. The metal is preferably copper. Use of the complexes in atomic layer deposition is also disclosed. | 05-21-2009 |
20090196822 | Hydrogen Production Using Complex Metal Oxide Pellets - Complex metal oxide-containing pellets and their use for producing hydrogen. The complex metal oxide-containing pellets are suitable for use in a fixed bed reactor due to sufficient crush strength. The complex metal oxide-containing pellets comprise one or more complex metal oxides and at least one of in-situ formed calcium titanate and calcium aluminate. calcium titanate and calcium aluminate are formed by reaction of suitable precursors in a mixture with one or more complex metal carbonates. The complex metal oxide-containing pellets optionally comprise at least one precious metal. | 08-06-2009 |
20090272938 | Ionic Liquid Based Mixtures For Gas Storage and Delivery - A mixture and method for the storage and delivery of a gas are disclosed herein. In one aspect, there is provided a mixture comprising: an ionic liquid comprising an anion and a cation, at least a portion of the gas that is disposed within and reversibly chemically reacted with the ionic liquid, and optionally an unreacted gas. In another aspect, there is provided a method for delivering a gas from a mixture comprising an ionic liquid and one or more gases comprising: reacting at least a portion of the gas with the ionic liquid to provide the mixture comprising a chemically reacted gas and an ionic liquid and separating the chemically reacted gas from the mixture wherein the chemically reacted gas after the separating step has substantially the same chemical identity as the chemically reacted gas prior to the reacting step. | 11-05-2009 |
20100038593 | Tubular Reactor With Jet Impingement Heat Transfer - A tubular reactor and method for producing a product mixture in a tubular reactor where the tubular reactor comprises an internal catalytic insert having orifices for forming fluid jets for impinging the fluid on the tube wall. Jet impingement is used to improve heat transfer between the fluid in the tube and the tube wall in a non-adiabatic reactor. The tubular reactor and method may be used for endothermic reactions such as steam methane reforming and for exothermic reactions such as methanation. | 02-18-2010 |
20100068130 | Process for the Production of Hydrogen Gas Employing a Thermally Stable Catalyst - The present invention provides a process for producing a gaseous product comprising hydrogen, said process comprising: contacting a feed gas mixture comprising steam and a gas comprising from 1 to 5 carbon atoms with a catalyst structure under reaction conditions sufficient to produce the product gas comprising hydrogen, wherein the catalyst structure comprises: a metal substrate comprising a metal; at least one layer of a catalyst support material coated onto the metal substrate, wherein the catalyst support material comprises: θ-alumina, zirconia, and at least one rare earth metal oxide; and at least one catalytically active component, wherein the at least one catalytically active component is incorporated either into or onto the catalyst support material. | 03-18-2010 |
20100196259 | CO2-Sorptive Pellets and Uses Thereof | 08-05-2010 |
20100264373 | PROCESS FOR PRODUCING A HYDROGEN-CONTAINING PRODUCT GAS - A process for producing a hydrogen-containing product gas by catalytic steam-hydrocarbon reforming with an overall steam-to-carbon molar ratio between 1.5 and 2.4 for the process. The process stream is reacted in at least two prereformers prior to reaction in catalyst-containing tubes in a top-fired reformer furnace. The process stream is reacted adiabatically in the first prereformer, while the process stream is heated prior to being introduced into the second prereformer and/or the second prereformer is heated. The process avoids carbon formation on the catalyst in the catalyst-containing tubes in the primary reformer. | 10-21-2010 |
20110182802 | Reactor, A Structure Packing, and a Method for Improving Oxidation of Hydrogen Sulfide or Polysulfides in Liquid Sulfur - Disclosed is a reactor, a structured packing, and a method for increasing the rate of decomposition of polysulfides and oxidation of polysulfides and hydrogen sulfide in liquid sulfur. The reactor, the structured packing, and the method involve a structured packing for contacting a first stream and a second stream in a reactor including a catalyst. The catalyst increases the rate of decomposition of polysulfides and oxidation of polysulfides and hydrogen sulfide in the liquid sulfur of the first stream with the second stream. The first stream includes liquid sulfur containing polysulfides and dissolved hydrogen sulfide. The second stream includes an oxygen-containing gas. | 07-28-2011 |
20110194991 | Tubular Reactor With Jet Impingement Heat Transfer - A tubular reactor for producing a product mixture in a tubular reactor where the tubular reactor comprises an internal catalytic insert with cup-shaped structures having orifices for forming fluid jets for impinging the fluid on the tube wall. Jet impingement is used to improve heat transfer between the fluid in the tube and the tube wall in a non-adiabatic reactor. The tubular reactor and method may be used for endothermic reactions such as steam methane reforming and for exothermic reactions such as methanation. | 08-11-2011 |
20120148479 | Reactor, a Retained Catalyst Structure, and a Method for Improving Decomposition of Polysulfides and Removal of Hydrogen Sulfide in Liquid Sulfur - Disclosed is a reactor, a retained catalyst structure, and a method for increasing the rate of decomposition of polysulfides and removal of hydrogen sulfide in liquid sulfur. The reactor, the retained catalyst structure, and the method include a retained catalyst structure arranged and disposed for contacting a first stream and a second stream in a reactor including a catalyst. The catalyst increases the rate of decomposition of polysulfides and facilitates the removal of hydrogen sulfide in the liquid sulfur of the first stream with the second stream. The first stream includes liquid sulfur containing polysulfides and dissolved hydrogen sulfide. The second stream includes an inert gas or a low oxygen-containing gas. | 06-14-2012 |
20130225399 | SUPPORTED CATALYST AND USE THEREOF FOR REFORMING OF STEAM AND HYDROCARBONS - A method of making a supported catalyst for reforming of steam and hydrocarbons and a steam-hydrocarbon reforming process using the supported catalyst. The supported catalyst is made from a mixture comprising 20 to 99.5 mass % of lanthanum-stabilized γ-alumina and/or lanthanum-stabilized θ-alumina, 0 to 60 mass % oalumina, 0 to 25 mass % of calcium carbonate and/or magnesium carbonate, and 0.5 to 5 mass % of graphite, a cellulose ether, and/or magnesium stearate. The supported catalyst has a porosity between 55% and 75% and a pore volume between 0.3 cc/g and 0.65 cc/g. | 08-29-2013 |