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公开(公告)号:US07737312B2
公开(公告)日:2010-06-15
申请号:US10549768
申请日:2004-03-10
申请人: Ivan Greager , Jan Hendrik Scholtz , Johan Pieter de Wet , Mieke Ann Desmet , Wilhelmina Jansen , Paul Jacobson , Luis Pablo Fidel Dancuart
发明人: Ivan Greager , Jan Hendrik Scholtz , Johan Pieter de Wet , Mieke Ann Desmet , Wilhelmina Jansen , Paul Jacobson , Luis Pablo Fidel Dancuart
IPC分类号: C07C2/68
CPC分类号: C07C2/66 , C07C7/04 , C07C7/10 , C10G2/32 , C10G29/205 , C10G2300/1022 , C10G2300/1096 , C10G2300/301 , C10G2300/4081 , C10G2300/44 , C10G2400/10 , C10G2400/30
摘要: This invention relates to a process for producing linear alkyl benzene, the process including the steps of obtaining a hydrocarbon condensate containing olefins, paraffins and oxygenates from a low temperature Fischer-Tropsch reaction; a) fractionating a desired carbon number distribution from the hydrocarbon condensate to form a fractionated hydrocarbon condensate stream; b) extracting oxygenates from the fractionated hydrocarbon condensate stream from step (a) to form a stream containing olefins and paraffins; c) combining the stream containing olefins and paraffins from step (b) with the feed stream from step (g) to form a combined stream; d) alkylating olefins in the combined stream from step (c) with benzene in the presence of a suitable alkylation catalyst in an alkylation reactor; e) recovering linear alkyl benzene from the alkylation reactor; f) recovering unreacted paraffins from the alkylation reactor; g) dehydrogenating the unreacted paraffins in the presence of a suitable dehydrogenation catalyst to form a feed stream containing olefins and paraffins; and h) sending the feed stream containing olefins and paraffins from step (g) to step (c).
摘要翻译: 本发明涉及一种直链烷基苯的制备方法,该方法包括以下步骤:从低温费 - 托反应获得含有烯烃,链烷烃和含氧化合物的烃缩合物; a)从烃缩合物中分馏所需的碳数分布以形成分馏的烃冷凝物流; b)从步骤(a)的分馏的烃冷凝物流中提取含氧化合物以形成含有烯烃和链烷烃的物流; c)将来自步骤(b)的含有烯烃和链烷烃的料流与来自步骤(g)的进料流混合以形成组合料流; d)在烷基化反应器中,在合适的烷基化催化剂存在下,将来自步骤(c)的合并物流中的烯烃与苯烷基化; e)从烷基化反应器回收直链烷基苯; f)从烷基化反应器回收未反应的链烷烃; g)在合适的脱氢催化剂存在下使未反应的链烷烃脱氢以形成含有烯烃和链烷烃的进料流; 和h)将来自步骤(g)的含有烯烃和链烷烃的进料流送至步骤(c)。
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公开(公告)号:US07153432B2
公开(公告)日:2006-12-26
申请号:US11015308
申请日:2004-12-16
申请人: Luis Pablo Fidel Dancuart Kohler , Gert Hendrik Du Plessis , Francois Jacobus Du Toit , Edward Ludovicus Koper , Trevor David Phillips , Janette Van Der Walt
发明人: Luis Pablo Fidel Dancuart Kohler , Gert Hendrik Du Plessis , Francois Jacobus Du Toit , Edward Ludovicus Koper , Trevor David Phillips , Janette Van Der Walt
CPC分类号: B01D61/04 , B01D61/025 , B01D61/145 , B01D61/147 , B01D61/16 , B01D61/362 , B01D61/364 , B01D61/58 , B01D2311/04 , C02F1/04 , C02F1/26 , C02F1/44 , C02F1/441 , C02F1/444 , C02F1/447 , C02F1/448 , C02F9/00 , B01D2311/12
摘要: A process for the production of highly purified water 38 from Fischer-Tropsch reaction water 12, includes at least the steps of a primary treatment stage comprising an equilibrium staged separation process 14 having at least one stage for removing at least a fraction of non-acid oxygenated hydrocarbons from the Fischer-Tropsch reaction water 12 to produce a primary water-enriched stream 16, a secondary treatment stage comprising at least one membrane separation process 28 for removing at least some suspended solids and acidic oxygenated hydrocarbons from at least a portion of the primary water-enriched stream 16 to produce a secondary water-enriched stream 34 and a tertiary treatment stage comprising a dissolved salt and organic removal stage 36 for removing at least some dissolved salts and organic constituents from at least a portion of the secondary water-enriched stream 34.
摘要翻译: 用于从费 - 托反应水12生产高纯度水38的方法包括至少包括平衡分级分离方法14的初级处理阶段的步骤14,其具有至少一个阶段,用于除去至少一部分非酸 来自费 - 托反应水12的氧化烃,以产生初级富水流16,二次处理阶段包括至少一个膜分离工艺28,用于从至少一部分的该部分去除至少一些悬浮固体和酸性氧化烃 初级富水流16以产生第二富水流34和第三处理阶段,其包括溶解的盐和有机去除阶段36,用于从至少一部分第二富水流中除去至少一些溶解的盐和有机成分 流34。
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公开(公告)号:US08075761B2
公开(公告)日:2011-12-13
申请号:US11280508
申请日:2005-11-15
IPC分类号: C10L1/08
CPC分类号: C10L1/08 , Y10S208/95
摘要: The invention provides a hydrocarbon composition for use in CI engines, said composition comprising a blend of hydrocarbons derived from a LTFT and from a HTFT process, said LTFT derived hydrocarbon being blended with said HTFT derived hydrocarbon in a volumetric ratio of from 1:20 to 20:1. The invention further provides a process for the production of the hydrocarbon composition and a the fuel composition including, in addition to the hydrocarbon composition, one or more component selected from the group including a crude oil derived diesel fuel, a crude oil derived naphtha, a lubricant or light cycle oil (LCO).
摘要翻译: 本发明提供用于CI发动机的烃组合物,所述组合物包含衍生自LTFT和HTFT方法的烃的共混物,所述LTFT衍生的烃与所述HTFT衍生的烃以1:20至 20:1。 本发明还提供一种生产该烃组合物的方法和一种燃料组合物,该组合物除烃组合物外还包含一种或多种选自以下的组分:原油衍生的柴油,原油衍生的石脑油, 润滑剂或轻质循环油(LCO)。
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公开(公告)号:US07166219B2
公开(公告)日:2007-01-23
申请号:US11015654
申请日:2004-12-16
申请人: Luis Pablo Fidel Dancuart Kohler , Gert Hendrik Du Plessis , Francois Jacobus Du Toit , Edward Ludovicus Koper , Trevor David Phillips , Janette Van Der Walt
发明人: Luis Pablo Fidel Dancuart Kohler , Gert Hendrik Du Plessis , Francois Jacobus Du Toit , Edward Ludovicus Koper , Trevor David Phillips , Janette Van Der Walt
IPC分类号: C02F3/00
CPC分类号: C02F9/00 , C02F1/04 , C02F1/26 , C02F3/00 , C02F2101/32 , C02F2101/34
摘要: A process for the production of highly purified water 44 from Fischer-Tropsch reaction water 12 includes distillation 14 as a primary treatment stage, biological treatment including anaerobic digestion 20 and aerobic digestion 22 as a secondary treatment stage, solid-liquid separation 32 as a tertiary treatment stage and a dissolved salt and organic removal stage 40 as final treatment stage.
摘要翻译: 从费 - 托反应水12生产高纯度水44的方法包括作为主要处理阶段的蒸馏14,包括厌氧消化20和需氧消化22作为二级处理阶段的生物处理,固液分离32作为第三级 处理阶段和溶解盐和有机物去除阶段40作为最终处理阶段。
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