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公开(公告)号：US20190168417A1
公开(公告)日：2019-06-06
申请号：US15828839
申请日：2017-12-01
发明人： Bandar Fadhel , Ahmad D. Hammad , Issam T. Amr , Rami A. Bamagain
CPC分类号： B28C5/42 , B01D53/02 , B01D53/1475 , B01D53/62 , B01D2251/604 , B01D2251/606 , B01D2252/102 , B01D2252/204 , B01D2253/102 , B01D2253/108 , B01D2253/204 , B01D2257/504 , B28C5/4203 , B28C5/46 , B28C7/0046 , B28C7/04 , C04B28/10 , C04B40/0231
摘要： A vehicle CO2 capture and utilization system includes a concrete mixer vehicle and a vehicle exhaust capture system. The concrete mixer vehicle comprises a vehicle exhaust and a mixer tank. The vehicle exhaust capture system is located onboard the concrete mixer vehicle. Additionally, the vehicle exhaust capture system includes one or more fluid pathways that fluidly couple the vehicle exhaust and the mixer tank.
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12.发明申请公开(公告)号：US20150166902A1
公开(公告)日：2015-06-18
申请号：US14617358
申请日：2015-02-09
CPC分类号： C10G21/28 , B01D11/0403 , B01J3/008 , C07C7/10 , C07D207/00 , C10G21/08 , C10G2300/202 , C10G2300/205 , C10G2300/44
摘要： Methods for recovering organic heteroatom compounds from a hydrocarbon feedstock include feeding into a contactor a hydrocarbon feedstock and an aqueous solvent to form an extraction mixture of the aqueous solvent with the hydrocarbon feedstock. The hydrocarbon feedstock includes a hydrocarbon and an organic heteroatom compound. The aqueous solvent includes an ionic liquid formed from pressurized carbon dioxide and water. A pressure and temperature of the extraction mixture may be established that together tune the aqueous solvent to selectively form a solvent complex with the at least one organic heteroatom compound. Then, the solvent complex is extracted to a recovery vessel from the extraction mixture in the contactor. By adjustment of a recovery temperature of the recovery vessel, a recovery pressure of the recovery vessel, or both, the solvent complex decomposes into carbon dioxide and the organic heteroatom compound. The organic heteroatom compound is then recovered from the recovery vessel.
摘要翻译： 从烃原料中回收有机杂原子化合物的方法包括将烃原料和含水溶剂进料到接触器中以形成含水溶剂与烃原料的萃取混合物。 烃原料包括烃和有机杂原子化合物。 含水溶剂包括由加压二氧化碳和水形成的离子液体。 可以建立萃取混合物的压力和温度，其一起调节水性溶剂以选择性地与至少一种有机杂原子化合物形成溶剂配合物。 然后，将溶剂配合物从接触器中的萃取混合物中提取回收容器。 通过调节回收容器的回收温度，回收容器的回收压力或二者，溶剂配合物分解成二氧化碳和有机杂原子化合物。 然后从回收容器中回收有机杂原子化合物。
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公开(公告)号：US11001549B1
公开(公告)日：2021-05-11
申请号：US16786858
申请日：2020-02-10
IPC分类号： C07C51/15 , C25B3/25 , C25B13/04 , C25B15/02 , C25B1/04 , C25B3/23 , C25B1/02 , C25B3/26 , C25B9/19 , C25B9/73
摘要： A system and method with a solid oxide electrolysis cell (SOEC), including feeding carbon dioxide and an olefin to the SOEC and discharging carbon monoxide and an olefin oxide from the SOEC, wherein the olefin oxide corresponds to the olefin.
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公开(公告)号：US10913179B2
公开(公告)日：2021-02-09
申请号：US16877791
申请日：2020-05-19
发明人： Bandar Fadhel , Ahmad D. Hammad , Issam T. Amr , Rami A. Bamagain
IPC分类号： C04B28/06 , B28C5/42 , C04B28/10 , B28C5/46 , B01D53/02 , B01D53/14 , B01D53/62 , B28C7/00 , B28C7/04 , C04B40/02 , C04B7/00 , C04B7/34 , C04B28/00 , C04B32/00 , C04B7/32 , C04B7/36 , C04B11/28
摘要： A vehicle CO2 capture and utilization system includes a concrete mixer vehicle and a vehicle exhaust capture system. The concrete mixer vehicle comprises a vehicle exhaust and a mixer tank. The vehicle exhaust capture system is located onboard the concrete mixer vehicle. Additionally, the vehicle exhaust capture system includes one or more fluid pathways that fluidly couple the vehicle exhaust and the mixer tank.
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15.发明授权Demulsification of emulsified petroleum using carbon dioxide and resin supplement without precipitation of asphaltenes 有权使用二氧化碳和树脂补充剂乳化石油，而不会沥青沥青沉淀公开(公告)号：US09169446B2
公开(公告)日：2015-10-27
申请号：US14143711
申请日：2013-12-30
发明人： Zaki Yusuf , Bandar Fadhel
摘要： Methods for demulsifying an emulsified petroleum source having a predetermined resin-to-asphaltene ratio without substantial aggregation or precipitation of asphaltenes may include adding a resin supplement to the emulsified petroleum source to form a resin-supplemented emulsion having a resin-to-asphaltene ratio above a predetermined critical value. An acidic-to-basic ratio of acidic functional groups to basic functional groups in the supplemented emulsion may be adjusted to be from about 0.25 to about 4.0. The resin-supplemented emulsion may be contacted with carbon dioxide to form an initial mixture having an emulsified oil phase and an emulsified aqueous phase. The initial mixture may be stabilized to facilitate rupture of the resin-supplemented emulsion, to cause phase separation, and to allow removal of a separated oil phase. The resin-to-asphaltene ratio being above the predetermined critical value in the supplemented emulsion maintains asphaltene suspension during demulsification, such that asphaltene agglomeration and precipitation are avoided.
摘要翻译： 将具有预定树脂与沥青质比例的乳化石油源破乳的方法不会沥青质基本上聚集或沉淀，可包括向乳化石油源中加入树脂补充剂以形成树脂与沥青质比例高于 一个预定的临界值。 补充乳液中酸性官能团与碱性官能团的酸碱比可以调节至约0.25至约4.0。 补充树脂的乳液可与二氧化碳接触以形成具有乳化油相和乳化水相的初始混合物。 初始混合物可以被稳定以促进补充树脂的乳液的破裂，引起相分离，并允许除去分离的油相。 在补充的乳液中树脂与沥青质的比值高于预定的临界值，在破乳过程中保持沥青质悬浮液，从而避免沥青质聚集和沉淀。
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16.发明申请DEMULSIFICATION OF EMULSIFIED PETROLEUM USING CARBON DIOXIDE AND RESIN SUPPLEMENT WITHOUT PRECIPITATION OF ASPHALTENES 有权使用二氧化碳和树脂补充剂在不使沥青降解的情况下进行模拟的石油化学公开(公告)号：US20150184085A1
公开(公告)日：2015-07-02
申请号：US14143711
申请日：2013-12-30
发明人： Zaki Yusuf , Bandar Fadhel
IPC分类号： C10G33/08
摘要： Methods for demulsifying an emulsified petroleum source having a predetermined resin-to-asphaltene ratio without substantial aggregation or precipitation of asphaltenes may include adding a resin supplement to the emulsified petroleum source to form a resin-supplemented emulsion having a resin-to-asphaltene ratio above a predetermined critical value. An acidic-to-basic ratio of acidic functional groups to basic functional groups in the supplemented emulsion may be adjusted to be from about 0.25 to about 4.0. The resin-supplemented emulsion may be contacted with carbon dioxide to form an initial mixture having an emulsified oil phase and an emulsified aqueous phase. The initial mixture may be stabilized to facilitate rupture of the resin-supplemented emulsion, to cause phase separation, and to allow removal of a separated oil phase. The resin-to-asphaltene ratio being above the predetermined critical value in the supplemented emulsion maintains asphaltene suspension during demulsification, such that asphaltene agglomeration and precipitation are avoided.
摘要翻译： 将具有预定树脂与沥青质比例的乳化石油源破乳的方法不会沥青质基本上聚集或沉淀，可包括向乳化石油源中加入树脂补充剂以形成树脂与沥青质比例高于 一个预定的临界值。 补充乳液中酸性官能团与碱性官能团的酸碱比可以调节至约0.25至约4.0。 补充树脂的乳液可与二氧化碳接触以形成具有乳化油相和乳化水相的初始混合物。 初始混合物可以被稳定以促进补充树脂的乳液的破裂，引起相分离，并允许除去分离的油相。 在补充的乳液中树脂与沥青质的比值高于预定的临界值，在破乳过程中保持沥青质悬浮液，从而避免沥青质聚集和沉淀。
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17.发明授权Methods for recovering organic heteroatom compounds from hydrocarbon feedstocks 有权从烃原料中回收有机杂原子化合物的方法公开(公告)号：US08961780B1
公开(公告)日：2015-02-24
申请号：US14107471
申请日：2013-12-16
CPC分类号： C10G21/28 , B01D11/0403 , B01J3/008 , C07C7/10 , C07D207/00 , C10G21/08 , C10G2300/202 , C10G2300/205 , C10G2300/44
摘要： Methods for recovering organic heteroatom compounds from a hydrocarbon feedstock include feeding into a contactor a hydrocarbon feedstock and an aqueous solvent to form an extraction mixture of the aqueous solvent with the hydrocarbon feedstock. The hydrocarbon feedstock includes a hydrocarbon and an organic heteroatom compound. The aqueous solvent includes an ionic liquid formed from pressurized carbon dioxide and water. A pressure and temperature of the extraction mixture may be established that together tune the aqueous solvent to selectively form a solvent complex with the at least one organic heteroatom compound. Then, the solvent complex is extracted to a recovery vessel from the extraction mixture in the contactor. By adjustment of a recovery temperature of the recovery vessel, a recovery pressure of the recovery vessel, or both, the solvent complex decomposes into carbon dioxide and the organic heteroatom compound. The organic heteroatom compound is then recovered from the recovery vessel.
摘要翻译： 从烃原料中回收有机杂原子化合物的方法包括将烃原料和含水溶剂进料到接触器中以形成含水溶剂与烃原料的萃取混合物。 烃原料包括烃和有机杂原子化合物。 含水溶剂包括由加压二氧化碳和水形成的离子液体。 可以建立萃取混合物的压力和温度，其一起调节水性溶剂以选择性地与至少一种有机杂原子化合物形成溶剂配合物。 然后，将溶剂配合物从接触器中的萃取混合物中提取回收容器。 通过调节回收容器的回收温度，回收容器的回收压力或二者，溶剂配合物分解成二氧化碳和有机杂原子化合物。 然后从回收容器中回收有机杂原子化合物。
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