Patent application number | Description | Published |
20090120290 | LOW TEMPERATURE SOLIDS REMOVAL SYSTEM FOR GASIFICATION - Disclosed is a process for removing coarse solids and fine solids from a gas, which includes wetting the coarse solids and fine solids in a first chamber thereby separating the coarse solids and fine solids from the gas. The first chamber also contains liquid to cool the coarse solids and the fine solids. The coarse solids and fine solids are routed to a liquid-filled second chamber where the coarse solids settle to the bottom. The liquid in the second chamber, still containing the fine solids is flushed into a third chamber where the fine solids are separated from the liquid. The separated fine solids and coarse solids are then routed to a fourth chamber. | 05-14-2009 |
20090158701 | SYSTEMS AND METHODS FOR POWER GENERATION WITH CARBON DIOXIDE ISOLATION - A power generation system includes at least one turbine system comprising a compressor section configured to supply a first portion and a second portion of compressed oxidant and an oxidant booster to further boost pressure of the first portion of compressed oxidant to generate a high pressure oxidant. The power generation system further includes a partial oxidation unit configured to receive the high pressure oxidant and a compressed fuel to generate a high pressure fuel stream and a CO | 06-25-2009 |
20090173079 | METHOD AND APPARATUS TO FACILITATE SUBSTITUTE NATURAL GAS PRODUCTION - A method of producing substitute natural gas (SNG) includes providing at least one steam turbine engine. The method also includes providing a gasification system that includes at least one gas shift reactor configured to receive a boiler feedwater stream and a synthesis gas (syngas) stream. The at least one gas shift reactor is further configured to produce a high pressure steam stream. The method further includes producing a steam stream within the at least one gas shift reactor and channeling at least a portion of the steam stream to the at least one steam turbine engine. | 07-09-2009 |
20090173080 | METHOD AND APPARATUS TO FACILITATE SUBSTITUTE NATURAL GAS PRODUCTION - A method of producing substitute natural gas (SNG) includes providing a syngas stream that includes at least some carbon dioxide (CO | 07-09-2009 |
20090173081 | METHOD AND APPARATUS TO FACILITATE SUBSTITUTE NATURAL GAS PRODUCTION - A method of producing substitute natural gas (SNG) includes providing a syngas stream that includes at least some carbon dioxide (CO | 07-09-2009 |
20090211155 | METHODS AND SYSTEMS FOR INTEGRATED BOILER FEED WATER HEATING - Methods and systems for a gasifier system are provided. The gasifier system includes a gasifier including a syngas cooler configured to transfer heat from a reaction zone of the gasifier to a flow of fluid through the syngas cooler, a reaction vessel coupled in flow communication with the syngas cooler wherein the reaction vessel is adapted to receive the flow of fluid and generate heat in an exothermic shift reaction. The system also includes a heat exchanger coupled in flow communication with the reaction vessel, the heat exchanger adapted to produce relatively high pressure steam using the generated heat. | 08-27-2009 |
20090239959 | METHODS AND SYSTEMS FOR REACTOR LOW PRODUCT VARIATION - A method of operating a carbon-to-liquids system is provided. The method includes receiving a flow of syngas at the carbon-to-liquids system, shifting the syngas to facilitate increasing a hydrogen to carbon monoxide ratio (H | 09-24-2009 |
20090239960 | METHODS AND SYSTEMS FOR FISCHER TROPSCH REACTOR LOW PRODUCT VARIATION - Methods and systems for operating a carbon to liquids system are provided. The method includes receiving a flow of syngas, shifting the syngas to increase an H | 09-24-2009 |
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 |
20100018237 | Low Water Consumption Cooling Tower for Gasification Plants - Disclosed is a hybrid cooling tower and a method and system for using the cooling tower. The cooling tower is design to reduce water consumption and eliminate plume formation. The cooling tower comprises a wet section having a plurality of wet section fans and a dry section having a plurality of dry section fans. The wet section fans are adjustable to operate at an increased rate and a reduced rate, depending upon ambient conditions surrounding the cooling tower. The wet section may comprise at least one shutter door. In operation, typically the wet section fans operate at the increased rate during a summer peak price period and at the reduced rate during a winter peak price period and an offpeak price period. Typically, the dry section fans operate at the increased rate all year. This method allows for less evaporative cooling and more latent cooling thereby reducing water consumption. | 01-28-2010 |
20100043288 | METHODS AND SYSTEMS FOR PARTIAL MODERATOR BYPASS - Methods and systems for a gasifier having a partial moderator bypass are provided. The gasifier includes a partial oxidation reactor including an inlet and an outlet and a primary reaction zone extending therebetween, the partial oxidation reactor configured to direct a flow of products of partial oxidation including fuel gases, gaseous byproducts of partial oxidation, and unburned carbon, and a secondary reaction chamber coupled in flow communication with the partial oxidation reactor, the secondary reaction chamber is configured to mix a flow of moderator with the flow of gaseous byproducts of partial oxidation and unburned carbon such that a concentration of fuel gases is increased. | 02-25-2010 |
20100044643 | Low NOx Gasification Startup System - Disclosed is a low NO | 02-25-2010 |
20100170285 | SYSTEMS FOR REDUCING COOLING WATER AND POWER CONSUMPTION IN GASIFICATION SYSTEMS AND METHODS OF ASSEMBLING SUCH SYSTEMS - An integrated gasification combined cycle system is provided. The integrated gasification combined cycle system includes an air compressor coupled in flow communication to an air separation unit, a condensate heater coupled in flow communication with the air compressor, and a condenser coupled in flow communication with the condensate heater. The condensate heater and the air compressor are coupled such that a portion of compressed air generated by the air compressor is channeled to the condensate heater. A method of assembling an integrated gasification combined cycle system is also provided. | 07-08-2010 |
20100172819 | METHODS AND SYSTEMS FOR ZERO DISCHARGE WATER TREATMENT - Methods and systems for a zero discharge waste water treatment system are provided. The system includes a filtration train including filter media having successively smaller diameter filtration elements, a reverse osmosis apparatus including a pump and a membrane coupled in flow communication with said filtration train, a vapor compressor coupled in flow communication with said reverse osmosis apparatus, and a spray dryer coupled in flow communication with said vapor compressor, said spray dryer configured to separate moisture in a brine solution from particulate suspended in the brine solution. | 07-08-2010 |
20100175426 | Power Management For Gasification Facility - Systems and methods for controlling power needs of a gasification facility are described. The systems include an ice refrigeration storage unit for supplying refrigeration to the larger consumers of cooling in the gasification facility. The methods include manipulating the ice refrigeration storage unit to minimize the utilization of power during peak price periods and maximize the utilization of power during offpeak price periods. | 07-15-2010 |
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 |
20100293918 | METHOD AND SYSTEM FOR USE WITH AN INTEGRATED GASIFICATION COMBINED CYCLE PLANT - A method of operating an integrated gasification combined cycle power generation system is provided. The method includes compressing air in an adiabatic air compressor to produce a compressed heated air stream, heating a nitrogen stream using the compressed heated air stream to produce a heated nitrogen stream and a cooled compressed air stream, and channeling the cooled compressed air stream to an air separation unit. | 11-25-2010 |
20100324156 | METHODS OF RECYCLING CARBON DIOXIDE TO THE GASIFICATION SYSTEM - Method of producing syngas in an IGCC system, comprising compressing and heating carbon dioxide-rich gas to produce heated compressed carbon dioxide-rich gas, mixing the heated compressed carbon dioxide-rich gas with oxygen and feedstock to form a feedstock mixture, subjecting the feedstock mixture to gasification to produce syngas, cooling the syngas in a radiant syngas cooler, contacting syngas cooled in the radiant syngas cooler with compressed carbon dioxide-rich gas to further cool the syngas, and removing an amount of carbon dioxide-rich gas from the product mixture and compressing the removed carbon dioxide-rich gas prior to mixing with oxygen and feedstock. | 12-23-2010 |
20110162381 | SYSTEM AND METHOD FOR COOLING SYNGAS PRODUCED FROM A GASIFIER - A syngas cooler that includes an outer wall defining a cavity. A first membrane water wall is positioned within the cavity. A thermal siphon is positioned between the first membrane water wall and the outer wall and is configured to channel a flow of syngas therethrough to facilitate cooling the channeled syngas. | 07-07-2011 |
20110179801 | METHODS AND APPARATUS FOR DILUENT NITROGEN SATURATION - In one aspect, an embodiment of the present disclosure provides an Integrated Gasification Combined Cycle (IGCC) apparatus. The apparatus includes a saturator configured to saturate NPG with water vapor, and a heat recovery steam generator (HRSG), a low pressure steam loop through the saturator, wherein the HRSG is configured to heat the low pressure steam loop. The apparatus further includes a compressor and a heat exchanger configured to heat the NPG using waste process heat and extraction air from the compressor, wherein the heated NPG thereby becomes diluent nitrogen. | 07-28-2011 |
20110198285 | Zero Discharge Water Desalination Plant With Minerals Extraction Integrated With Natural Gas Combined Cycle Power Generation - A desalination and minerals extraction process includes a desalination facility fluidly coupled to a minerals extraction facility. The desalination facility includes a nanofiltration membrane section producing a first tailings stream and a reverse osmosis membrane section producing a second tailings stream and a desalinated water outlet stream from an inlet feed stream. The extraction facility produces at least one mineral compound, an extraction tailings stream, and a second desalinated water outlet stream. At least one of the first tailings stream and the second tailings stream is fed into the extraction facility. In certain exemplary embodiments, a natural gas combined cycle power unit supplies power to at least one of the desalination facility and the extraction facility. In certain exemplary embodiments, the extraction tailings stream is recycled into the desalination facility and there are no extraction tailings streams or desalination tailings streams discharged into the environment. | 08-18-2011 |
20110297595 | DESALINATION INTAKE SYSTEM WITH NET POSITIVE IMPACT ON HABITAT - An environmentally supportive seawater intake system includes a first filtering system in communication with raw seawater for providing a flow of seawater in a first direction into a raceway. A second filtering system is also in communication with seawater in the raceway and is adapted to receive a portion of the seawater in the raceway and directing it in a second direction away from the flow of residual water in the raceway. An input device receives the second portion flowing in the second direction, and a recovery system receives and returns the first, residual portion to the sea environment. | 12-08-2011 |
20110305609 | GASIFICATION SYSTEMS FOR PARTIAL MODERATOR BYPASS - Methods and systems for a gasifier having a partial moderator bypass are provided. The gasifier includes a partial oxidation reactor including an inlet and an outlet and a primary reaction zone extending therebetween, the partial oxidation reactor configured to direct a flow of products of partial oxidation including fuel gases, gaseous byproducts of partial oxidation, and unburned carbon, and a secondary reaction chamber coupled in flow communication with the partial oxidation reactor, the secondary reaction chamber is configured to mix a flow of moderator with the flow of gaseous byproducts of partial oxidation and unburned carbon such that a concentration of fuel gases is increased. | 12-15-2011 |
20120103190 | METHOD AND SYSTEM FOR TREATING FISHCHER-TROPSCH REACTOR TAIL GAS - A method and system for coal-to-liquids (CTL) conversion is provided. The system includes a coal gasifier configured to partially oxidize a coal fuel stream to generate a flow of synthesis gas (syngas), a Fischer-Tropsch (FT) reactor configured to receive the flow of syngas and to generate a stream of tail gas, and an absorber coupled in flow communication downstream of the FT reactor and configured to receive the stream of tail gas. The absorber is further configured to generate a first flow including carbon dioxide, C2 hydrocarbons, and higher boiling gas components (C3+) and a second flow including C1, carbon monoxide, hydrogen, and nitrogen. The system also includes a first membrane separator including a selective membrane configured to separate the second flow from the absorber generating a permeate flow of hydrogen and a non-permeate flow of combustion turbine fuel gas including methane and hydrogen. | 05-03-2012 |
20120125829 | DESALINATION INTAKE SYSTEM WITH NET POSITIVE IMPACT ON HABITAT - An environmentally supportive seawater intake system includes a first filtering system in communication with raw seawater for providing a flow of seawater and a second filtering system is also in communication with the first filtering system for providing intake water to a downstream system while minimizing negative impact on the seawater environment and organic species living therein. | 05-24-2012 |
20120144840 | METHODS AND SYSTEMS OF REDUCING VISCOSITY OF GASIFICATION SYSTEM SLAG - Methods and systems for gasifier fines recycling system are provided. The system includes a gasifier slag removal system configured to separate first fines from a particulate slag removed from a gasifier by at least one of settling and filtering, a second fines handling system configured to receive second fines from a source other than the gasifier, and an injection system configured to mix the first fines and the second fines and a fuel for injection into the gasifier. | 06-14-2012 |
20120267578 | METHODS OF RECYCLING CARBON DIOXIDE TO THE GASIFICATION SYSTEM - Method of producing syngas in an IGCC system, comprising compressing and heating carbon dioxide-rich gas to produce heated compressed carbon dioxide-rich gas, mixing the heated compressed carbon dioxide-rich gas with oxygen and feedstock to form a feedstock mixture, subjecting the feedstock mixture to gasification to produce syngas, cooling the syngas in a radiant syngas cooler, contacting syngas cooled in the radiant syngas cooler with compressed carbon dioxide-rich gas to further cool the syngas, and removing an amount of carbon dioxide-rich gas from the product mixture and compressing the removed carbon dioxide-rich gas prior to mixing with oxygen and feedstock. | 10-25-2012 |
20130020259 | Membrane and Electrodialysis based Seawater Desalination with Salt, Boron and Gypsum Recovery - A method of producing desalinated water and recovering minerals from the feedwater uses membrane separation and electrodialysis brine concentration. This process can recover all of the minerals as high purity industrial minerals, including capturing the calcium and sulfate as agricultural grade gypsum and boron as high purity boric acid. In addition the process allows the use of low cost lime or dolime to produce valuable magnesium hydroxide. | 01-24-2013 |
20130192190 | METHOD AND SYSTEM FOR USE WITH AN INTEGRATED GASIFICATION COMBINED CYCLE PLANT - A method of operating an integrated gasification combined cycle power generation system is provided. The method includes compressing air in an adiabatic air compressor to produce a compressed heated air stream, heating a nitrogen stream using the compressed heated air stream to produce a heated nitrogen stream and a cooled compressed air stream, and channeling the cooled compressed air stream to an air separation unit. | 08-01-2013 |
20140026484 | METHODS 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. | 01-30-2014 |
20140041810 | SYSTEM FOR REMOVING HIGH PURITY SALT FROM A BRINE - A system for removing high purity salt from a brine. One system includes a first evaporator configured to receive a brine stream, to produce a first output comprising a sodium chloride slurry, and to produce a first intermediate output. The system also includes a second evaporator fluidly coupled to the first evaporator and configured to receive the first intermediate output, to produce a first recovery output, and to produce a second intermediate output. The system includes a third evaporator fluidly coupled to the second evaporator and configured to receive the second intermediate output and to produce a second recovery output. The first recovery output and the second recovery output are used to produce the brine stream received by the first evaporator. | 02-13-2014 |
20140042029 | SYSTEM FOR RINSING ELECTRODIALYSIS ELECTRODES - A system for rinsing electrodialysis electrodes includes an anode input coupled to an anode of an electrodialysis (ED) system for receiving a first fluid from the anode. The first fluid is for removing ions from the anode. The system also includes an anode output coupled to the anode of the ED system for providing the first fluid to the anode. The system includes a cathode input coupled to a cathode of the ED system for receiving a second fluid from the cathode. The second fluid is for removing ions from the cathode of the ED system. The system also includes a cathode output coupled to the cathode of the ED system for providing the second fluid to the cathode. The system includes an air stripper for receiving the first and/or second fluid, and for removing oxygen and/or a chlorine gas from the first and/or second fluid. | 02-13-2014 |
20140042061 | HEATING SYSTEM FOR DESALINATION - A heating system for desalination. One system includes a desalination system configured to receive a brine and to produce desalinated water from the brine. The system also includes a power production system having an engine configured to provide power to the desalination system. The power production system does not include combined cycle power production. The system also includes a heating system driven by the power production system and configured to provide heat for heating the brine. | 02-13-2014 |
20140044485 | SYSTEM FOR PRODUCING A GYPSUM SLURRY FOR IRRIGATION - A system includes a conveyor providing an agricultural grade gypsum, a pump providing a fluid, a mixing device configured to mix the agricultural grade gypsum provided by the conveyor with the fluid provided by the pump to produce a gypsum slurry, and a slurry pump configured to pump the gypsum slurry from the mixing device to a storage tank. | 02-13-2014 |
20140045248 | SYSTEM FOR REMOVING SELENIUM FROM A FEED STREAM - A system for removing selenium from a solid feed stream includes a selenium dissolver configured to selectively dissolve elemental selenium from the solid feed stream and to produce a selenium rich solution and a crystallizer coupled to the selenium dissolver and configured to receive the selenium rich solution from the dissolver, to add an acid to the selenium rich solution, to remove purified selenium from the selenium rich solution, and to remove sulfur dioxide from the selenium rich solution. | 02-13-2014 |
20140319040 | HYDROCHLORIC ACID PRODUCTION SYSTEM - A system includes an ion separation unit that may receive dilute hydrochloric acid and may generate a concentrated hydrochloric acid and a chamber fluidly coupled to the ion separation unit. The chamber may receive the concentrated hydrochloric acid and may separate the concentrated hydrochloric acid into a liquid concentrated hydrochloric acid and a vapor containing vaporized hydrochloric acid. The system also includes a scrubber fluidly coupled to the chamber. The scrubber may receive the vapor from the chamber, and the scrubber is may remove at least a portion of the vaporized hydrochloric acid from the vapor via a purified condensate to generate a purified vapor and the dilute hydrochloric acid. The system also includes a condenser fluidly coupled to the scrubber The condenser may receive the purified vapor from the scrubber to condense the purified vapor into the purified condensate, and to output the purified condensate to the scrubber. | 10-30-2014 |