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公开(公告)号：US09902914B2
公开(公告)日：2018-02-27
申请号：US14924311
申请日：2015-10-27
Applicant: Fluor Technologies Corporation
Inventor： John Mak
CPC classification number: C10L3/104 , B01D53/14 , B01D53/1406 , B01D53/1425 , B01D53/1462 , B01D2251/606 , B01D2252/2026 , B01D2252/20405 , B01D2252/20431 , B01D2252/20468 , B01D2252/20489 , B01D2252/50 , C01B17/0408 , C10L3/102 , C10L3/103 , C10L2290/12 , C10L2290/541 , C10L2290/542 , C10L2290/545
Abstract: Plants, processes, and methods for reducing the H2S and CO2 contents of shale gasses from fields that produce shale gasses having varying H2S and CO2 contents are provided. Acid gas enters an absorber and is scrubbed using a lean physical solvent, producing a treated gas and a rich physical solvent. The H2S content of the treated gas is further reduced in an amine absorber, producing a pipeline gas and a semi-lean amine. The pipeline gas contains lower levels of H2S and CO2 than gas produced using a polishing bed. A physical solvent regeneration unit regenerates the lean physical solvent from the rich physical solvent for feeding into the absorption unit. An amine regeneration unit regenerates the lean amine from the semi-lean amine for feeding into the amine absorber. Contemplated plants may further comprise a Claus Unit or a Redox unit for oxidizing H2S to elemental sulfur.
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公开(公告)号：US09884291B2
公开(公告)日：2018-02-06
申请号：US15225057
申请日：2016-08-01
Applicant: Fluor Technologies Corporation
Inventor： Thomas King Chow , Curt Graham
CPC classification number: B01D53/8606 , B01D19/0036 , B01D53/1425 , B01D53/1468 , B01D53/62 , B01D53/75 , B01D53/8609 , B01D2251/202 , B01D2251/304 , B01D2252/204 , B01D2257/302 , B01D2257/308 , B01D2257/504 , B01D2258/0283 , C01B17/164 , C01B17/165 , C01B17/167 , Y02C10/04 , Y02P20/152
Abstract: A system for reducing SO2 emissions comprises a hydrogenation reactor, a tail gas cooler, a contact condenser, a hydrolysis reactor, and an absorber. The hydrogenation reactor is configured to receive a Claus tail gas and convert at least a portion of SO2 in the Claus tail gas to H2S to produce a hydrogenated Claus tail gas stream. The hydrolysis reactor is configured to convert at least a portion of COS to H2S. The absorber comprises an amine-based solvent and is configured to absorb at least a portion of the H2S and recycle the H2S to the Claus plant.
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公开(公告)号：US09856141B2
公开(公告)日：2018-01-02
申请号：US14990646
申请日：2016-01-07
Applicant: Fluor Technologies Corporation
Inventor： Ravi Ravikumar , Patrick Goodman , Sanjiv Dabee
CPC classification number: C01B3/16 , C01B3/52 , C01B2203/0283 , C01B2203/0415 , C01B2203/0465 , C01B2203/062 , C01B2203/0883 , C01B2203/147 , C10J3/82 , C10J2300/0916 , C10J2300/093 , C10J2300/0943 , C10J2300/1618 , C10K1/001 , C10K1/004 , C10K1/006 , C10K1/101 , C10K3/04 , C10K3/06
Abstract: A method of producing syngas comprising receiving raw syngas from a gasification unit; introducing the raw syngas and water to a syngas scrubber to produce unshifted syngas; introducing a first portion of unshifted syngas to a first cooling unit to produce cooled unshifted syngas and a first aqueous condensate comprising cyanide in an amount of 5-200 ppmw; recycling the first aqueous condensate to the syngas scrubber; introducing a second portion of unshifted syngas to a water gas shift unit to produce shifted syngas; introducing the shifted syngas to a second cooling unit to produce cooled shifted syngas and a second aqueous condensate comprising cyanide in an amount of less than 2.5 ppmw; contacting the cooled shifted syngas with the cooled unshifted syngas to produce modified syngas; and introducing the second aqueous condensate to a sour water stripper to produce stripped water and an acid gas comprising H2S, CO2, and ammonia.
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64.发明申请公开(公告)号：US20170361265A1
公开(公告)日：2017-12-21
申请号：US15697238
申请日：2017-09-06
Applicant: Fluor Technologies Corporation
Inventor： John Mak
CPC classification number: B01D53/1425 , B01D53/1462 , B01D53/18 , B01D2252/202 , B01D2252/2021 , B01D2252/2023 , B01D2252/2025 , B01D2252/20431
Abstract: Acid gas is removed from a high pressure feed gas that contains significant quantities of CO2 and H2S. In especially preferred configurations and methods, feed gas is contacted in an absorber with a lean and an ultra-lean solvent that are formed by flashing rich solvent and stripping a portion of the lean solvent, respectively. Most preferably, the flash vapors and the stripping overhead vapors are recycled to the feed gas/absorber, and the treated feed gas has a CO2 concentration of less than 2 mol % and a H2S concentration of less than 10 ppmv, and more typically less than 4 ppm
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公开(公告)号：US09821267B2
公开(公告)日：2017-11-21
申请号：US14508758
申请日：2014-10-07
Applicant: FLUOR TECHNOLOGIES CORPORATION
Inventor： Curt Graham , Garry Jacobs , Jesus Cabrera , Ghaith Aljazzar
CPC classification number: B01D53/1493 , B01D53/1418 , B01D53/1425 , B01D53/1456 , C01B17/162
Abstract: Elemental sulfur carrying capacity of a hydrocarbonaceous solvent is improved by first loading the solvent with sulfur and subsequent hydrotreatment under conditions that convert at least some of the elemental sulfur in the sulfur loaded solvent to hydrogen sulfide while preserving at least 95% of the monoaromatic and polyaromatic components in the solvent.
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Patent Agency Ranking
公开(公告)号：US09815025B2
公开(公告)日：2017-11-14
申请号：US14657792
申请日：2015-03-13
Applicant: FLUOR TECHNOLOGIES CORPORATION
Inventor： Satish Reddy , Joseph Yonkoski
CPC classification number: B01D53/96 , B01D53/1425 , B01D53/1475 , B01D2252/204 , B01D2258/0283 , Y02A50/2342 , Y02C10/04 , Y02C10/06
Abstract: Corrosion in a CO2 removal system is reduced or even entirely avoided by use of a metal ion chelator unit that removes metal ions, and especially iron ions from an amine solvent to a level of equal or less than 1 mg/l without substantially binding heat stable salts.
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公开(公告)号：US20170232362A9
公开(公告)日：2017-08-17
申请号：US14184605
申请日：2014-02-19
Applicant: FLUOR TECHNOLOGIES CORPORATION
Inventor： Henry Kister , Carlos Trompiz
IPC: B01D3/42
CPC classification number: B01D3/4294 , B01D3/008 , B01D3/20 , B01D53/185 , B01J2219/32234 , B01J2219/32279 , F25J3/04927
Abstract: Embodiments of false downcomers are described having a lip extending inwardly from a bottom portion of the wall of the false downcomer. The lip has a length sufficient to deflect downward vapor from exiting through the bottom opening.
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公开(公告)号：US20170216766A1
公开(公告)日：2017-08-03
申请号：US15011748
申请日：2016-02-01
Applicant: Fluor Technologies Corporation
Inventor： Stephen George Mogose , Paul Andrews
CPC classification number: B01D53/266 , B01D53/265 , C10L3/06 , C10L2290/02 , C10L2290/54 , C10L2290/562 , C10L2290/567 , E21B43/34
Abstract: A natural gas production module including a wellhead configured to supply a stream of raw natural gas from a subterranean formation, and a first truckable gas processing module in fluid communication with the wellhead, wherein the first gas processing module includes a component configured to process the raw gas supplied by the wellhead.
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公开(公告)号：US20170203252A1
公开(公告)日：2017-07-20
申请号：US14995774
申请日：2016-01-14
Applicant: Fluor Technologies Corporation
Inventor： Dennis W. Johnson , James H. Brown
CPC classification number: B01D53/508 , B01D53/30 , B01D53/75 , B01D53/79 , B01D2251/304 , B01D2251/404 , B01D2251/602 , B01D2251/606 , B01D2251/608 , B01D2257/302 , B01D2257/404 , B01D2257/504 , B01D2258/0283 , F23J15/003 , F23J15/006 , F23J15/02 , F23J2215/20 , Y02E20/326
Abstract: A method for treating a flue gas that includes determining a sulfur trioxide concentration within the flue gas and determining an injection rate for a sulfur trioxide sorbent based upon the sulfur trioxide concentration. Also, a method for treating a flue gas that includes determining a sulfuric acid dew point for the flue gas and determining a coolant injection rate for a coolant to be injected into the flue gas to cause the flue gas to have a temperature of from about 20 to about 30° F. above the sulfuric acid dew point.
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公开(公告)号：US09677006B2
公开(公告)日：2017-06-13
申请号：US14312138
申请日：2014-06-23
Applicant: FLUOR TECHNOLOGIES CORPORATION
Inventor： Chilkunda K. Venkatesh
CPC classification number: C10G7/00 , C10G2300/308 , C10G2300/4056 , Y10T29/49716
Abstract: Plants and methods are presented for crude feed pre-processing before feeding the crude feed into a crude unit or vacuum unit. Pre-processing is preferably achieved with a combination of a preflash drum and a preflash column that allows for high-temperature treatment of the liquids and separate vapor phase handling, which advantageously enables retrofitting existing plants to accommodate lighter crude feeds.
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