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公开(公告)号:US20100146856A1
公开(公告)日:2010-06-17
申请号:US12337724
申请日:2008-12-18
申请人: Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
发明人: Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
IPC分类号: C10J3/68
CPC分类号: C10J3/721 , C10J3/466 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/1223 , Y02E20/18 , Y02P20/145
摘要: A gasifier is provided gasify multiple fuels. The gasifier is configured to include a first gasification zone for gasifying a high-calorific-value feedstock with an oxidant. The gasifier is configured to substantially consume the oxidant within the first gasification zone. The gasifier further includes a second gasification zone for gasifying a low-calorific-value, high-oxygen-content feedstock. The high-calorific-value fuel may be coal and the low-calorific-value fuel may be biomass.
摘要翻译: 提供气化器气化多种燃料。 气化器构造成包括用于使氧化剂气化高热值原料的第一气化区。 气化器构造成基本上消耗第一气化区内的氧化剂。 气化器还包括用于气化低热值,高含氧量的原料的第二气化区。 高热值燃料可以是煤,低热值燃料可以是生物质。
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公开(公告)号:US08617271B2
公开(公告)日:2013-12-31
申请号:US12337762
申请日:2008-12-18
申请人: Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
发明人: Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
IPC分类号: C01B3/36
CPC分类号: C10J3/721 , C10J3/466 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/1223 , Y02E20/18 , Y02P20/145
摘要: A coal gasifier is retrofitted to achieve multiple advantages such as reduced oxygen consumption, reduced CO2 and NOx emissions, better H:C ratio, better carbon conversion etc. This is achieved by dividing the coal into at least two zones and modifying the gasifier and operating it as described. The coal is injected into a first zone, configured to devolatilize a substantial portion of the injected coal to produce coal char and volatiles. The operation is tuned to substantially consume the oxidant injected in the first zone. A low-calorific-value, high oxidant feedstock is injected in second zone of the gasifier. The devolatilization of the low-calorific-value, high oxidant content feedstock provides the oxygen containing compounds which gasify at least a portion of the coal char generated in the first zone.
摘要翻译: 改造煤气化炉可实现多种优点,例如减少氧气消耗,减少二氧化碳和NOx排放,更好的H:C比,更好的碳转化等。这是通过将煤分为至少两个区域和修改气化器和运行 如所述。 煤被注入第一区域,其被配置为使大部分注入的煤脱挥发生以产生煤炭和挥发物。 该操作被调整以基本上消耗在第一区域中注入的氧化剂。 将低热值的高氧化剂原料注入气化器的第二区。 低热值高氧化剂含量原料的脱挥发分提供了含氧化合物,其使在第一区域中产生的煤焦炭的至少一部分气化。
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公开(公告)号:US20100146857A1
公开(公告)日:2010-06-17
申请号:US12337742
申请日:2008-12-18
申请人: Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
发明人: Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
IPC分类号: C10J3/46
CPC分类号: C10J3/466 , C10J3/506 , C10J3/721 , C10J2200/152 , C10J2300/0916 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0969 , C10J2300/0976 , Y02E20/18
摘要: A method of operating a gasifier is provided that envisions dividing the gasifier into multiple zones. A high-calorific-value feedstock with an oxidant is injected in the first zone. The gasifier is operated to substantially consume the oxidant within the first gasification zone. The method of operating the gasifier further includes injecting a low-calorific-value, high-oxygen-content feedstock in a second gasification zone. The low-calorific-value, high-oxygen-content feedstock is devolatilized and gasified in second zone. A method of operation provides for a synergistic co-gasification of the high-calorific-value feedstock and the low-calorific-value, high oxidant content feedstock. The method provides for specific control actions that enable operation of multi-fuel, multizone gasifier.
摘要翻译: 提供了一种操作气化器的方法,其设想将气化器分成多个区域。 在第一区域注入具有氧化剂的高热值原料。 操作气化器以在第一气化区内基本上消耗氧化剂。 操作气化器的方法还包括在第二气化区中注入低热值,高含氧量的原料。 低热值,高含氧量的原料在第二区域脱挥发和气化。 操作方法提供高热值原料和低热值,高氧化剂含量原料的协同共气化。 该方法提供了能够操作多燃料多区域气化器的具体控制动作。
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公开(公告)号:US08574329B2
公开(公告)日:2013-11-05
申请号:US12337742
申请日:2008-12-18
申请人: Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
发明人: Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
CPC分类号: C10J3/466 , C10J3/506 , C10J3/721 , C10J2200/152 , C10J2300/0916 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0969 , C10J2300/0976 , Y02E20/18
摘要: A method of operating a gasifier is provided that envisions dividing the gasifier into multiple zones. A high-calorific-value feedstock with an oxidant is injected in the first zone. The gasifier is operated to substantially consume the oxidant within the first gasification zone. The method of operating the gasifier further includes injecting a low-calorific-value, high-oxygen-content feedstock in a second gasification zone. The low-calorific-value, high-oxygen-content feedstock is devolatilized and gasified in second zone. A method of operation provides for a synergistic co-gasification of the high-calorific-value feedstock and the low-calorific-value, high oxidant content feedstock. The method provides for specific control actions that enable operation of multi-fuel, multizone gasifier.
摘要翻译: 提供了一种操作气化器的方法,其设想将气化器分成多个区域。 在第一区域注入具有氧化剂的高热值原料。 操作气化器以在第一气化区内基本上消耗氧化剂。 操作气化器的方法还包括在第二气化区中注入低热值,高含氧量的原料。 低热值,高含氧量的原料在第二区域脱挥发和气化。 操作方法提供高热值原料和低热值,高氧化剂含量原料的协同共气化。 该方法提供了能够操作多燃料多区域气化器的具体控制动作。
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公开(公告)号:US20100146858A1
公开(公告)日:2010-06-17
申请号:US12337762
申请日:2008-12-18
申请人: Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
发明人: Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
IPC分类号: C10J3/00
CPC分类号: C10J3/721 , C10J3/466 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/1223 , Y02E20/18 , Y02P20/145
摘要: A coal gasifier is retrofitted to achieve multiple advantages such as reduced oxygen consumption, reduced CO2 and NOx emissions, better H:C ratio, better carbon conversion etc. This is achieved by dividing the coal into at least two zones and modifying the gasifier and operating it as described. The coal is injected into a first zone, configured to devolatilize a substantial portion of the injected coal to produce coal char and volatiles. The operation is tuned to substantially consume the oxidant injected in the first zone. A low-calorific-value, high oxidant feedstock is injected in second zone of the gasifier. The devolatilization of the low-calorific-value, high oxidant content feedstock provides the oxygen containing compounds which gasify at least a portion of the coal char generated in the first zone.
摘要翻译: 改造煤气化炉可实现多种优点,例如减少氧气消耗,减少二氧化碳和NOx排放,更好的H:C比,更好的碳转化等。这是通过将煤分为至少两个区域和修改气化器和运行 如所述。 煤被注入第一区域,其被配置为使大部分注入的煤脱挥发生以产生煤炭和挥发物。 该操作被调整以基本上消耗在第一区域中注入的氧化剂。 将低热值的高氧化剂原料注入气化器的第二区。 低热值高氧化剂含量原料的脱挥发分提供了含氧化合物,其使在第一区域中产生的煤焦炭的至少一部分气化。
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公开(公告)号:US07683232B2
公开(公告)日:2010-03-23
申请号:US11137770
申请日:2005-05-25
CPC分类号: C11C3/003 , C01B3/323 , C01B3/382 , C01B2203/0244 , C01B2203/06 , C01B2203/1023 , C01B2203/1029 , C01B2203/1047 , C01B2203/1094 , C07C67/333 , C10G3/45 , C10G3/47 , C10G3/48 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2400/20 , Y02E50/13 , Y02P30/20 , C07C69/52 , C07C69/533
摘要: A process is disclosed for producing functionalized olefins from a fuel source including an organic compound including a functional group. Useful fuel sources include, for example, biofeedstocks (e.g., carbohydrates, triglycerides, polyols, and biodiesel). The process is preferably carried out by partial oxidation. The overall process can be carried out autothermally.
摘要翻译: 公开了从包括官能团的有机化合物的燃料源制备官能化烯烃的方法。 有用的燃料来源包括例如生物饲料(例如,碳水化合物,甘油三酯,多元醇和生物柴油)。 该方法优选通过部分氧化进行。 整个过程可以自动进行。
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公开(公告)号:US20060014840A1
公开(公告)日:2006-01-19
申请号:US11137770
申请日:2005-05-25
IPC分类号: C07C27/10
CPC分类号: C11C3/003 , C01B3/323 , C01B3/382 , C01B2203/0244 , C01B2203/06 , C01B2203/1023 , C01B2203/1029 , C01B2203/1047 , C01B2203/1094 , C07C67/333 , C10G3/45 , C10G3/47 , C10G3/48 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2400/20 , Y02E50/13 , Y02P30/20 , C07C69/52 , C07C69/533
摘要: A process is disclosed for producing functionalized olefins from a fuel source including an organic compound including a functional group. Useful fuel sources include, for example, biofeedstocks (e.g., carbohydrates, triglycerides, polyols, and biodiesel). The process is preferably carried out by partial oxidation. The overall process can be carried out autothermally.
摘要翻译: 公开了从包括官能团的有机化合物的燃料源制备官能化烯烃的方法。 有用的燃料来源包括例如生物饲料(例如,碳水化合物,甘油三酯,多元醇和生物柴油)。 该方法优选通过部分氧化来进行。 整个过程可以自动进行。
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公开(公告)号:US20100140137A1
公开(公告)日:2010-06-10
申请号:US12331622
申请日:2008-12-10
申请人: Gregg A. Deluga , Dan Hancu , Jin Ki Hong , Daniel G. Norton , Rick B. Watson , Arturo Vazquez , Ramanathan Subramanian
发明人: Gregg A. Deluga , Dan Hancu , Jin Ki Hong , Daniel G. Norton , Rick B. Watson , Arturo Vazquez , Ramanathan Subramanian
IPC分类号: C10G11/00 , B01J21/04 , B01J23/60 , B01J23/46 , B01J23/42 , B01J23/656 , B01J23/63 , B01J19/00
CPC分类号: B01J37/0215 , B01D53/9409 , B01D2251/208 , B01J23/40 , B01J23/464 , B01J23/468 , B01J23/60 , B01J23/626 , B01J23/63 , B01J23/6567 , B01J35/04 , B01J37/0242 , C01B3/40 , C01B2203/0261 , C10G11/00 , C10G11/02 , C10G11/10 , F01N3/2066 , F01N2370/02 , F01N2510/06 , F01N2610/03 , F01N2610/08 , Y02P20/52 , Y02T10/24
摘要: A reductant producing apparatus and method is provided, the apparatus includes a catalyst attached to an encasement. The encasement has a first and second intake formed therein that are fluidly coupled to the catalyst. The first intake configured to allow entry of a hydrocarbon fuel into the encasement. The second intake is configured to allow entry of oxygen into the encasement. The catalyst is configured to catalyze an autothermal reaction to convert a mixture into a plurality of reductants comprising a plurality of hydrocarbons having a hydrocarbon chain length that is less than a hydrocarbon chain length of hydrocarbons in the hydrocarbon fuel. The mixture comprises the hydrocarbon fuel and the oxygen, and the mixture has a carbon-to-oxygen ratio that is greater than a one-to-one ratio.
摘要翻译: 提供了还原剂的制造装置和方法,该装置包括附着在外壳上的催化剂。 包装件具有形成在其中的第一和第二进料,其流体地联接到催化剂。 配置为允许碳氢化合物燃料进入外壳的第一进气口。 第二摄入被配置为允许氧进入包装。 催化剂被配置为催化自热反应以将混合物转化为多种还原剂,其包含烃链长度小于烃燃料中烃链长度的多个烃。 该混合物包括烃燃料和氧气,并且该混合物的碳 - 氧比大于一比一比。
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公开(公告)号:US09011647B2
公开(公告)日:2015-04-21
申请号:US12478852
申请日:2009-06-05
申请人: Vitali Victor Lissianski , Anthony Mark Thompson , Daniel Lawrence Derr , Gregg Anthony Deluga , Ramanathan Subramanian , Surinder Prabhjot Singh
发明人: Vitali Victor Lissianski , Anthony Mark Thompson , Daniel Lawrence Derr , Gregg Anthony Deluga , Ramanathan Subramanian , Surinder Prabhjot Singh
IPC分类号: C10G1/00
CPC分类号: C10G1/00
摘要: A process for the plasma-assisted treatment of coal in which coal is directly converted to heavy hydrocarbons. The first step in the process is direct conversion of coal to aliphatic hydrocarbons under plasma conditions in the presence of light hydrocarbons, such as natural gas. In the second process step, the aliphatic hydrocarbons are upgraded to a liquid fuel. The energy for the process can be provided by radio frequency energy, such as microwave energy, that is powered by a renewable energy source. The process has flexibility to adjust aromatic content in the fuel to match fuel specification requirements.
摘要翻译: 煤的等离子体辅助处理方法,其中煤直接转化为重质烃。 该方法的第一步是在轻烃(如天然气)存在下,在等离子体条件下将煤直接转化成脂肪烃。 在第二工艺步骤中,将脂族烃升级成液体燃料。 该过程的能量可以通过由可再生能源供电的射频能量(例如微波能量)来提供。 该方法具有调节燃料中芳烃含量的灵活性,以符合燃料规格要求。
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公开(公告)号:US20100307960A1
公开(公告)日:2010-12-09
申请号:US12478852
申请日:2009-06-05
申请人: Vitali Victor Lissianski , Anthony Mark Thompson , Daniel Lawrence Derr , Gregg Anthony Deluga , Ramanathan Subramanian , Surinder Prabhjot Singh
发明人: Vitali Victor Lissianski , Anthony Mark Thompson , Daniel Lawrence Derr , Gregg Anthony Deluga , Ramanathan Subramanian , Surinder Prabhjot Singh
CPC分类号: C10G1/00
摘要: A process for the plasma-assisted treatment of coal in which coal is directly converted to heavy hydrocarbons. The first step in the process is direct conversion of coal to aliphatic hydrocarbons under plasma conditions in the presence of light hydrocarbons, such as natural gas. In the second process step, the aliphatic hydrocarbons are upgraded to a liquid fuel. The energy for the process can be provided by radio frequency energy, such as microwave energy, that is powered by a renewable energy source. The process has flexibility to adjust aromatic content in the fuel to match fuel specification requirements.
摘要翻译: 煤的等离子体辅助处理方法,其中煤直接转化为重质烃。 该方法的第一步是在轻烃(如天然气)存在下,在等离子体条件下将煤直接转化成脂肪烃。 在第二工艺步骤中,将脂族烃升级成液体燃料。 该过程的能量可以通过由可再生能源供电的射频能量(例如微波能量)来提供。 该方法具有调节燃料中芳烃含量的灵活性,以符合燃料规格要求。
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