| FLUOR TECHNOLOGIES CORPORATION Patent applications |
| Patent application number | Title | Published |
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| 20120130914 | JURISDICTION COMPLIANCE ENGINES - Jurisdiction compliance engines are presented. Contemplated jurisdiction compliance engines are design tool agonistic and can operate in conjunction with design tools to ensure instantiated construction objects comply with jurisdiction rules sets. The jurisdiction rules sets can include optimization criteria based on metrics that can govern how construction objects are integrated into a design project. | 05-24-2012 |
| 20120090350 | Configurations and Methods of Heating Value Control in LNG Liquefaction Plant - NGL recovery from natural gas is achieved by processing the natural gas in a scrub column that operates at high pressure. A C3+ depleted vapor stream is generated from the vapor portion of partially condensed scrub column overhead and expanded to provide refrigeration for the vapor portion to so form a second reflux stream and the C3+ depleted vapor stream. The C3+ depleted vapor stream is then combined with another vapor portion of partially condensed column overhead to produce a lean liquefaction feed stream. | 04-19-2012 |
| 20120073441 | Configurations And Methods For High Pressure Acid Gas Removal - Physical solvent is regenerated using flashing and stripping processes to produce an ultra-lean solvent. In especially preferred aspects, flashed C1-C3 hydrocarbons are recycled to the absorber, while C4+ hydrocarbons are recovered from the CO2 that is removed from the solvent. It is further preferred that depressurization of the rich solvent provides most of the refrigeration duty. | 03-29-2012 |
| 20120072386 | Intelligent Plant Development Library Environment - An intelligent plant development library environment is presented. Contemplated environments comprise an EPC knowledge system capable of incorporating know-how of one or more construction firms in the form of assembly objects. Assembly objects represent construction components (e.g., bolts, cable trays, pipes, processing units, deliverables, etc.) that can be incorporated into a plant design. Assembly objects are stored in an assembly database and include available contexts considered relevant to the assembly objects. An inference engine is utilized to derive a specified context related to a plant design from one or more design tools. The inference engine applies rule sets to infer which assembly objects to instantiate as construction objects. The inference engine can further configure the design tools to incorporate the instantiated construction objects into a plant construction project model. Example rule sets include forward chaining rules, backward chaining rules, case-based reasoning rules, inductive reasoning rules, or abductive reasoning rules. | 03-22-2012 |
| 20120024535 | Suction Pile Wellhead and Cap Closure System - Various embodiments of underwater wellhead closure systems are described that include a template having first and second anchoring ports and that is configured to be secured to a floor of a body of water. A suction pile having a cylindrical body with a head portion and an open bottom can be coupled to the first anchoring port, such that the suction pile can provide additional hold down force to the template. The system can also include a suction cap coupled to the second anchoring port, and having a cylindrical body with an open bottom and a head portion having at least one suction pump. | 02-02-2012 |
| 20110271714 | Configurations and Methods of Carbon Capture - An IGCC plant has a precombustion decarbonization unit in which acid gas is removed from a combustion gas before the combustion gas enters a combustion turbine. In one preferred configuration, a sulfur removal unit removes hydrogen sulfide from a feed gas before the desulfurized feed gas enters an autorefrigeration unit in which carbon dioxide is removed. In another preferred configuration, hydrogen sulfide is converted to carbonyl sulfide in a dryer, and the carbonyl sulfide is absorbed in the liquid carbon dioxide that is prepared from the feed gas using autorefrigeration. | 11-10-2011 |
| 20110259596 | Configurations and Methods for Improved Subsea Production Control - Systems and methods of production control are contemplated in which one or more multiphase flow meters are operationally coupled to a production conduit to provide flow and compositional information for the fluid in the production conduit. Data from the multiphase flow meter are then provided to a control system that uses the data to control operation of one or more choke valves of one or more well heads that are fluidly coupled to the production conduit. | 10-27-2011 |
| 20110256033 | Devices And Methods Of Heat Removal From Exothermic High Temperature Reaction Processes - Devices and methods are presented in which heat transfer from the surface of a high-temperature exothermic reaction mass is removed while largely maintaining the temperature of the mass at a desired level by allowing heat to radiate from the surface of the reaction mass to a first absorber that forms part of a reactor vessel, from which the heat is then removed using a second absorber. | 10-20-2011 |
| 20110240561 | Configurations and Methods of Treatment of Silicate-Containing Waste Streams - Contemplated wastewater treatment plants and processes comprise a unit in which a silicate-containing waste stream is combined with an alkaline process stream to so form a pH-controlled intermediate that is then fed to a reactor in which carbonization effects precipitation of the silicate. Following a particle growth step in the reaction vessel that renders the precipitate suitable for filtration, the so produced silicon dioxide can be safely disposed of in a landfill while the liquid can be discharged or sent to a zero liquid discharge pond to precipitate sodium carbonates. | 10-06-2011 |
| 20110203376 | Devices And Methods Of Ultrasound Time Of Flight Diffraction Sensitivity Demonstration - An ultrasound time-of-flight diffraction reference block has a plurality of notches that extend into the block to simulate cracks, wherein the notches have a normal and transverse orientation with respect to a test path formed on the block. | 08-25-2011 |
| 20110203314 | Configurations And Methods Of High Pressure Acid Gas Removal - Acid gas is removed from a feed gas using a physical solvent that is regenerated using successive flashing stages after heating of the rich solvent using low-level waste heat that is preferably produced or available within the acid gas removal plant. Especially preferred waste heat sources include compressor discharges of the refrigeration system and/or recompression system for CO2, and/or (low level) heat content from the feed gas. | 08-25-2011 |
| 20110192805 | Devices And Methods For Water Removal In Distillation Columns - Water is removed from oily water produced during operation of a separation column by withdrawing the oily water from the column during separation into an external separator where the oily water is separated into a water phase and an oily phase. The oily phase is then heated to a temperature effective to produce a density differential that drives the oily phase back into the operating column. | 08-11-2011 |
| 20110186134 | Methods And Apparatus For Splitting Multi-Phase Flow - A multi-phase fluid is split in a flow splitting device that includes a feed pipe in which a flow redistribution element induces tangential motion in the phases such that the denser phase is forced to redistribute around the periphery of the feed pipe. The so redistributed flow is then split into two or more distribution conduits that are typically perpendicular to the flow direction of the feed flow. Most typically, the feed pipe is in a vertical position. | 08-04-2011 |
| 20110178935 | Systems And Methods Of Integrated And Automated Generation Of Work Packages - Systems and methods of dynamic work package generation are presented that allow not only real-time modification of construction work packages, but also allow tracking of the work packages throughout completion and generation/updating of constructions records. The systems and methods contemplated herein will therefore improve management of safety and non-safety components, allow for traceability and tracking, and reduce errors due to user intervention. | 07-21-2011 |
| 20110175244 | Configurations and Methods of Gas-Assisted Spray Nozzles - Contemplated configurations and methods are drawn to systems in which gas assisted spray nozzles are used to distribute a liquid phase in micron-sized droplets in a device effluent at a position upstream of a second device having multiple parallel flow paths for the effluent. Most preferably, the assist gas is a high-pressure gas phase that is generated in a process upstream of the device effluent, the first device is a hydrotreating or hydrocracking reactor or distillation column, and the second device is an air cooler or heat exchanger. | 07-21-2011 |
| 20110174866 | High-Speed Friction Stir Welding - Contemplated systems and methods significantly improve friction stir welding of hard metals and particularly steel and stainless steel. Among other factors, the inventors found that high transverse velocity of the tool is critical to obtain predictable and desirable weld quality, which is preferably achieved in such materials by minimizing spindle run out. Moreover, the transverse and angular velocities are preferably selected such as to achieve a temperature in the weld that is below the phase change temperature and/or the solid state transformation point of the materials. | 07-21-2011 |
| 20110167824 | Configurations And Methods For Waste Heat Recovery And Ambient Air Vaporizers In LNG Regasification - Contemplated power plants and LNG regasification facilities employ a combination of ambient air and non-ambient air as continuous heat sources to regasify LNG and to optimize power production. Most preferably, contemplated plants and methods are operable without the need for supplemental heat sources under varying temperature conditions. | 07-14-2011 |
| 20110146164 | Modular Processing Facility - The various processes of a plant are segmented into separate process blocks that are connected to one another using fluid conduits or electrical connections. Each process block is specialized to perform specific tasks in an assembly line manner to achieve an overall goal. For example, multiple distillation process blocks could be daisy-chained to create fuel from crude oil. Each process block is generally small enough to be mounted on a truck or a flatbed for easy transport, allowing for an assembly line of process blocks to be transported anywhere in the world with ease. | 06-23-2011 |
| 20110139578 | Adjustable Conveyor Chute - A conveyor assembly has a supply source from which a plurality of rolling objects is delivered to a conveyor belt, wherein the conveyor assembly is also configured such that the horizontal velocity of the rolling objects delivered to the conveyor belt is substantially the same as the horizontal velocity of the conveyor belt. Such configuration advantageously reduces, or even eliminates undesired movement of the objects on the conveyor belt and thus significantly improves quantification of the objects on the conveyor belt. | 06-16-2011 |
| 20110127218 | Regenerator Configurations and Methods with Reduced Steam Demand - Steam for use as stripping medium in a regenerator is recovered from a portion of the regenerator bottom product using a pervaporation unit. In most preferred aspects, the portion is selected such as to maintain neutral water balance in the stripper for a desired regeneration level. | 06-02-2011 |
| 20110056238 | Methods and Configurations of Boil-off Gas Handling in LNG Regasification Terminals - A LNG storage and regasification plant includes a reliquefaction unit in which boil-off vapors from the storage tanks are re liquefied and recycled back to the LNG storage tanks for tank pressure and Wobbe index control. Preferably, LNG cold is used for reliquefaction and operational flexibility is achieved by feeding a portion of the pressurized boil-off gas to a fuel gas header and/or to be recondensed by the sendout LNG. | 03-10-2011 |
| 20100293854 | Configurations And Methods For Fuel Gas Treatment With Total Sulfur Removal And Olefin Saturation - Refinery off gases are treated in a plant in two processing steps, wherein the off gases are first scrubbed in a wash column using lean oils for removal of heavy mercaptans and C5+ hydrocarbons, and wherein a hydrotreater is then used for saturating olefinic hydrocarbons and reducing sulfurous compounds. Most preferably, lean recycle oil is used for temperature control of the hydrotreater reactor(s) in configurations where the lean oil from a hydrotreater reactor outlet separator is mixed with the reactor feed to so cool the hydrotreater reactor via evaporation. | 11-25-2010 |
| 20100233501 | Compositions and Methods for Dissimilar Material Welding - Devices and methods of welding dissimilar materials are contemplated in which an adaptor is used in an intermediate position between the dissimilar materials. Most preferred adaptors are manufactured by friction stir welding from two dissimilar materials that are identical or similar to the dissimilar materials to be welded together. Therefore, coupling of dissimilar materials in the field via the adaptors is greatly simplified as conventional welding methods can now be employed. | 09-16-2010 |
| 20100206003 | Configurations And Methods For Improved Natural Gas Liquids Recovery - Contemplated plants for recovery of NGL from natural gas employ alternate reflux streams in a first column and a residue gas bypass stream, wherein expansion of various process streams provides substantially all of the refrigeration duty in the plant. Contemplated plants not only have flexible recovery of ethane between 2% and 90% while recovering at least 99% of propane, but also reduce and more typically eliminate the need for external refrigeration. | 08-19-2010 |
| 20100198407 | Air Demand Feedback Control Systems And Methods For Sulfur Recovery Units - A Claus plant with multiple parallel thermal stages that provide a combined effluent to downstream catalytic stages includes a controller that allows independent and individual control for each of the thermal stages as a function of measured chemical composition of the thermal stage effluents and catalytic stage effluent. | 08-05-2010 |
| 20100163498 | Skim Tank Configurations And Methods - A skim tank includes a flow-control structure that forces a solid-depleted phase of a mixed-phase feed into a toroidal motion within the container to thereby provide an up-flow movement within the structure. Most preferably, at least a portion of the solid-depleted phase is recirculated to further increase up-flow movement within the structure. | 07-01-2010 |
| 20100146971 | LNG Regasification And Power Generation - LNG is regasified with concurrent power production in systems and methods where the refrigeration content of the LNG condenses a low pressure working fluid vapor and in which the combined refrigeration content of the warmed LNG and low pressure working fluid condensate condenses an intermediate pressure working fluid vapor. | 06-17-2010 |
| 20100135880 | Hydrocarbon Based Sulfur Solvent Systems and Methods - Contemplated configurations and methods for elemental sulfur removal from various gases, and especially well acid gases employ a hydrocarbon solvent that dissolves the sulfur to form a rich solvent and that is then regenerated by hydrotreating. Thus, sulfur is removed from the rich solvent as H2S that may then be processed (e.g., in Claus unit or absorption unit) while the regenerated solvent is routed back to the well and associated production pipes. | 06-03-2010 |
| 20100126187 | Configurations And Methods For Offshore LNG Regasification And Heating Value Conditioning - Contemplated plant configurations and methods employ a vaporized and supercritical LNG stream at an intermediate temperature that is expanded, wherein refrigeration content of the expanded LNG is used to chill one or more recompressor feed streams and to condense a demethanizer reflux. One portion of the so warmed and expanded LNG is condensed and fed to the demethanizer as reflux, while the other portion is expanded and fed to the demethanizer as feed stream. Most preferably, the demethanizer overhead is combined with a portion of the vaporized and supercritical LNG stream to form a pipeline product. | 05-27-2010 |
| 20100111784 | Configurations And Methods For Carbon Dioxide And Hydrogen Production From Gasification Streams - A syngas treatment plant is configured to remove sulfurous compounds and carbon dioxide from shifted or un-shifted syngas in a configuration having a decarbonization section and a desulfurization section. Most preferably, the solvent in the decarbonization section is regenerated and cooled by flashing, while the solvent is regenerated in the desulfurization section via stripping using external heat, and it is still further preferred that carbonylsulfide is removed in the desulfurization section via hydrolysis, and that the so produced hydrogen sulfide is removed in a downstream absorber. | 05-06-2010 |
| 20100101240 | Configurations and Methods for Ambient Air Vaporizers - Cryogenic fluid is vaporized using two sections of an ambient air vaporizer where in the first section ambient air is dehydrated at a temperature at or above freezing point of water using refrigeration content of partially heated cryogenic fluid, wherein the dehydrated air is used in the second section to form the partially heated cryogenic fluid from a cryogenic fluid. | 04-29-2010 |
| 20100043488 | NGL Recovery Methods and Configurations - Contemplated NGL plants include a feed gas bypass circuit through which a portion of the feed gas is provided downstream to a vapor portion of the feed gas to thereby increase turbo expander inlet temperature and demethanizer temperature. Contemplated configurations are especially advantageous for feed gases with relatively high carbon dioxide content as they entirely avoid carbon dioxide freezing in the demethanizer, provide additional power production by the turboexpander, and recover C2+ components to levels of at least 80% while achieving a low carbon dioxide content in the NGL product. | 02-25-2010 |
| 20100043453 | Ambient Air Vaporizer - Contemplated systems and methods employ a portion of vaporized and heated LNG as a defrosting medium in an LNG ambient air vaporizer. Most preferably, the LNG is heated to a temperature of about 100° F. to 400° F., and is after defrosting fed back to the LNG stream at a position that is upstream and/or downstream of the vaporizer or to the natural gas delivery pipeline. | 02-25-2010 |
| 20100030199 | Configurations And Methods For Power Generation In LNG Regasification Terminals - Disclosed are embodiments of a fluid delivery device ( | 02-04-2010 |
| 20100024473 | Configurations And Methods of RVP Control For C5+ Condensates - Controlled RVP C5+ products are produced from feed gas in configurations and methods in which a heavier portion of the feed gas is fractionated into several streams having distinct RVP and in which a C5+ stream is produced from the lighter portion of the feed gas. The so formed streams are then combined to produce C5+ products with controlled RVP. Thus, RVP control is achieved without the need for external products for blending process streams derived from the feed gas. | 02-04-2010 |
| 20100011810 | NGL Recovery Methods and Configurations - Contemplated plants and methods for NGL recovery from feed gases having a carbon dioxide content equal or greater than about 2% employ temperature control configurations that allow high-level and flexible recovery of ethane and heavier components while avoiding freezing of the carbon dioxide in the process. Where the feed gas has a significant fraction of C3+ components and moderate carbon dioxide content, a single column configuration with an intermediate reflux condenser may be used, while two-column configurations may be used for feed gases with high carbon dioxide content and relatively low C3+ component concentration. | 01-21-2010 |
| 20100011809 | Ethane Recovery Methods And Configurations - Contemplated methods and configurations use a cooled ethane and CO2-containing feed gas that is expanded in a first turbo-expander and subsequently heat-exchanged to allow for relatively high expander inlet temperatures to a second turbo expander. Consequently, the relatively warm demethanizer feed from the second expander effectively removes CO2 from the ethane product and prevents carbon dioxide freezing in the demethanizer, while another portion of the heat-exchanged and expanded feed gas is further chilled and reduced in pressure to form a lean reflux for high ethane recovery. | 01-21-2010 |
| 20100006299 | Dual Subsea Production Chokes for HPHT Well Production - Configurations and methods for subsea hydrocarbon production at high pressure wells are contemplated in which production control is achieved by implementing two choke valves in series between the wellhead and the riser The first production choke reduces pressure from well pressure to a reduced pressure, while the second production choke further reduces the pressure from the reduced pressure to riser pressure. The first production choke is preferably coupled to the production tree, and the second production choke is coupled to production tree, a subsea pipeline-end device (e.g., PLET or PLEM), a well jumper, or a flowline jumper. | 01-14-2010 |
| 20100000255 | Configurations And Methods For Gas Condensate Separation From High-Pressure Hydrocarbon Mixtures - Contemplated configurations and methods for gas processing use a refluxed absorber that receives a liquid and a vapor hydrocarbon feed. The absorber further receives a stripping medium that is at least in part formed from a vapor portion of a stabilizer overhead and also receives a scrubbing medium that is at least in part formed from a liquid portion of the stabilizer overhead. Most preferably, the absorber overhead is maintained at a temperature near or even below the hydrate point of the feed. | 01-07-2010 |
| 20090308101 | Propane Recovery Methods and Configurations - High-pressure feed gas is chilled and expanded to condense a portion of the feed gas into a C2+ enriched liquid phase and a C2+ depleted vapor phase. The liquid phase is expanded to provide additional cooling for the feed gas and deethanizer reflux prior to being fed to the deethanizer while the vapor is combined with residue gas of a deethanizer. | 12-17-2009 |
| 20090304574 | Configurations And Methods Of Hydrogen Fueling - Configurations and methods are contemplated in which an automobile filing station receives liquid ammonia and in which hydrogen is produced by catalytic cracking. The so produced hydrogen is then compressed and fed to a filling dock. Preferably, contemplated stations will include a polishing unit in which undissociated ammonia is removed and fed back to the ammonia storage tank. | 12-10-2009 |
| 20090301133 | Ethane Recovery Methods and Configurations for High Carbon Dioxide Content Feed Gases - Ethane is separated from a carbon dioxide-containing feed gas in a demethanizer that receives a rich subcooled reflux stream at very low temperature. Freezing of carbon dioxide is prevented by feeding a temperature-controlled vapor portion of the feed gas to the column, wherein the temperature of the vapor portion is adjusted by routing a portion of the expander discharge through a heat exchanger in response to the tray temperature in the demethanizer. Thus, high separation efficiency is achieved at reduced, or even eliminated carbon dioxide freezing. | 12-10-2009 |
| 20090282836 | Configurations And Methods For LNG Fueled Power Plants - Contemplated configurations and methods use first and second precoolers, preferably in alternating operation, to provide a combustion turbine with air at a temperature of 50° F., and more typically less than 32° F. and most typically less than 0° F. In such configurations and methods it is generally preferred that a heat transfer fluid circuit provides both, heated and cooled heat transfer fluid to thereby allow cooling and deicing of the precoolers. Most preferably, refrigeration is provided from an LNG regasification unit to form the cooled heat transfer fluid while heat from a power cycle (e.g., from surface condenser) is used to form the heated heat transfer fluid. | 11-19-2009 |
| 20090277219 | Configurations and Methods for Offshore LNG Regasification and BTU Control - LNG is pumped to supercritical pressure and vaporized, preferably in an offshore location to thereby form a natural gas stream with an intermediate temperature. A first portion of that stream is then processed in an onshore location to remove at least some non-methane components to thereby form a lean LNG, which is then combined with a second portion of that stream to form a sales gas having desired chemical composition. The intermediate temperature and the split ratio of the gas stream in first and second portion are a function of the concentration of the non-methane components in the LNG. | 11-12-2009 |
| 20090247653 | Configurations And Methods of SNG Production - SNG plants according to the inventive subject matter include one or more methanation reactors that produce a primary methanation product that is cooled to a temperature sufficient to condense water, which is removed in a separator. So produced dried methanation product is then split to provide a reflux stream to the methanation reactors and a feed stream to an adiabatic trim reactor. Most preferably, the plant comprises at least two methanation reactors that are operated in series, wherein the first reactor receives the recycle stream and wherein the second reactor receives a portion of the first methanation reactor effluent and a portion of the first methanation reactor feed. | 10-01-2009 |
| 20090221864 | High Ethane Recovery Configurations And Methods In LNG Regasification Facility - LNG is processed in contemplated plants and methods such that refrigeration content of the LNG feed is used to provide reflux duty to the demethanizer and to further condense a vapor phase of the demethanizer overhead product. In such plants, the demethanizer provides a bottom product to a deethanizer, wherein a demethanizer side draw provides refrigeration to the deethanizer overhead product to thus form an ethane product and deethanizer reflux. | 09-03-2009 |
| 20090217676 | LNG Vapor Handling Configurations And Methods - LNG from a carrier is unloaded to an LNG storage tank in configurations and methods in which expansion of compressed and condensed boil-off vapors from the LNG storage tank provide refrigeration to subcool the LNG that is being unloaded. Most advantageously, such configuration and methods reduce the amount of boil-off vapors and eliminate the need for a vapor return line and associated compressor. | 09-03-2009 |
| 20090216605 | Integrated Acceptance Testing - Contemplated validation systems provide access to a master validator, one or more remote validators, and an authorized party such that validation using a validation script can be performed in a flexible manner that allows modifications to the script in real time. Typically, modifications are requested by a remote validator in the field where the remote validator can not answer a validation request generated by the validation script in a proper or predetermined manner. A master validator will receive the request and modify the validation script accordingly to allow the validation to proceed. Most typically, modification of the script is authorized by an authorized party. | 08-27-2009 |
| 20090212023 | Welding Processes - Contemplated methods for welding stainless steel substantially improve welding speed and quality. Most typically, such attributes are achieved by welding a root pass using GMAW-Sm to thereby depositing a root, welding a hot pass using GMAW-P to thereby deposit additional weld metal onto the root, and by welding at least one of a fill pass and a cap pass using at least one of GMAW-P and FCAW. | 08-27-2009 |
| 20090205946 | Integrated Compressor/Stripper Configurations And Methods - Contemplated solvent regenerators include a flash drum in which lean solvent from the regenerator is flashed, and from which supplemental steam is recovered that is then fed back to the regenerator using a compressor, and most preferably a thermocompressor. Such devices have a substantially reduced net steam and energy requirement despite an increase in electrical energy demand, and further maintain a neutral water balance in the regenerator. | 08-20-2009 |
| 20090173103 | Cryogenic Process Utilizing High Pressure Absorber Column - A gas processing plant has a de-ethanizer and a refluxed absorber, wherein the absorber operates at higher pressure than the de-ethanizer, and wherein at least a portion of the absorber bottoms product is expanded to provide cooling for the absorber reflux stream and/or the distillation column feed stream. Especially contemplated gas processing plants include propane and ethane recovery plants, and where the gas processing plant is an ethane recovery plant, it is contemplated that the ethane product comprises no more than 500 ppm carbon dioxide. | 07-09-2009 |
| 20090165498 | Configurations and Methods for Rich Gas Conditioning for NGL Recovery - Contemplated gas treatment plants for recovery of NGL from rich feed gas include an upstream conditioning unit in which heavier hydrocarbons, and most typically C5 and heavier are removed prior to feeding the processed feed gas to an NGL recovery plant, thus avoiding the need to process the heavier hydrocarbons in the NGL recovery plant. Such conditioning units advantageously reduce energy demand for dehydration otherwise required and allow for production of C2-C4, and C5+ streams that can be sold as valuable products. | 07-02-2009 |
| 20090148371 | Two-Stage Quench Scrubber - Contemplated configurations and methods for flue gas treatment comprise a quench section and a scrubbing section that are configured and operated to avoid net condensation of water from the quenched flue gas in the scrubbing section. Consequently, the active agent in the scrubbing medium can be maintained at high concentration and will so allow continuous removal of SOX and NOX to very low concentrations. Moreover, as the scrubbing medium is not diluted by condensate, loss of active agent can be substantially reduced. Especially preferred systems will reduce SO2 concentrations in flue gas to less than 5 ppm, and more typically less than 3 ppm while substantially reducing water and reagent consumption | 06-11-2009 |
| 20090092524 | Configurations And Methods for Claus Plant Operation with Variable Sulfur Content - Contemplated plants include an acid gas enrichment unit in which acid gas unsuitable for feeding into a Claus plant from an upstream acid gas removal unit is separated into a concentrated hydrogen sulfide stream that is fed to the Claus plant and a carbon dioxide stream that is compressed in a compressor before sequestration, further purification, and/or recycling to a gasification unit. | 04-09-2009 |
| 20090087368 | Configurations And Methods For Removal Of Mercaptanes From Feed Gases - A sulfur species-containing feed gas is processed in a treatment plant in which COS is hydrolyzed, and in which so produced hydrogen sulfide and other sulfur species are absorbed in a lean hydrocarbon liquid. The sulfur species in the so formed rich hydrocarbon liquid are then subjected to catalytic conversion into disulfides, which are subsequently removed from the rich solvent. Most preferably, sulfur free lean solvent is regenerated in a distillation column and/or refinery unit, and light components are recycled from the rich hydrocarbon liquid to the absorber. | 04-02-2009 |
| 20090004096 | Cos-Claus Configurations and Methods - Carbonyl sulfide (COS) from a COS-containing stream ( | 01-01-2009 |
| 20090004080 | Configurations and Methods for Sox Removal in Oxygen-Containing Gases - Sulfur oxides are removed from an oxygen-containing acid gas in configurations and methods in which oxygen is removed from the acid gas using reducing gases at relatively high temperature. The so treated acid gas is then fed to a direct reduction reactor in which the sulfur species are converted to elemental sulfur. Contemplated configurations are particularly effective and economically attractive as they are generally not limited by reaction equilibrium as present in a Claus reaction and do not require solvent and solvent-associated equipment. | 01-01-2009 |
| 20090004070 | Configurations and Methods for Effluent Gas Treatment - Methods and configurations are drawn to a plant in which an effluent gas ( | 01-01-2009 |
| 20080307789 | Integration of Lng Regasification with Refinery and Power Generation - Contemplated plants thermally integrate operation of a refinery component, and most preferably of a hydrocarbon splitter with LNG regasification to provide refrigeration duty and with a power cycle to provide the reboiler duty of the component. It should be noted that such configurations advantageously allow operation of the splitter at a reduced temperature and at reduced pressure, thereby increasing separation efficiency, while the power output is boosted using air intake chilling. Most notably, such process advantages are achieved by satisfying the heating duty of LNG regasification. | 12-18-2008 |
| 20080296890 | Cryogenic Pipeline Configurations and Methods - A pipe-in-pipe pipeline has a bulkhead that transfers thermal stress from an inner pipe to an outer pipe, wherein at least part of the bulkhead forms a conduit for a product traveling through the inner pipe. Most preferably, the pipeline is a cryogenic pipeline for transport of liquefied natural gas. Where desirable, insulating material may be disposed between the inner pipe and outer pipe, while spacers may maintain the distance between the pipes. | 12-04-2008 |
| 20080271480 | Intergrated Ngl Recovery and Lng Liquefaction - Contemplated plants include a refluxed absorber and a distillation column, wherein the absorber is operated at a higher pressure than the distillation column to thereby produce a cryogenic pressurized lean gas. The lean gas is further compressed to a pressure suitable for liquefaction using energy from feed gas vapor expansion. Desired separation of C2 products is ensured by temperature control of the absorber and distillation column using flow ratios of various streams within the plant, and by dividing the separation process into two portions at different pressures. | 11-06-2008 |
| 20080202162 | Cryogenic Process Utilizing High Pressure Absorber Column - A gas processing plant has a de-ethanizer and a refluxed absorber, wherein the absorber operates at higher pressure than the de-ethanizer, and wherein at least a portion of the absorber bottoms product is expanded to provide cooling for the absorber reflux stream and/or the distillation column feed stream. Especially contemplated gas processing plants include propane and ethane recovery plants, and where the gas processing plant is an ethane recovery plant, it is contemplated that the ethane product comprises no more than 500 ppm carbon dioxide. | 08-28-2008 |
