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1.发明授权Apparatus and methods for the production of ammonia and Fischer-Tropsch liquids 有权用于生产氨和费 - 托液体的设备和方法公开(公告)号：US07919065B2
公开(公告)日：2011-04-05
申请号：US12764373
申请日：2010-04-21
CPC分类号： C01C1/0488 , C10G2/30 , C10G2/32 , C10J3/00 , C10J3/84 , C10J3/86 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/165 , C10J2300/1659 , C10J2300/1662 , C10J2300/1668 , C10J2300/1671 , C10J2300/1675 , C10J2300/1678 , C10J2300/1687 , C10J2300/1876 , C10J2300/1884 , C10J2300/1892 , C10K1/003 , C10K1/004 , C10K1/143 , C10K3/04 , Y02E20/16 , Y02P20/13 , Y02P20/52
摘要： A gasification plant and methods for producing ammonia, Fischer-Tropsch fuels, electrical power, and/or sulfur from carbon-bearing feedstocks including coal and/or petroleum coke. Methods for production of desired relative amounts of ammonia and Fischer-Tropsch liquid hydrocarbons by adjusting the amount of synthesis gas bypassing the Fischer-Tropsch reactor. The multi-product and integrated plants may be used to reduce the amount of CO2 vented into the atmosphere during the production of these products.
摘要翻译： 一种气化设备以及从包含煤和/或石油焦炭的含碳原料生产氨，费 - 托燃料，电力和/或硫的方法。 通过调节绕过费 - 托反应器的合成气的量来生产所需相对量的氨和费 - 托液体烃的方法。 多产品和综合设备可用于减少在生产这些产品期间排放到大气中的二氧化碳的量。
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2.发明授权Method for providing auxiliary power to an electric power plant using fischer-tropsch technology 有权使用费 - 托技术向发电厂提供辅助电力的方法公开(公告)号：US07644587B2
公开(公告)日：2010-01-12
申请号：US11316455
申请日：2005-12-21
申请人： Dennis L. Yakobson , Claude C. Corkadel, III , Charles B. Benham , Belma Demirel , Peter S. Pedersen
发明人： Dennis L. Yakobson , Claude C. Corkadel, III , Charles B. Benham , Belma Demirel , Peter S. Pedersen
CPC分类号： F02C6/10 , C10G2/332 , C10G2300/1003 , C10G2300/202 , C10G2400/02 , C10J2300/0903 , C10J2300/0959 , C10J2300/0969 , C10J2300/0973 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1675 , C10K1/00 , F05D2210/12 , F05D2220/72 , F05D2220/76 , Y02E20/14 , Y02E20/16 , Y02P20/129
摘要： A method for meeting both base-load and peak-load demand in a power production facility. By integrating a Fischer-Tropsch (FT) hydrocarbon production facility with an electrical power generating facility, peak-load power demand can be met by reducing the temperature of the FT reactor thereby increasing the quantity of tail gases and using FT tail gases to fuel a gas turbine generator set. The method enables rapid power response and allows the synthesis gas generating units and the FT units to operate with constant flow rates.
摘要翻译： 一种在发电设备中满足基本负载和峰值负载需求的方法。 通过将费 - 托（FT）碳氢化合物生产设备与发电设备相结合，可以通过降低FT反应器的温度来满足峰值负载功率需求，从而增加尾气量并使用FT尾气来燃料 燃气轮机发电机组。 该方法能够实现快速功率响应，并允许合成气体发生单元和FT单元以恒定的流速运行。
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3.发明申请METHOD FOR PROVIDING AUXILIARY POWER TO AN ELECTRIC POWER PLANT USING FISCHER TROPSCH TECHNOLOGY 有权使用FISCHER TROPSCH技术向电力设备提供辅助电力的方法公开(公告)号：US20100109338A1
公开(公告)日：2010-05-06
申请号：US12628975
申请日：2009-12-01
申请人： Dennis L. Yakobson , Claude C. Corkadel, III , Charles B. Benham , Belma Demirel , Peter S. Pedersen
发明人： Dennis L. Yakobson , Claude C. Corkadel, III , Charles B. Benham , Belma Demirel , Peter S. Pedersen
IPC分类号： F02C6/00 , F02C7/22 , H01L31/042 , F03D9/00 , H02K7/18
CPC分类号： F02C6/10 , C10G2/332 , C10G2300/1003 , C10G2300/202 , C10G2400/02 , C10J2300/0903 , C10J2300/0959 , C10J2300/0969 , C10J2300/0973 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1675 , C10K1/00 , F05D2210/12 , F05D2220/72 , F05D2220/76 , Y02E20/14 , Y02E20/16 , Y02P20/129
摘要： A method for meeting both base-load and peak-load demand in a power production facility. By integrating a Fischer-Tropsch (FT) hydrocarbon production facility with an electrical power generating facility, peak-load power demand can be met by reducing the temperature of the FT reactor thereby increasing the quantity of tail gases and using FT tail gases to fuel a gas turbine generator set. The method enables rapid power response and allows the synthesis gas generating units and the FT units to operate with constant flow rates.
摘要翻译： 一种在发电设备中满足基本负载和峰值负载需求的方法。 通过将费 - 托（FT）碳氢化合物生产设备与发电设备相结合，可以通过降低FT反应器的温度来满足峰值负载功率需求，从而增加尾气量并使用FT尾气来燃料 燃气轮机发电机组。 该方法能够实现快速功率响应，并允许合成气体发生单元和FT单元以恒定的流速运行。
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公开(公告)号：US07300642B1
公开(公告)日：2007-11-27
申请号：US11004036
申请日：2004-12-03
CPC分类号： C01C1/0488 , C10G2/30 , C10G2/32 , C10J3/00 , C10J3/84 , C10J3/86 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/165 , C10J2300/1659 , C10J2300/1662 , C10J2300/1668 , C10J2300/1671 , C10J2300/1675 , C10J2300/1678 , C10J2300/1687 , C10J2300/1876 , C10J2300/1884 , C10J2300/1892 , C10K1/003 , C10K1/004 , C10K1/143 , C10K3/04 , Y02E20/16 , Y02P20/13 , Y02P20/52
摘要： A gasification plant for producing ammonia, Fischer-Tropsch fuels, and electrical power from carbon-bearing feedstocks.
摘要翻译： 用于生产氨，费 - 托燃料和含碳原料的电力的气化设备。
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5.发明授权Apparatus and methods for the production of ammonia and fischer-tropsch liquids 有权用于生产氨和费 - 托液体的设备和方法公开(公告)号：US07803329B2
公开(公告)日：2010-09-28
申请号：US11874741
申请日：2007-10-18
CPC分类号： C01C1/0488 , C10G2/30 , C10G2/32 , C10J3/00 , C10J3/84 , C10J3/86 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/165 , C10J2300/1659 , C10J2300/1662 , C10J2300/1668 , C10J2300/1671 , C10J2300/1675 , C10J2300/1678 , C10J2300/1687 , C10J2300/1876 , C10J2300/1884 , C10J2300/1892 , C10K1/003 , C10K1/004 , C10K1/143 , C10K3/04 , Y02E20/16 , Y02P20/13 , Y02P20/52
摘要： A gasification plant and methods for producing ammonia, Fischer-Tropsch fuels, electrical power, and/or sulfur from carbon-bearing feedstocks including coal and/or petroleum coke. Methods for production of desired relative amounts of ammonia and Fischer-Tropsch liquid hydrocarbons by adjusting the amount of synthesis gas bypassing the Fischer-Tropsch reactor. The multi-product and integrated plants may be used to reduce the amount of CO2 vented into the atmosphere during the production of these products.
摘要翻译： 一种气化设备以及从包含煤和/或石油焦炭的含碳原料生产氨，费 - 托燃料，电力和/或硫的方法。 通过调节绕过费 - 托反应器的合成气的量来生产所需相对量的氨和费 - 托液体烃的方法。 多产品和综合设备可用于减少在生产这些产品期间排放到大气中的二氧化碳的量。
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6.发明授权公开(公告)号：US08146368B2
公开(公告)日：2012-04-03
申请号：US12628975
申请日：2009-12-01
申请人： Dennis L. Yakobson , Claude C. Corkadel, III , Charles B. Benham , Belma Demirel , Peter S. Pedersen
发明人： Dennis L. Yakobson , Claude C. Corkadel, III , Charles B. Benham , Belma Demirel , Peter S. Pedersen
CPC分类号： F02C6/10 , C10G2/332 , C10G2300/1003 , C10G2300/202 , C10G2400/02 , C10J2300/0903 , C10J2300/0959 , C10J2300/0969 , C10J2300/0973 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1675 , C10K1/00 , F05D2210/12 , F05D2220/72 , F05D2220/76 , Y02E20/14 , Y02E20/16 , Y02P20/129
摘要： A method for meeting both base-load and peak-load demand in a power production facility. By integrating a Fischer-Tropsch (FT) hydrocarbon production facility with an electrical power generating facility, peak-load power demand can be met by reducing the temperature of the FT reactor thereby increasing the quantity of tail gases and using FT tail gases to fuel a gas turbine generator set. The method enables rapid power response and allows the synthesis gas generating units and the FT units to operate with constant flow rates.
摘要翻译： 一种在发电设备中满足基本负载和峰值负载需求的方法。 通过将费 - 托（FT）碳氢化合物生产设备与发电设备相结合，可以通过降低FT反应器的温度来满足峰值负载功率需求，从而增加尾气量并使用FT尾气来燃料 燃气轮机发电机组。 该方法能够实现快速功率响应，并允许合成气体发生单元和FT单元以恒定的流速运行。
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7.发明申请Method for providing auxiliary power to an electric power plant using fischer-tropsch technology 有权使用费 - 托技术向发电厂提供辅助电力的方法公开(公告)号：US20080223046A1
公开(公告)日：2008-09-18
申请号：US11316455
申请日：2005-12-21
申请人： Dennis L. Yakobson , Claude C. Corkadel , Charles B. Benham , Belma Demirel , Peter S. Pedersen
发明人： Dennis L. Yakobson , Claude C. Corkadel , Charles B. Benham , Belma Demirel , Peter S. Pedersen
IPC分类号： F02C1/00
CPC分类号： F02C6/10 , C10G2/332 , C10G2300/1003 , C10G2300/202 , C10G2400/02 , C10J2300/0903 , C10J2300/0959 , C10J2300/0969 , C10J2300/0973 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1675 , C10K1/00 , F05D2210/12 , F05D2220/72 , F05D2220/76 , Y02E20/14 , Y02E20/16 , Y02P20/129
摘要： A method for meeting both base-load and peak-load demand in a power production facility. By integrating a Fischer-Tropsch (FT) hydrocarbon production facility with an electrical power generating facility, peak-load power demand can be met by reducing the temperature of the FT reactor thereby increasing the quantity of tail gases and using FT tail gases to fuel a gas turbine generator set. The method enables rapid power response and allows the synthesis gas generating units and the FT units to operate with constant flow rates.
摘要翻译： 一种在发电设备中满足基本负载和峰值负载需求的方法。 通过将费 - 托（FT）碳氢化合物生产设备与发电设备相结合，可以通过降低FT反应器的温度来满足峰值负载功率需求，从而增加尾气量并使用FT尾气来燃料 燃气轮机发电机组。 该方法能够实现快速功率响应，并允许合成气体发生单元和FT单元以恒定的流速运行。
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8.发明申请Apparatus and methods for the production of ammonia and fischer-tropsch liquids 有权用于生产氨和费 - 托液体的设备和方法公开(公告)号：US20080132588A1
公开(公告)日：2008-06-05
申请号：US11874741
申请日：2007-10-18
CPC分类号： C01C1/0488 , C10G2/30 , C10G2/32 , C10J3/00 , C10J3/84 , C10J3/86 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/165 , C10J2300/1659 , C10J2300/1662 , C10J2300/1668 , C10J2300/1671 , C10J2300/1675 , C10J2300/1678 , C10J2300/1687 , C10J2300/1876 , C10J2300/1884 , C10J2300/1892 , C10K1/003 , C10K1/004 , C10K1/143 , C10K3/04 , Y02E20/16 , Y02P20/13 , Y02P20/52
摘要： A gasification plant and methods for producing ammonia, Fischer-Tropsch fuels, electrical power, and/or sulfur from carbon-bearing feedstocks including coal and/or petroleum coke. Methods for production of desired relative amounts of ammonia and Fischer-Tropsch liquid hydrocarbons by adjusting the amount of synthesis gas bypassing the Fischer-Tropsch reactor. The multi-product and integrated plants may be used to reduce the amount of CO2 vented into the atmosphere during the production of these products.
摘要翻译： 一种气化设备以及从包含煤和/或石油焦炭的含碳原料生产氨，费 - 托燃料，电力和/或硫的方法。 通过调节绕过费 - 托反应器的合成气的量来生产所需相对量的氨和费 - 托液体烃的方法。 多产品和集成设备可用于在生产这些产品期间减少排放到大气中的CO 2的量。
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公开(公告)号：US07683006B2
公开(公告)日：2010-03-23
申请号：US12412779
申请日：2009-03-27
IPC分类号： B01J23/745 , C07C27/06
摘要： A method for transforming at least a part of the catalyst precursor hematite into x-carbide (Fe5C2) and ε′-carbide (FeC2.2) without a large amount of fines generation. This method slows the transformation of the hematite to iron carbides by reducing the partial pressure of the synthesis gas by inert gas dilution. The activation time is about three to about five hours.
摘要翻译： 一种将至少一部分催化剂前体赤铁矿转化为x碳化物（Fe5C2）和“碳化物”（FeC2.2）而不产生大量细粉的方法。 该方法通过惰性气体稀释降低合成气的分压来减缓赤铁矿转化为碳化铁。 激活时间约为3至5个小时。
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公开(公告)号：US20080015266A1
公开(公告)日：2008-01-17
申请号：US11456962
申请日：2006-07-12
IPC分类号： C07C27/06
摘要： A method for transforming at least a part of the catalyst precursor hematite into χ-carbide (Fe5C2) and ε′-carbide (FeC2.2) without a large amount of fines generation. This method slows the transformation of the hematite to iron carbides by reducing the partial pressure of the synthesis gas by inert gas dilution. The activation time is about three to about five hours.
摘要翻译： 一种用于将至少一部分催化剂前体赤铁矿转化为碳化物（Fe 2 O 3）2和ε-碳化物（FeC 2 H 2 O 2）的方法， SUB>），没有大量的细粉生成。 该方法通过惰性气体稀释降低合成气的分压来减缓赤铁矿转化为碳化铁。 激活时间约为3至5个小时。
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