Class / Patent application number | Description | Number of patent applications / Date published |
048076000 | Producers | 24 |
20080263952 | Fuel gasification system - The present invention provides a fuel gasification furnace including a gasification chamber ( | 10-30-2008 |
20080307703 | METHOD AND APPARATUS TO PROTECT SYNTHESIS GAS VIA FLASH PYROLYSIS AND GASIFICATION IN A MOLTEN LIQUID - Disclosed are a method and a corresponding apparatus for converting a biomass reactant into synthesis gas. The method includes the steps of (1) heating biomass in a first molten liquid bath at a first temperature, wherein the first temperature is at least about 100° C., but less than the decomposition temperature of the biomass, wherein gas comprising water is evaporated and air is pressed from the biomass, thereby yielding dried biomass with minimal air content. (2) Recapturing the moisture evaporated from the biomass in step 1 for use in the process gas. (3) Heating the dried biomass in a second molten liquid bath at a second temperature, wherein the second temperature is sufficiently high to cause flash pyrolysis of the dried biomass, thereby yielding product gases, tar, and char. (4) Inserting recaptured steam into the process gas, which may optionally include external natural gas or hydrogen gas or recycled syngas for mixing and reforming with tar and non-condensable gases. (5) Further reacting the product gases, tar, and char with the process gas within a third molten liquid bath at a third temperature which is equal to or greater than the second temperature within the second molten liquid bath, thereby yielding high quality and relatively clean synthesis gas after a relatively long residence time needed for char gasification. A portion of the synthesis gas so formed is combusted to heat the first, second, and third molten liquid baths, unless external natural or hydrogen gas is available for this use. | 12-18-2008 |
20090064578 | Biomass Gasifier System with Low Energy and Maintenance Requirements - A down-draft fixed bed gasifier is disclosed that produced clean producer or synthesis gas. The gasifier can be installed at a stationary location or can be scaled down to enable placing the gasifier on a trailer that can be moved to the site of biomass generation. The gasifier is vertically oriented and generally cylindrical, and the design allows for a continual input of feedstock into the gasifier with less clogging and without lowering the gas pressure inside the gasifier. The design incorporates an internal catalyst to clean tars from the produced gas, and uses heat from the combustion chamber of the gasifier to heat the catalyst. The flow of air may be either positive flow or negative flow. | 03-12-2009 |
20090064579 | HEAT EXCHANGE REFORMER UNIT AND REFORMER SYSTEM - In a heat exchange reformer unit, a reforming passage supporting reform catalyst for inducing reforming reactions and a combustion passage supporting oxidizing catalyst for combustion are disposed adjacent to each other with a plate portion interposed therebetween. Heat-exchanging passages of the reforming passage that produce reformate gas that contains hydrogen from supplied reformation material, and heat-exchanging passages of the combustion passage that supply heat, which is generated by catalytically burning supplied fuel, to the reforming passage constitute a parallel-flow heat exchanger. Reformation material guide passages for introducing reformation material into the heat-exchanging passages in a predetermined direction, and mixed gas guide passages for introducing fuel into the heat-exchanging passages in a direction intersecting the gas flow direction in the reformation material guide passages, are provided upstream of the heat-exchanging passages in a gas flow direction. | 03-12-2009 |
20090090053 | SYSTEMS AND METHODS FOR OXIDATION OF SYNTHESIS GAS TAR - The various embodiments of the present invention relate generally to the process of gasification and the production of synthesis gas. More particularly, the various embodiments of the present disclosure relate to the process of biomass gasification and the reduction or elimination of tars from the hydrocarbon-rich product gas derived from biomass gasification. The present invention comprises systems and methods for the reduction of tar from a synthesis gas derived from biomass gasification. | 04-09-2009 |
20090158657 | METHOD AND SYSTEM OF HEATING A FLUID CATALYTIC CRACKING UNIT HAVING A REGENERATOR AND A REACTOR - In at least one embodiment of the present invention, a method of heating a FCC unit having a regenerator and a reactor having overall CO | 06-25-2009 |
20090165377 | METHOD FOR PRODUCING SYNTHETIC GAS USING AN OXYGEN-CONTAINING GAS PRODUCED BY AT LEAST ONE GAS TURBINE - The invention concerns a method for producing synthetic gas on an industrial site comprising at least one gas turbine wherein the oxygen-containing gas produced by the gas turbine is upgraded in a combustion implemented on the industrial site or in a heat recovery unit of the industrial site. Preferably, the oxygen-containing gas is used as oxidant of the combustion thereby enabling the reaction for forming the syngas. The invention also concerns a method for controlling the introduction of the oxygen-containing required for combustion to enable the syngas to be formed into a syngas reactor and an associated device. | 07-02-2009 |
20090205252 | Auger gasifier with continuous feed - The auger gasifier described includes, in its preferred embodiments, a vertically elongated (“oblong”) primary gasifier chamber with an auger that can move up and down, allowing for large amounts of fuel input when necessary. This improvement, in turn, requires and/or is facilitated by provision for simultaneous elevation adjustments of the auger and bed dam to assure that fuel material is processed in degrees from the top downward without sweeping massive amounts of the fluidized bed materials towards the output end of the chamber. Another improvement involves provision for pressurization of the primary gasifier chamber, allowing substantial improvements in the speed of processing materials through the gasifier. Due to issues arising from thermal expansion of the refractory material lining the chamber, provision is made for nozzle and refractory imbedded pipe hole thermal expansion capability. Finally, provision is for steam injection into and/or auxiliary heating of the chamber to enhance gasification and the production of syngas. | 08-20-2009 |
20090205253 | STEAM REFORMING FUEL PROCESSOR, BURNER ASSEMBLY, AND METHODS OF OPERATING THE SAME - Systems and methods for producing hydrogen gas with a fuel processing system that includes a hydrogen-producing region that produces hydrogen gas from a feed stream and a heating assembly that consumes a fuel stream to produce a heated exhaust stream for heating the hydrogen-producing region. In some embodiments, the heating assembly heats the hydrogen-producing region to at least a minimum hydrogen-producing temperature. In some embodiments, the rate at which an air stream is delivered to the heating assembly is controlled to selectively increase or decrease the temperature of the heated exhaust stream. In some embodiments, the feed stream and the fuel stream both contain a carbon-containing feedstock and at least 25 wt % water. In some embodiments, the feed and fuel streams have the same composition. | 08-20-2009 |
20090235585 | Actively Cooled Fuel Processor - A fuel processor for producing a hydrogen-containing product stream from a fuel stream and an oxidant stream is actively-cooled by a gaseous or liquid coolant which is directed to flow in contact with at least a portion of the outer shell of the fuel processor. Active cooling can improve the operating characteristics of the fuel processor as well as allowing for the use of compact fuel processor designs that would otherwise tend to have insufficient heat loss capability. | 09-24-2009 |
20090277089 | Method and apparatus for controlling gasifier efficiency - In a gasifier system, the gas thermal conductivity of the producer gas may beneficially be used as a control variable in controlling the combustion parameters of the gasifier process or gasifier system. For example, the control variable may be used to modulate the volume amount of air provided to a gasifier vessel or to modulate an oxidizer delivery rate. | 11-12-2009 |
20090282738 | Apparatus, System, and Method for Producing Bio-Fuel Utilizing Concentric-Chambered Pyrolysis - An apparatus, system, and method for subjecting biomass to pyrolysis to extract energy products using a pyrolysis unit comprising generally concentric chambers including a combustion chamber and at least one pyrolysis chamber. Each chamber is in communication with an adjacent chamber such that a directed, generally-deoxygenated heated gas stream passes through the combustion chamber to each of the pyrolysis chambers in turn. Additionally, each pair of adjacent chambers shares a heat-conducting wall, further promoting heat transfer throughout the unit. A heat source, which can be a burn enclosure configured as part of the pyrolysis unit, produces the heated gas stream. Biomass introduced into the pyrolysis unit is pyrolysized by the gas stream, resulting in exhaust containing non-condensing gases, bio-oil vapor, and entrained char. The exhaust is directed from the pyrolysis unit to other parts of the system where the bio-oil and char can be separated from the exhaust and collected. | 11-19-2009 |
20090307974 | System and process for reduction of greenhouse gas and conversion of biomass - A system and process for reducing atmospheric greenhouse gas, particularly carbon dioxide, uses, in some forms, a reactor, such as a plasma gasification reactor (PGR), to chemically reduce sequestered carbon dioxide with high heat in a carbonaceous bed to form gaseous products then used above the bed to convert biomass to lighter hydrocarbons, as well as hydrogen and carbon monoxide. In some arrangements the sequestered carbon dioxide supplied to a reactor is derived from a power plant's exhaust. The gaseous products of a reactor may be supplied to an additional reactor for processing to form liquid fuels or may be supplied as gas fuel to an electric power plant or otherwise combusted. Where the output of the CO | 12-17-2009 |
20090320368 | Methods and Systems for Gasifying a Process Stream - Methods and systems for gasifying process streams are described. In some embodiments, a method for gasifying a process stream includes gasifying the process stream in a first chamber to generate one or more product gases, transporting at least a portion of the one or more product gases to a second chamber, combusting at least a portion of the one or more product gases in the presence of one or more catalysts in the second chamber to generate a heat energy, and indirectly providing the heat energy from the second chamber to the first chamber as a primary heat source to drive gasification of the process stream. | 12-31-2009 |
20100037518 | TWO STAGE ENTRAINED GASIFICATION SYSTEM AND PROCESS - The present invention relates to a system and process for gasifying feedstock such as carbonaceous materials. The invention includes partial combustion of dry solids and pyrolysis of carbonaceous material slurry in two separate reactor sections and produce mixture products comprising synthesis gas. The invention employs one or more catalytic or sorbent bed for removing tar from the synthesis gas. The inventive system and process allow a gasification to be carried out under higher slurry feeding rate and lower temperature with the provision to manage the tar being produced, therefore to increase the conversion efficiency of the overall gasification. | 02-18-2010 |
20100037519 | DOWNDRAFT GASIFIER WITH INTERNAL CYCLONIC COMBUSTION CHAMBER - A downdraft gasifier is disclosed. The gasifier includes a biomass section that accepts and stirs raw biomass materials, a pyrolysis and tar cracking section having an inner cylinder for receiving biomass and an outer surrounding cylinder for gases from the biomass, and a char gasification section for receiving biomass and gases from the pyrolysis and tar cracking section. The char gasification section provides a grating and scraper for passing gases and ash and retaining biomass for char gasification on the grate. | 02-18-2010 |
20100058662 | CIRCULATING COAL FLUIDIZED BED COAL GAS PRODUCER SYSTEM - The present invention relates to a circulating coal fluidized bed coal gas producer system, including a coal gas producer, a high temperature separator, a heat exchanger, a low temperature separator, and a waste heat boiler, which are connected successively, wherein the coal gas producer is provided with a first air inlet and at least one secondary air inlet for feeding high temperature gasification agent into the producer, and is provided with a circulating coal inlet for feeding circulating coal into the producer, the first air inlet and the secondary air inlet are connected to the heat exchanger, and the circulating coal inlet is connected to the high temperature separator, the low temperature separator and the heat exchanger respectively. In the present invention, with designs of entering air twice, feeding coal at two inlets, two separations and circulations of powder coal, the temperature of gasification agent when fed into the producer could reach 750° C.-850° C. Reaction heat consumption between the powder coal and the gasification agent is 20% lower than that of prior art. The combustible ingredient in coal gas is 20% higher than that of prior art. The coal consumption decreases to about 0.22 Kg/Nm | 03-11-2010 |
20100162625 | Biomass fast pyrolysis system utilizing non-circulating riser reactor - A biomass fast pyrolysis system for conversion of biomass vegetation to synthetic gas and liquid fuels includes: a) a non-circulating riser reactor for pyrolysis of biomass vegetation feedstock utilizing a heat carrier, the non-circulating riser reactor being physically structured and adapted to have a rate of reaction of at least 8,000 biomass vegetation feedstock lbs/hr/ft | 07-01-2010 |
20100175320 | ENERGY EFFICIENT SYSTEM AND PROCESS FOR THE CONTINUOUS PRODUCTION OF FUELS AND ENERGY FROM SYNGAS - A system and apparatus is provided that maximizes mass and energy conversion efficiencies in an integrated thermochemical process for the conversion of fossil fuel or renewable biomass to synthesis gas. The system combines gasification, catalytic conversion of gas to liquid, electricity generation, steam and chilled water generation with a system controller to maximize the conversion efficiency from syngas to merchantable products over the efficiency of syngas alone burned as a fuel. A clean synthesis gas stream is introduced into a catalytic reactor that utilizes specially formulated catalysts to generate liquid fuel from CO and H | 07-15-2010 |
20100180502 | BURNER FOR HIGHLY CAKING COAL, AND GASIFIER - In a burner for highly caking coal in which a solid fuel channel that is attached penetrating through a surrounding wall of a gasifier for gasifying a highly caking solid fuel that has been pulverized into particles and that supplies the solid fuel into the gasifier by gas flow transportation, and a gasifying agent channel that supplies a gasifying agent into the gasifier are provided, a blockage detection unit that detects a blockage situation of the solid fuel channel is provided, and a process for reducing the temperature of the solid fuel is performed when the blockage detection unit detects a predetermined blockage situation. | 07-22-2010 |
20100199558 | SYSTEM AND METHOD FOR OPERATING POWER GENERATION SYSTEMS - A method and system for supplying fuel are provided. The fuel supply system includes a supply of a flow of fuel wherein the fuel includes an amount of moisture in a first predetermined range, a supply of a flow of gas wherein the gas includes an amount of moisture in a second predetermined range and wherein the second predetermined range is less than the first predetermined range. The fuel supply system further includes a vessel configured to receive the flow of fuel and the flow of gas, mix the flow of fuel and the flow of gas, and separate the flow of fuel from the flow of gas wherein moisture is transferred from the flow of fuel to the flow of gas. | 08-12-2010 |
20100251613 | METHOD AND APPARATUS TO RECYCLE TAIL GAS - A method of recycling a tail gas includes converting sulfur present in an acid gas stream into elemental sulfur to produce a tail gas and recycling the tail gas to at least one of a gasification reactor and a gas removal subsystem. | 10-07-2010 |
20100293853 | Method and system for wasteless processing and complete utilization of municipal and domestic wastes - Proposed are a system and method for wasteless pyrolytic processing and complete utilization of municipal and domestic wastes. The wastes are sequentially passed through units of sorting, grinding, drying, accumulating, and sending to a pyrolysis reactor for pyrolytic treatment. The syngas produced in the pyrolysis is passed through dry cleaning, dust catching, a first wet cleaning with water, a second wet cleaning with alkali, and a floatation unit for separation of water which is purified to an extent sufficient for technical use. The purified syngas is also passed through an absorber and is then used as a working medium for a power generation unit such as a gas turbine co-generator that generates electricity. Solid products of the pyrolysis reaction, such as coke, are returned to the reactor for afterburning, and the heat of the reaction can be utilized in a dryer, or the like. | 11-25-2010 |
20120017510 | DOWNDRAFT GASIFIER WITH IMPROVED STABILITY - A downdraft gasifier ( | 01-26-2012 |