Process for the purification of an aqueous stream coming from the Fischer-Tropsch reaction
    1.
    发明授权
    Process for the purification of an aqueous stream coming from the Fischer-Tropsch reaction 有权
    用于净化来自费 - 托反应的水流的方法

    公开(公告)号:US09296628B2

    公开(公告)日:2016-03-29

    申请号:US13318498

    申请日:2010-04-22

    摘要: Process for the purification of an aqueous stream coming from the Fischer-Tropsch reaction which comprises feeding said aqueous stream to one or more pervaporation units obtaining an aqueous stream enriched in oxygenated organic compounds (retentate side) and an aqueous stream enriched in water (permeate side), feeding said aqueous stream enriched in oxygenated organic compounds to a saturator obtaining a gaseous stream leaving the saturator, feeding said gaseous stream to a synthesis gas production plant. Said process allows at least a part of the aqueous stream coming from the Fischer-Tropsch reaction to be used as process water in a synthesis gas production plant, subsequently sent to a Fischer-Tropsch plant for the production of hydrocarbons.

    摘要翻译: 净化来自费 - 托反应的含水物流的方法,其包括将所述水流加入到一个或多个渗透蒸发单元中,获得富含氧化有机化合物(滞留物侧)的水流和富含水的水流(渗透侧 ),将富含氧化的有机化合物的所述水流进料到饱和器,获得离开饱和器的气流,将所述气流进料到合成气生产设备。 所述方法允许来自费 - 托反应的至少一部分水流作为合成气生产设备中的工艺用水,随后送至费 - 托工厂用于生产碳氢化合物。

    PROCESS FOR THE PURIFICATION OF AN AQUEOUS STREAM COMING FROM THE FISCHER-TROPSCH REACTION
    4.
    发明申请
    PROCESS FOR THE PURIFICATION OF AN AQUEOUS STREAM COMING FROM THE FISCHER-TROPSCH REACTION 有权
    从FISCHER-TROPSCH反应中净化水质流的方法

    公开(公告)号:US20120055868A1

    公开(公告)日:2012-03-08

    申请号:US13254621

    申请日:2010-02-18

    IPC分类号: C02F9/14 C02F101/30

    摘要: Process for the purification of an aqueous stream coming from the Fischer-Tropsch reaction which comprises: —feeding said aqueous stream containing the organic by-products of the reaction to a distillation column, obtaining two output streams: —an aqueous stream (i) exiting from the column head, enriched with alcohols having from 1 to 20 carbon atoms, preferably from 1 to 9 carbon atoms, and other optional volatile compounds; an aqueous stream (ii) exiting from the column bottom, enriched with organic acids having from 1 to 10 carbon atoms, preferably from 2 to 6 carbon atoms; —subjecting said aqueous stream (ii) to an anaerobic biological treatment obtaining a purified aqueous stream (iii); wherein said anaerobic biological treatment is carried out with a hydraulic retention time lower than 15 hours, preferably ranging from 4 hours to 10 hours, more preferably ranging from 5 hours to 8 hours.

    摘要翻译: 净化来自费 - 托反应的水流的方法,其包括:将含有反应的有机副产物的所述含水物流送入蒸馏塔,获得两个输出流: - 在水流(i) 富集具有1至20个碳原子,优选1至9个碳原子的醇和其它任选的挥发性化合物; 从塔底出来的含水物流(ii)富含具有1-10个碳原子,优选2-6个碳原子的有机酸; - 将所述含水物流(ii)进行厌氧生物处理,得到纯化的含水物流(iii); 其中所述厌氧生物处理水力停留时间低于15小时,优选4小时至10小时,更优选5小时至8小时进行。

    PROCESS FOR THE TREATMENT OF THE AQUEOUS STREAM COMING FROM THE FISCHER-TROPSCH REACTION BY MEANS OF ION EXCHANGE RESINS
    5.
    发明申请
    PROCESS FOR THE TREATMENT OF THE AQUEOUS STREAM COMING FROM THE FISCHER-TROPSCH REACTION BY MEANS OF ION EXCHANGE RESINS 有权
    通过离子交换树脂从FISCHER-TROPSCH反应处理水质流的处理方法

    公开(公告)号:US20110147313A1

    公开(公告)日:2011-06-23

    申请号:US12996464

    申请日:2009-05-28

    IPC分类号: B01J39/00

    摘要: Process for the treatment of the aqueous stream coming from the Fischer-Tropsch reaction comprising: feeding the aqueous stream containing the organic by products of the reaction to a distillation or stripping column; separation from the column of an aqueous stream enriched in alcohols having from 1 to 8 carbon atoms and other possible volatile compounds; feeding the aqueous stream containing the organic acids leaving the bottom of the distillation column to an ion exchange step wherein said aqueous stream is put in contact with an anionic exchange resin bed and the production of two outgoing aqueous streams: an aqueous stream (i) enriched in organic acids having from 1 to 8 carbon atoms; a purified aqueous stream (ii) with a low content of organic acids.

    摘要翻译: 用于处理来自费 - 托反应的水流的方法,包括:将含有反应产物的含水反应产物的水流送入蒸馏塔或汽提塔; 与富含1至8个碳原子的醇的水流柱和其它可能的挥发性化合物分离; 将含有离开蒸馏塔底部的有机酸的含水物流送入离子交换步骤,其中所述含水物流与阴离子交换树脂床接触并产生两个输出的含水物流:含水物流(i)富集 在具有1至8个碳原子的有机酸中; 具有低含量有机酸的纯化水流(ⅱ)。

    PROCESS FOR THE TREATMENT OF THE AQUEOUS STREAM COMING FROM THE FISCHER-TROPSCH REACTION
    6.
    发明申请
    PROCESS FOR THE TREATMENT OF THE AQUEOUS STREAM COMING FROM THE FISCHER-TROPSCH REACTION 审中-公开
    从FISCHER-TROPSCH反应处理水质流的处理方法

    公开(公告)号:US20110127155A1

    公开(公告)日:2011-06-02

    申请号:US12863101

    申请日:2009-01-14

    IPC分类号: C02F9/08

    摘要: The present invention relates to a process for the treatment of the aqueous stream coming from the Fischer-Tropsch reaction, comprising: —feeding the aqueous stream (1) containing organic by-products of the reaction to a distillation or stripping column (10); —collection from the column of a distillate (2) enriched in alcohols having from 1 to 8 carbon atoms and other possible volatile compounds—feeding the aqueous stream leaving the bottom of the column (3) to a reverse osmosis unit (20) and the production of two outgoing streams; —an aqueous stream (4) enriched in organic acids with from 1 to 8 carbon atoms; —a partially purified aqueous stream (5) with a low acid content.

    摘要翻译: 本发明涉及处理来自费 - 托反应的含水物流的方法,包括:将含有反应有机副产物的含水物流(1)送入蒸馏塔或汽提塔(10); - 富集具有1至8个碳原子的醇的馏出物(2)的柱和其它可能的挥发性化合物 - 将离开塔(3)的底部的水流送入反渗透单元(20),和 生产两个输出流; - 含有1至8个碳原子的有机酸的含水物流(4); - 具有低酸含量的部分纯化的水流(5)。

    Process for the skeleton isomerization of linear olefins
    9.
    发明授权
    Process for the skeleton isomerization of linear olefins 失效
    线性烯烃骨架异构化方法

    公开(公告)号:US5600054A

    公开(公告)日:1997-02-04

    申请号:US381062

    申请日:1995-01-31

    IPC分类号: B01J21/02 C07C5/27

    CPC分类号: B01J21/02 C07C5/277

    摘要: Process for the skeleton isomerization of linear olefins, preferably n-butenes or n-pentenes, which consists in putting said olefins in contact with a catalyst comprising alumina on whose surface boron oxide is deposited in a quantity which is lower than 2.1.times.10.sup.-4 g/m.sup.2 of the surface of the alumina.

    摘要翻译: 线性烯烃,优选正丁烯或正戊烯骨架异构化的方法,其包括将所述烯烃与包含氧化铝的催化剂接触,所述催化剂在其表面上沉积氧化硼,其量低于2.1×10 -4 g / m2的氧化铝表面。