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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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2.
公开(公告)号:US20170197827A1
公开(公告)日:2017-07-13
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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