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公开(公告)号:US20050139555A1
公开(公告)日:2005-06-30
申请号:US11015308
申请日:2004-12-17
申请人: Luis Pablo Dancuart Kohler , Gert Plessis , Francois Toit , Edward Koper , Trevor Phillips , Janette Walt
发明人: Luis Pablo Dancuart Kohler , Gert Plessis , Francois Toit , Edward Koper , Trevor Phillips , Janette Walt
IPC分类号: B01D61/04 , B01D61/16 , B01D61/58 , C02F1/04 , C02F1/26 , C02F1/44 , C02F9/00 , C02F9/02 , C02F101/32 , C02F101/34 , B01D37/00 , C07C27/26
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:US20050131086A1
公开(公告)日:2005-06-16
申请号:US11015654
申请日:2004-12-16
申请人: Luis Dancuart Kohler , Gert Plessis , Francois Toit , Edward Koper , Trevor Phillips , Janette Walt
发明人: Luis Dancuart Kohler , Gert Plessis , Francois Toit , Edward Koper , Trevor Phillips , Janette Walt
IPC分类号: C02F3/04 , B01D3/14 , B01D11/04 , B01D61/14 , C02F1/04 , C02F1/20 , C02F1/26 , C02F1/32 , C02F3/00 , C02F3/08 , C02F3/12 , C02F9/00 , C02F9/02 , C02F9/14 , C07C27/26
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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公开(公告)号:US20050131085A1
公开(公告)日:2005-06-16
申请号:US11014518
申请日:2004-12-16
申请人: Luis Kohler , Gert Plessis , Francois Toit , Edward Koper , Trevor Phillips , Janette Walt
发明人: Luis Kohler , Gert Plessis , Francois Toit , Edward Koper , Trevor Phillips , Janette Walt
IPC分类号: C02F3/08 , B01D3/14 , C02F1/04 , C02F1/20 , C02F1/24 , C02F1/26 , C02F1/28 , C02F1/32 , C02F1/38 , C02F1/40 , C02F1/42 , C02F1/44 , C02F1/52 , C02F1/66 , C02F1/72 , C02F3/02 , C02F3/04 , C02F3/06 , C02F3/12 , C02F9/00 , C07C27/26
CPC分类号: C02F1/045 , B01D3/148 , C02F1/001 , C02F1/04 , C02F1/048 , C02F1/20 , C02F1/24 , C02F1/26 , C02F1/28 , C02F1/283 , C02F1/32 , C02F1/38 , C02F1/385 , C02F1/40 , C02F1/42 , C02F1/44 , C02F1/441 , C02F1/444 , C02F1/52 , C02F1/66 , C02F1/72 , C02F3/02 , C02F3/04 , C02F3/06 , C02F3/08 , C02F3/12 , C02F9/00 , C02F2103/04 , C02F2103/36 , C02F2103/365 , C02F2303/08 , C02F2305/06 , Y02W10/15
摘要: A process for the production of highly purified water from Fischer-Tropsch reaction water includes distillation as a primary treatment stage, evaporation as a secondary treatment stage, aerobic treatment as a tertiary treatment stage, solid-liquid separation as a quartic treatment stage, and membrane separation as a final treatment stage.
摘要翻译: 从费 - 托反应水生产高纯水的方法包括蒸馏作为主要处理阶段,蒸发作为二次处理阶段,好氧处理作为第三处理阶段,固液分离作为四分之一处理阶段,以及膜 分离为最终治疗阶段。
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