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1.发明申请公开(公告)号：US20090074643A1
公开(公告)日：2009-03-19
申请号：US12298869
申请日：2007-04-18
CPC分类号： B01J23/50 , B01D53/8671 , B01D53/8681 , B01D2255/1023 , B01D2255/104 , B01D2255/106 , B01D2255/206 , B01D2255/20761 , B01D2255/20769 , B01D2257/408 , B01D2257/70 , B01J23/44 , B01J23/63 , B01J23/6525 , B01J23/66 , B01J35/04 , C01B3/58 , C10K1/34
摘要： A process for the catalytic removal of hydrogen cyanide, formic acid and formic acid derivatives from synthesis gas comprising these compounds, carbon monoxide and hydrogen, the process comprising contacting the synthesis gas with a catalyst comprising one or more metals selected from the group consisting of silver, gold, copper, palladium, platinum and their mixtures and supported on a carrier comprising at least one of the oxides of scandium, yttrium, lanthanum, cerium, titanium, zirconium, aluminium, zinc, chromium and molybdenum.
摘要翻译： 一种从包含这些化合物，一氧化碳和氢气的合成气中催化除去氰化氢，甲酸和甲酸衍生物的方法，该方法包括使合成气与包含一种或多种选自银 ，金，铜，钯，铂及其混合物，并负载在包含钪，钇，镧，铈，钛，锆，铝，锌，铬和钼的至少一种氧化物的载体上。
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2.发明授权公开(公告)号：US08623303B2
公开(公告)日：2014-01-07
申请号：US12298869
申请日：2007-04-18
IPC分类号： B01D53/86
CPC分类号： B01J23/50 , B01D53/8671 , B01D53/8681 , B01D2255/1023 , B01D2255/104 , B01D2255/106 , B01D2255/206 , B01D2255/20761 , B01D2255/20769 , B01D2257/408 , B01D2257/70 , B01J23/44 , B01J23/63 , B01J23/6525 , B01J23/66 , B01J35/04 , C01B3/58 , C10K1/34
摘要： A process for the catalytic removal of hydrogen cyanide, formic acid and formic acid derivatives from synthesis gas comprising these compounds, carbon monoxide and hydrogen, the process comprising contacting the synthesis gas with a catalyst comprising one or more metals selected from the group consisting of silver, gold, copper, palladium, platinum and their mixtures and supported on a carrier comprising at least one of the oxides of scandium, yttrium, lanthanum, cerium, titanium, zirconium, aluminum, zinc, chromium and molybdenum.
摘要翻译： 一种从包含这些化合物，一氧化碳和氢气的合成气中催化除去氰化氢，甲酸和甲酸衍生物的方法，该方法包括使合成气与包含一种或多种选自银 ，金，铜，钯，铂及其混合物，并负载在包含钪，钇，镧，铈，钛，锆，铝，锌，铬和钼的至少一种氧化物的载体上。
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公开(公告)号：US07820867B2
公开(公告)日：2010-10-26
申请号：US12063021
申请日：2006-08-16
申请人： Finn Joensen , Bodil Voss , Jesper Nerlov
发明人： Finn Joensen , Bodil Voss , Jesper Nerlov
CPC分类号： C07C29/151 , C10G3/00 , C10G3/49 , C10G2300/1022 , C10G2300/4081 , C10G2400/02 , C10L1/06 , Y02P30/20 , C07C31/04
摘要： Process for converting oxygenate compounds to hydrocarbons comprising the steps: (a) introducing a feed stream of synthesis gas to a synthesis section for the production of easily convertible oxygenates, (b) passing the effluent stream from said synthesis section containing easily convertible oxygenates to a gasoline synthesis section, (c) passing the effluent of said gasoline synthesis section to a separator and withdrawing from said separator hydrocarbons boiling in the gasoline boiling range, (d) admixing a recycle stream from the separator containing unconverted synthesis gas volatile hydrocarbons with the feed stream of synthesis gas of step (a), (e) introducing a feed containing difficulty convertible oxygenates to the synthesis section of step (a).
摘要翻译： 将含氧化合物转化为烃的方法，包括以下步骤：（a）将合成气的进料流引入合成段，以生产容易转化的含氧化合物，（b）将含有易转化含氧化合物的合成段的流出物流送至 汽油合成段，（c）将所述汽油合成段的流出物通入分离器并从汽油沸程沸腾的所述分离器中取出，（d）将含有未转化的合成气挥发性烃的分离器的再循环流与进料混合 步骤（a）的合成气流，（e）将含有难以转化的含氧化合物的进料引入步骤（a）的合成部分。
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4.发明申请公开(公告)号：US20080228021A1
公开(公告)日：2008-09-18
申请号：US12063021
申请日：2006-08-16
申请人： Finn Joensen , Bodil Voss , Jesper Nerlov
发明人： Finn Joensen , Bodil Voss , Jesper Nerlov
IPC分类号： C07C1/00
CPC分类号： C07C29/151 , C10G3/00 , C10G3/49 , C10G2300/1022 , C10G2300/4081 , C10G2400/02 , C10L1/06 , Y02P30/20 , C07C31/04
摘要： Process for converting oxygenate compounds to hydrocarbons comprising the steps: (a) introducing a feed stream of synthesis gas to a synthesis section for the production of easily convertible oxygenates, (b) passing the effluent stream from said synthesis section containing easily convertible oxygenates to a gasoline synthesis section, (c) passing the effluent of said gasoline synthesis section to a separator and withdrawing from said separator hydrocarbons boiling in the gasoline boiling range, (d) admixing a recycle stream from the separator containing unconverted synthesis gas volatile hydrocarbons with the feed stream of synthesis gas of step (a), (e) introducing a feed containing difficulty convertible oxygenates to the synthesis section of step (a).
摘要翻译： 将含氧化合物转化为烃的方法，包括以下步骤：（a）将合成气的进料流引入合成段，以生产容易转化的含氧化合物，（b）将含有易转化含氧化合物的合成段的流出物流送至 汽油合成段，（c）将所述汽油合成段的流出物通入分离器并从汽油沸程沸腾的所述分离器中取出，（d）将含有未转化的合成气挥发性烃的分离器的再循环流与进料混合 步骤（a）的合成气流，（e）将含有难以转化的含氧化合物的进料引入步骤（a）的合成部分。
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