Class / Patent application number | Description | Number of patent applications / Date published |
048077000 | Coal | 32 |
20080222956 | System for the Conversion of Coal to a Gas of Specified Composition - The present invention provides a coal gasification system with an integrated control subsystem. The system generally comprises, in various combinations, a gasification reactor vessel (or converter) having one or more processing zones and one or more plasma heat sources, a solid residue handling subsystem, a gas quality conditioning subsystem, as well as an integrated control subsystem for managing the overall energetics of the conversion of coal to energy and maintaining all aspects of the gasification processes at an optimal set point The gasification system may also optionally comprise a heat recovery subsystem and/or a product gas regulating subsystem. | 09-18-2008 |
20080289254 | METHOD AND APPARATUS FOR A COAL GASIFIER - A method and apparatus for efficiently forming a gaseous material from a solid starting material. The produced gaseous material includes a CGE HHV having a high percentage of an original HHV of the starting material. The gaseous product may be used to form a plurality of materials for various purposes. | 11-27-2008 |
20080307704 | Coal gasification plant and method for operating the same - It is an object to solve a bypass line corrosion problem effectively, enable prompt supply of a fuel gas into a bypass line in the event of an emergency, and provide an inexpensive coal gasification plant. An integrated coal gasification combined cycle power generation plant includes a coal gasification furnace, a dust remover, a gas refiner, a gas turbine and the like, a main system line connecting therebetween, and a bypass line connecting between the outlet side of the coal gasification furnace in the main system line and a flare stack, wherein a dust remover bypass valve which is disposed in an upstream portion of the bypass line and which opens and closes the bypass line, a treatment gas control valve which is disposed in a downstream portion of the bypass line and which controls the flow rate, and a first inert gas input line which is disposed downstream from the dust remover bypass valve and which supplies the inert gas to the bypass line are provided. | 12-18-2008 |
20090049747 | GASIFICATION REACTOR - A gasification reactor comprising a pressure shell, a reaction zone partly bounded by a vertically oriented tubular membrane wall, a horizontally directed burner having a burner head at which, in use, a combustion flame is discharged into said reaction zone, said burner protruding into the vertical wall part of the membrane wall via a burner muffle, said burner muffle comprising several vertically oriented, concentric and interconnected rings, wherein each successive ring has an increasing diameter relative to the preceding ring resulting in that the burner muffle has a muffle opening for the burner head at one end and a larger opening at its other—flame discharge—end, the rings comprising a conduit having an inlet end for a cooling medium and an outlet for used cooling medium and wherein the muffle opening for the burner head is located between the pressure shell and the membrane wall and wherein the burner muffle protrudes into the reaction zone. | 02-26-2009 |
20090049748 | METHOD AND SYSTEM FOR CONVERTING WASTE INTO ENERGY - Disclosed herein is system comprising a system comprising a high temperature gasifier; the high temperature gasifier being operative to function at temperatures of greater than or equal to about 450° F.; and a synthesizing reactor in fluid communication with the high temperature gasifier; the synthesizing reactor being operative to convert carbon dioxide into another form of carbon. Disclosed herein too a method comprising gasifying a waste stream to produce a composition that comprises syngas; the syngas comprising carbon monoxide and hydrogen; the gasifying being conducted in a high temperature gasifier; the high temperature gasifier being operative to function at temperatures of greater than or equal to about 450° F.; converting the carbon monoxide into carbon dioxide; and feeding the carbon dioxide to an synthesizing reactor to produce an oil rich algae. | 02-26-2009 |
20090064580 | VENTURI INSERTS, INTERCHANGEABLE VENTURIS, AND METHODS OF FLUIDIZING - A fluidized bed apparatus having an agglomeration passage in which is positioned a removeable venturi inset. | 03-12-2009 |
20090077887 | Method and apparatus for treating a syngas - Treating a synthesis gas includes generating a plasma jet from a non-transferred arc torch having a main axis, the jet having a propagation axis that is substantially collinear with the main axis of the torch. The plasma torch is mounted on a feed enclosure. The syngas is received at an inlet port of the feed enclosure, the inlet port being downstream from he plasma torch and feeding the syngas so the flow encounters the plasma jet to mix the syngas and plasma jet. The mixture is propagated in an elongate reactor placed downstream from the inlet port to convert the syngas into an outlet gas. The reactor is in communication in its upstream portion with the feed enclosure and has a longitudinal axis that is substantially collinear with the propagation axis of the plasma jet. The outlet gas is extracted via an outlet port. | 03-26-2009 |
20090090054 | HYDROGASIFICATION REACTOR AND METHOD OF OPERATING SAME - The present invention provides a system and method for evaluating effects of process parameters on hydrogasification processes. The system includes a hydrogasification reactor, a pressurized feed system, a hopper system, a hydrogen gas source, and a carrier gas source. Pressurized carbonaceous material, such as coal, is fed to the reactor using the carrier gas and reacted with hydrogen to produce natural gas. | 04-09-2009 |
20090126271 | METHOD FOR GASIFYING SOLID FUEL WITH UNIFIED GAS PURIFICATION AND GASIFIER USING SAID METHOD - A function of absorbing CO | 05-21-2009 |
20090158658 | FIXED BED COAL GASIFIER - A fixed bed coal gasifier ( | 06-25-2009 |
20090178336 | PROCESS TO PROVIDE A PARTICULATE SOLID MATERIAL TO A PRESSURISED REACTOR - The invention is directed to a process to provide a particulate solid carbonaceous material to a pressurised gasification reactor comprising following steps, (a) transporting the solid material from a first lower pressure zone to a higher pressure zone using a bulk materials pump comprising a housing having a flow path for the solid material between an inlet fluidly connected to the first lower pressure zone and an outlet fluidly connected to the higher pressure zone, wherein said flow path in said housing is further defined by a space between two rotatable drive disks spaced from each other and wherein a materials scraper is present between said drive disks at the outlet to route a cake of solid material that is being transported between said drive disks to a transport conduit, which transport conduit fluidly connects the outlet of said housing and a burner as present in the gasification reactor, and (b) injecting a gaseous stream into the cake of solid material where the cake of solid material is discharged from the housing and enters the transport conduit, and (c) transporting the solid material and the gaseous stream in a transport conduit to the burner. | 07-16-2009 |
20090300986 | METHOD AND APPARATUS FOR COOLING SOLID PARTICLES UNDER HIGH TEMPERATURE AND PRESSURE - An apparatus for cooling hot ash particles discharged from a pressurized fluidized bed reactor, comprises a vessel, a solids inlet, a plurality of cooling pipes housed inside the vessel, and a solids outlet, wherein the cooling pipes are connected to a header located outside the vessel and are arranged such that the solids can flow through the cooling pipes under gravity without being blocked by the header, and wherein cooling liquid flows from the header via a flow path through the pipes, and exchanges heat with the hot ash particles through walls of the cooling pipes. The apparatus may further comprises a computerized evaporative cooling device comprising water nozzles and a thermocouple that measures the temperature inside the vessel. Also provided is a fluidized bed reactor comprising the cooling device. | 12-10-2009 |
20100018115 | METHOD AND APPARATUS TO FACILITATE SUBSTITUTE NATURAL GAS PRODUCTION - A method of producing substitute natural gas (SNG) includes providing a gasification reactor having a cavity defined at least partially by a first wall. The reactor also includes a first passage defined at least partially by at least a portion of the first wall and a second wall, wherein the first passage is in heat transfer communication with the first wall. The reactor further includes a second passage defined at least partially by at least a portion of the second wall and a third wall. The method also includes coupling the cavity in flow communication with the first and second passages. The method further includes producing a first synthetic gas (syngas) stream within the cavity. The method also includes channeling at least a portion of the first syngas stream to the first and second passages. | 01-28-2010 |
20100018116 | SYSTEM AND METHOD FOR CONVERTING SOLIDS INTO FUEL - A system for converting a solid fuel into a fuel including a pyrolytic unit for producing a pyro gas comprising hydrocarbons, a synthesis gas production unit for converting the pyro gas into a synthesis gas comprising a mixture of hydrogen and carbon monoxide, and a gas-to-liquid unit for converting the synthesis gas into a fuel. | 01-28-2010 |
20100018117 | DRY COAL POWDER GASIFICATION FURNANCE - A dry coal powder gasification furnace comprises a furnace body. The furnace body consists of a gasification furnace body for hot and dirty coal gas ( | 01-28-2010 |
20100050515 | Pressurized Gasification Apparatus to Convert Coal or Other Carbonaceous Material to Gas While Producing a Minimum Amount of Tar - An apparatus for the gasification of coal or other carbonaceous material is provided for operation at an elevated pressure of at least 30 psia, preferably, between 30 psia and 150 psia. Coal or other carbonaceous material passes downwards through two interconnected sections of a gasifier. In the upper section the coal is dried and partially devolatalized and so converted into a char before it passes into the lower section where it is converted, by reaction with steam and air, into ash and a gaseous mixture of carbon monoxide, hydrogen, carbon dioxide, methane, ethane, ethylene, hydrogen sulphide, carbonyl sulphide and small amounts of ammonia and phenols. The coal, ultimately converted to ash, exits the gasifier through a flanged semi-spherical containment section that has an integrated rotating grate, which collects and disposes of the ash and through which pass the air and steam used as reactants in the gasifier. | 03-04-2010 |
20100126067 | BURNER FOR HIGHLY CAKING COAL, AND GASIFIER - In a burner for highly caking coal in which a solid fuel channel and a gasifying agent channel are provided in a double pipe structure, the temperature increase of the particles of a highly caking solid fuel and the resulting fusion and expansion of the particles are prevented or suppressed, thereby enabling a stable operation of the gasifier. In a burner for highly caking coal in which a solid fuel channel that is attached for gasifying a highly caking solid fuel that has been pulverized into particles and that supplies the solid fuel into the gasifier, and a gasifying agent channel that supplies a gasifying agent into the gasifier are provided in a double pipe structure, the burner has a triple pipe structure including a cooling water channel that circulates cooling water between the solid fuel channel and the gasifying agent channel, and the cooling water is recovered after use. | 05-27-2010 |
20100146856 | MULTIZONE CO-GASIFICATION - A gasifier is provided gasify multiple fuels. The gasifier is configured to include a first gasification zone for gasifying a high-calorific-value feedstock with an oxidant. The gasifier is configured to substantially consume the oxidant within the first gasification zone. The gasifier further includes a second gasification zone for gasifying a low-calorific-value, high-oxygen-content feedstock. The high-calorific-value fuel may be coal and the low-calorific-value fuel may be biomass. | 06-17-2010 |
20100180503 | STARTING METHOD OF COAL GASIFIER AND STARTING DEVICE THEREFOR - In a coal gasification furnace adapted to feed pulverized coal thereinto by the use of inert carrier gas and gasify the same, any startup burner can be unnecessitated thereby eliminating any startup combustion chamber. Further, even in the use of a startup burner, it is smaller and lighter in weight than conventional startup burners, allowing the startup combustion chamber to be compact and limiting the height of the entirety of the gasification furnace. As a characteristic feature, a pulverized coal fuel supply passageway ( | 07-22-2010 |
20100242361 | FLUIDIZED BEDS HAVING MEMBRANE WALLS AND METHODS OF FLUIDIZING - A fluidized bed apparatus where at least a portion of the apparatus comprises a membrane wall. | 09-30-2010 |
20100251614 | TWO STAGE DRY FEED GASIFICATION SYSTEM AND PROCESS - A dry feed two stage gasification system and process is disclosed for gasifying feedstock such as carbonaceous materials with improved energy efficiency, along with reductions in feedstock consumption and carbon dioxide emissions. The feedstock is first dried and pretreated with the hot syngas in the upper section of the gasifier to generate a dry char that is low in volatile-matter content. This dry char is sent to the first stage of a two stage gasifier where it reacts with oxygen in the presence of steam to produce a hot syngas stream. | 10-07-2010 |
20110099903 | METHOD AND EQUIPMENT FOR PRODUCING SYNTHESIS GAS - A method and equipment for producing synthesis gas (S) from solid carbon particles (C), the carbon particles (C) being obtained by pyrolysis, gasification of the carbon particles (C) occurs by indirect heating of the carbon particles (C) in the presence of a process gas (P) in the same space where the carbon particles (C) are present, and the synthesis gas (S) generated during the gasification is discharged from the space. The method is characterised in that the carbon particles (C) and the process gas (P) are located in a reactor ( | 05-05-2011 |
20110146153 | High Pressure Feeder and Method of Operating to Feed Granular or Fine Materials - A coal feed system to feed pulverized low rank coals containing up to 25 wt % moisture to gasifiers operating up to 1000 psig pressure is described. The system includes gas distributor and collector gas permeable pipes imbedded in the lock vessel. Different methods of operation of the feed system are disclosed to minimize feed problems associated with bridging and packing of the pulverized coal. The method of maintaining the feed system and feeder device exit pressures using gas addition or extraction with the pressure control device is also described. | 06-23-2011 |
20110162277 | SYSTEMS AND METHOD FOR HEATING AND DRYING SOLID FEEDSTOCK IN A GASIFICATION SYSTEM - A system for heating and drying a quantity of coal feedstock being channeled to a gasifier includes a first heat exchanger coupled in flow communication with the gasifier for transferring heat from an input stream to an output stream of heat transfer fluid, and a second heat exchanger positioned downstream from the first heat exchanger for receiving the output stream of heat transfer fluid from the first heat exchanger, said second heat exchanger transfers heat from the output stream of heat transfer fluid to a stream of heating gas. | 07-07-2011 |
20110203177 | METHOD FOR PROCESSING COAL AND APPARATUS FOR THE IMPLEMENTATION THEREOF - The invention relates to the art of coal processing and is useful in power engineering and chemical industry for manufacturing coal adsorbents, metallurgical semicoke, and a generator or process gas. A method is proposed for coal processing, this method comprising firing of coal inside an air-tight chamber, measuring temperature inside the chamber along the height thereof, removing gas at the top of the chamber, and supplying a gasifying agent from the bottom upward. The coal processing is carried out while maintaining optimized values of the temperature difference between the burning coal bed and the gas at the outlet thereof from the chamber. An apparatus for carrying out this method consists of chamber | 08-25-2011 |
20110277385 | SYSTEM AND METHOD FOR CONVEYING A SOLID FUEL IN A CARRIER GAS - Systems are provided for gasification operations. The systems may use carbonous gas as part of plant operations. The systems may include a gasifier and a solid fuel feeder. The solid fuel feeder is capable of feeding solid fuel in a carbonous carrier gas to the gasifier during a startup period and also during a steady state period of the gasifier. | 11-17-2011 |
20110308155 | Producing Low Tar Gases in a Multi-Stage Gasifier - A system for gasifying solid matter uses multiple stages to produce low-tar combustible gas includes a first reactor having a fluidized bed to produce hydrogen containing gas, pyrolysis vapors, tars, and char particles at temperature less than the exit of the second reactor and a higher temperature partial oxidation combustor zones. A second reactor includes a higher temperature partial oxidation zone to activate hydrogen and cause cracking of aromatic ring compounds, a co-flow moving granular bed with a char gasification stage to catalyze tar reduction, and control char residence time, and a media screen comprising a parallel wire screen substantially vertically oriented supporting granular media. | 12-22-2011 |
20120031000 | System and Method for Dry Feed Gasifier Start-Up - A gasification system including a first feed line, a second feed line, a stabilization fuel line, and a fuel feed system controller including a processor. The processor is programmed to enable the stabilization fuel line to inject a stabilization fuel into a gasifier to initiate a stabilizer flame inside the gasifier, enable the first feed line to inject a dry fuel into the gasifier at a start-up dry fuel flow rate, increase the flow rate of the dry fuel from the start-up dry fuel flow rate to a normal operating condition (NOC) dry fuel flow rate, decrease a flow rate of the stabilization fuel as the flow rate of the dry fuel increases to the NOC dry fuel flow rate, and prevent the stabilization fuel line from injecting the stabilization fuel into the gasifier once the flow rate of the dry fuel is at the NOC dry fuel flow rate. | 02-09-2012 |
20120085027 | PRESSURE WAVE PULVERIZER FOR GASIFICATIN APPLICATIONS - A gasification apparatus includes a pressure wave pulverizer and a gasifier. The pressure wave pulverizer includes a first gas flow generator and a passage with a pulverizer inlet, a pulverizer outlet, and a gas inlet. The pulverizer inlet is supplied with the solid feedstock. The passage includes a gas acceleration section. The gas flow generator is configured to draw high speed gas through the gas inlet so as to induce pressure waves in the gas acceleration section thereby drying the solid feedstock and disintegrating the solid feedstock into particles. The gasifier is in flow communication with the pulverizer outlet. | 04-12-2012 |
20120266538 | TOP-FEEDING DOUBLE-SWIRL TYPE GASIFIER - The present invention provides a top-feeding double-swirl type gasifier: a feed line through which pulverized coal is supplied by nitrogen; a distributor for dividing the pulverized coal supplied; a plurality of burner nozzles for supplying the pulverized coal, divided in the distributor, and an oxidizer; a pressure reactor in which the pulverized coal and the oxidizer react with each other to produce a flow of synthesis gas; and a swirl generator for imparting a swirling force to the oxidizer which is fed into the pressure reactor, the gasifier further comprising a slag cooling and storing container placed beneath the pressure reactor. Each of the burner nozzles consists of a triple tube having a circular cross section. The pulverized coal and carrier gas are supplied to the most central region of the burner nozzle, and an oxidizer is supplied to an annular region | 10-25-2012 |
20130312328 | METHOD AND APPARATUS FOR PARTICLE RECYCLING IN MULTIPHASE CHEMICAL REACTORS - Method and apparatus for recycling fine ash particles for a multiphase chemical reactor (MCR), wherein coal is partially oxidized in the MCR to produce an exit gas stream in which fine ash particles are entrained, and wherein the MCR comprises a high temperature region with a temperature at or above a fusion temperature of the fine ash particles, wherein substantially all of the fine ash particles from the exit gas stream are returned to the high temperature region, to achieve improved carbon conversion and reduction in fly ash quantity. | 11-28-2013 |
20140173983 | GASIFICATION SYSTEM - A coal gasification system includes a coal gasifier that allows, for example, coal, as carbonaceous solid fuel, to react in the furnace with a gasifying agent (for example, air or oxygen) to generate combustible gas from the coal, a pulverized coal supply device (solid fuel supply means) that pulverizes the coal into a fine powder form and charges the coal into the coal gasifier, and an ash supply device (ash supply means) that charges ash of the coal (pulverized coal) to an inside of the coal gasifier. The ash supply device is configured to recharge slag that is generated when the pulverized coal is gasified in the coal gasifier and is discharged, into the coal gasifier as the ash. The slag is melted in a combustor to be molten slag, and adheres to an inner wall of the combustor to function as a refractory material. | 06-26-2014 |