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1.发明授权Combustion turbine and elevated pressure air separation system with argon recovery 失效燃烧涡轮机和高压空气分离系统与氩气回收
公开(公告)号：US5722259A
公开(公告)日：1998-03-03
申请号：US615665
申请日：1996-03-13
申请人： James Christian Sorensen , Rakesh Agrawal , Arthur Ramsden Smith , Steven Lawrence Feldman , Donald Winston Woodward
发明人： James Christian Sorensen , Rakesh Agrawal , Arthur Ramsden Smith , Steven Lawrence Feldman , Donald Winston Woodward
CPC分类号： F25J3/04206 , F01K23/068 , F25J3/0409 , F25J3/04303 , F25J3/04351 , F25J3/04412 , F25J3/04545 , F25J3/04563 , F25J3/04575 , F25J3/04593 , F25J3/04672 , F25J3/04678 , F25J2200/20 , F25J2200/54 , F25J2205/02 , F25J2215/02 , F25J2215/50 , F25J2235/58 , F25J2240/44 , F25J2245/02 , F25J2245/40 , F25J2245/42 , F25J2250/20 , F25J2250/40 , F25J2250/50 , F25J2270/02 , F25J2290/10 , Y02E20/16 , Y02E20/18 , Y10S62/915
摘要： An integrated gasification combined cycle (IGCC) power generation system is operated with a cryogenic air separation system which produces oxygen used in a gasification system to produce fuel gas for the IGCC combustion turbine and pressurized nitrogen which is introduced into the combustor for control of nitrogen oxides and increased combustion turbine output. The air separation system produces argon as an additional product, and the air separation system preferably operates in the feed pressure range of about 100 to about 160 psia. The compressed air feed for the air separation system and the compressed combustion air for the IGCC system are provided independently in separate compression steps.
摘要翻译： 一体化气化联合循环（IGCC）发电系统采用低温空气分离系统运行，该系统产生用于气化系统的氧气，以产生用于IGCC燃气轮机的燃料气体和被加入到燃烧器中以加压氮气的氮气 并增加燃油轮机的输出功率。 空气分离系统产生氩作为附加产物，并且空气分离系统优选在约100至约160psia的进料压力范围内操作。 用于空气分离系统的压缩空气进料和IGCC系统的压缩燃烧空气在单独的压缩步骤中独立地提供。
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2.发明授权
公开(公告)号：US5865023A
公开(公告)日：1999-02-02
申请号：US909565
申请日：1997-08-12
CPC分类号： F25J3/04127 , C10K1/004 , C10K1/10 , F01K21/047 , F01K23/068 , F02C3/22 , F02C3/28 , F25J3/04018 , F25J3/04545 , F25J3/04575 , F25J3/04593 , F25J3/04606 , F25J3/04612 , C10J2300/165 , C10J2300/1653 , C10J2300/1675 , C10J2300/1869 , C10J2300/1884 , C10J2300/1892 , F02G2250/03 , F05D2260/212 , F25J2205/32 , F25J2205/34 , F25J2230/02 , F25J2240/70 , F25J2270/14 , Y02E20/16 , Y02E20/18 , Y02P20/123 , Y02P20/124 , Y02P20/129 , Y02P80/15
摘要： A method for improving the efficiency of a gasification combined cycle system for the coproduction of electric power and one or more chemical or liquid fuel products from a synthesis gas feed containing hydrogen and carbon monoxide. Waste heat is recovered from the chemical reaction system in the form of heated water which is used to heat and humidify one or more gas streams introduced into the combustor of the combined cycle system gas turbine. Waste refrigeration recovered from the synthesis gas purification system optionally is used to cool the air inlet to the gas turbine compressor.
摘要翻译： 一种用于提高气化联合循环系统的效率的方法，用于从含有氢气和一氧化碳的合成气进料共同生产电力和一种或多种化学或液体燃料产物。 从化学反应系统以热水的形式回收余热，用于加热和加湿引入到联合循环系统燃气轮机的燃烧器中的一个或多个气流。 从合成气净化系统回收的废制冷气任选用于冷却燃气轮机压缩机的进气口。
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3.发明授权Control scheme for conversion of variable composition synthesis gas to liquid fuels in a slurry bubble column reactor 有权在浆液鼓泡塔反应器中将可变成分合成气转化为液体燃料的控制方案公开(公告)号：US06642280B2
公开(公告)日：2003-11-04
申请号：US09925233
申请日：2001-08-09
IPC分类号： C07C2700
CPC分类号： C07C29/1512 , B01J8/22 , B01J19/0006 , B01J2208/00548 , B01J2208/00628 , B01J2219/00191 , C07C41/01 , C07C43/043 , C07C31/04
摘要： A control scheme is set forth for conversion of variable composition synthesis gas to liquid fuels in a three-phase or slurry bubble column reactor (SBCR). The control scheme allows one to achieve constant or optimum liquid fuel production and constant or limited purge gas flow with highly variable synthesis gas feed condition. This is accomplished by adjusting one or more of the following independent variables: recycle ratio, water addition, and bypass flow.
摘要翻译： 阐述了在三相或浆液鼓泡塔式反应器（SBCR）中将可变成分合成气转化为液态燃料的控制方案。 控制方案允许通过高度可变的合成气进料条件实现恒定或最佳的液体燃料产生和恒定或有限的净化气体流。 这是通过调整以下独立变量中的一个或多个来实现的：循环比例，加水量和旁路流量。
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4.发明授权
公开(公告)号：US5666800A
公开(公告)日：1997-09-16
申请号：US259649
申请日：1994-06-14
CPC分类号： F25J3/04127 , C10K1/004 , C10K1/10 , F01K21/047 , F01K23/068 , F02C3/22 , F02C3/28 , F25J3/04018 , F25J3/04545 , F25J3/04575 , F25J3/04593 , F25J3/04606 , F25J3/04612 , C10J2300/165 , C10J2300/1653 , C10J2300/1675 , C10J2300/1869 , C10J2300/1884 , C10J2300/1892 , F02G2250/03 , F05D2260/212 , F25J2205/32 , F25J2205/34 , F25J2230/02 , F25J2240/70 , F25J2270/14 , Y02E20/16 , Y02E20/18 , Y02P20/123 , Y02P20/124 , Y02P20/129 , Y02P80/15
摘要： A method for improving the efficiency of a gasification combined cycle system for the coproduction of electric power and one or more chemical or liquid fuel products from a synthesis gas feed containing hydrogen and carbon monoxide. Waste heat is recovered from the chemical reaction system in the form of heated water which is used to heat and humidify one or more gas streams introduced into the combustor of the combined cycle system gas turbine. Waste refrigeration recovered from the synthesis gas purification system optionally is used to cool the air inlet to the gas turbine compressor.
摘要翻译： 一种用于提高气化联合循环系统的效率的方法，用于从含有氢气和一氧化碳的合成气进料共同生产电力和一种或多种化学或液体燃料产物。 从化学反应系统以热水的形式回收余热，用于加热和加湿引入到联合循环系统燃气轮机的燃烧器中的一个或多个气流。 从合成气净化系统回收的废制冷气任选用于冷却燃气轮机压缩机的进气口。
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