Adsorption of dibenzothiophenes from hydrocarbon and model diesel feeds
    24.
    发明授权
    Adsorption of dibenzothiophenes from hydrocarbon and model diesel feeds 有权
    从碳氢化合物和模型柴油饲料吸附二苯并噻吩

    公开(公告)号:US08142647B2

    公开(公告)日:2012-03-27

    申请号:US12336199

    申请日:2008-12-16

    IPC分类号: C10G25/06

    摘要: A process for adsorbing aromatic sulfur compounds, where an adsorbent is contacted with a C6-C20 aromatic and/or aliphatic stream which comprises a solution of (i) at least one benzothiophene compound, (ii) a solvent which comprises at least one C6-C16 aliphatic compound, and (iii) optionally at least one C6-C12 aromatic compound. In this process, the adsorbent is regenerated using an organic regenerant such as, but not limited to, toluene. Also disclosed is another process for adsorbing aromatic sulfur compounds. In this process, an adsorbent is contacted with a mixture comprising a model diesel feed comprising at least one benzothiophene compound. In this process, the adsorbent is regenerated using an organic regenerant such as, but not limited to, toluene.

    摘要翻译: 一种吸附芳族硫化合物的方法,其中吸附剂与C 6 -C 20芳族和/或脂族物流接触,其包含(i)至少一种苯并噻吩化合物的溶液,(ii)包含至少一种C6- C16脂族化合物,和(iii)任选的至少一种C 6 -C 12芳族化合物。 在该方法中,使用有机再生剂例如但不限于甲苯来再生吸附剂。 还公开了另一种吸附芳族硫化合物的方法。 在该方法中,将吸附剂与包含至少一种苯并噻吩化合物的模型柴油进料的混合物接触。 在该方法中,使用有机再生剂例如但不限于甲苯来再生吸附剂。

    ADSORPTION OF DIBENZOTHIOPHENES FROM HYDROCARBON AND MODEL DIESEL FEEDS
    25.
    发明申请
    ADSORPTION OF DIBENZOTHIOPHENES FROM HYDROCARBON AND MODEL DIESEL FEEDS 有权
    从碳氢化合物和柴油进料中吸收二苯并噻吩

    公开(公告)号:US20100147748A1

    公开(公告)日:2010-06-17

    申请号:US12336199

    申请日:2008-12-16

    IPC分类号: C10G17/02

    摘要: A process for adsorbing aromatic sulfur compounds, where an adsorbent is contacted with a C6-C20 aromatic and/or aliphatic stream which comprises a solution of (i) at least one benzothiophene compound, (ii) a solvent which comprises at least one C6-C16 aliphatic compound, and (iii) optionally at least one C6-C12 aromatic compound. In this process, the adsorbent is regenerated using an organic regenerant such as, but not limited to, toluene. Also disclosed is another process for adsorbing aromatic sulfur compounds. In this process, an adsorbent is contacted with a mixture comprising a model diesel feed comprising at least one benzothiophene compound. In this process, the adsorbent is regenerated using an organic regenerant such as, but not limited to, toluene.

    摘要翻译: 一种吸附芳族硫化合物的方法,其中吸附剂与C 6 -C 20芳族和/或脂族物流接触,其包含(i)至少一种苯并噻吩化合物的溶液,(ii)包含至少一种C6- C16脂族化合物,和(iii)任选的至少一种C 6 -C 12芳族化合物。 在该方法中,使用有机再生剂例如但不限于甲苯来再生吸附剂。 还公开了另一种吸附芳族硫化合物的方法。 在该方法中,将吸附剂与包含至少一种苯并噻吩化合物的模型柴油进料的混合物接触。 在该方法中,使用有机再生剂例如但不限于甲苯来再生吸附剂。

    Process and system for producing synthetic crude oil from offshore produced fluids containing high CO2 content
    29.
    发明授权
    Process and system for producing synthetic crude oil from offshore produced fluids containing high CO2 content 有权
    从含有高二氧化碳含量的海洋生产液中生产合成原油的工艺和制度

    公开(公告)号:US09162208B2

    公开(公告)日:2015-10-20

    申请号:US13644328

    申请日:2012-10-04

    IPC分类号: B01J12/00 C10G2/00 C10G5/00

    CPC分类号: B01J12/00 C10G2/32 C10G2/50

    摘要: A system and process for producing synthetic crude oil from produced fluids of an oil well is disclosed. The system comprises a separation plant for producing an associated gas stream from produced fluids a membrane unit comprising a plurality of polymer membranes to provide a CO2 enriched permeate stream and a CO2 depleted product gas stream, a gas conversion plant for converting the CO2 depleted product gas stream into a synthetic crude oil and a heat exchanger adding heat to the associated gas stream so that the membrane unit operates at a temperature of at least 80° C. during separation of the associated gas stream using the membrane unit. A process using the aforementioned components, including separation of the associated gas stream using the membrane unit at a temperature >80° C., into a CO2 enriched stream and a CO2 depleted product stream, is also described.

    摘要翻译: 公开了一种从油井的生产流体生产合成原油的系统和方法。 该系统包括用于从产生的流体产生相关气流的分离装置,包括多个聚合物膜的膜单元,以提供富含CO 2的渗透物流和CO 2贫化产物气流,用于转化CO 2贫化产物气体的气体转化装置 流入合成原油和向相关气流加热的热交换器,使得膜单元在使用膜单元分离相关气流期间在至少80℃的温度下操作。 还描述了使用上述组分的方法,包括将温度> 80℃下使用膜单元的相关气流分离成富CO 2流和二氧化碳贫化产物流。