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    ELECTROCHEMICAL MODULE CONFIGURATION FOR THE CONTINUOUS ACIDIFICATION OF ALKALINE WATER SOURCES AND RECOVERY OF CO2 WITH CONTINUOUS HYDROGEN GAS PRODUCTION
    2.
    发明申请
    ELECTROCHEMICAL MODULE CONFIGURATION FOR THE CONTINUOUS ACIDIFICATION OF ALKALINE WATER SOURCES AND RECOVERY OF CO2 WITH CONTINUOUS HYDROGEN GAS PRODUCTION 有权
    电化学模块配置连续酸化碱性水源和回收二氧化碳连续生产氢气

    公开(公告)号：US20140238869A1

    公开(公告)日：2014-08-28

    申请号：US14193281

    申请日：2014-02-28

    申请人： Felice DiMascio ,  Heather D. Willauer ,  Dennis R. Hardy ,  Frederick Williams ,  M. Kathleen Lewis

    发明人： Felice DiMascio ,  Heather D. Willauer ,  Dennis R. Hardy ,  Frederick Williams ,  M. Kathleen Lewis

    IPC分类号： C25B9/08 ,  C25B1/10

    CPC分类号： C25B1/10 ,  C01B31/20 ,  C01B32/50 ,  C02F2001/46185 ,  C02F2201/46115 ,  C25B1/00 ,  C25B9/10 ,  Y02E60/366

    摘要： An electrochemical cell for the continuous acidification of alkaline water sources and recovery of carbon dioxide with simultaneous continuous hydrogen gas production having a center compartment, an electrolyte-free anode compartment having a mesh anode in direct contact with an ion permeable membrane, an endblock in direct contact with the anode where the endblock provides a gas escape route behind the anode, an electrolyte-free cathode compartment having a mesh cathode in direct contact with an ion permeable membrane, and an endblock in direct contact with the cathode where the endblock provides a gas escape route behind the cathode. Current applied to the electrochemical cell for generating hydrogen gas also lowers the pH of the alkaline water to produce carbon dioxide with no additional current or power. Also disclosed is the related method for continuously acidifying alkaline water sources and recovering carbon dioxide with continuous hydrogen gas production.

    摘要翻译： 一种用于碱性水源的连续酸化和二氧化碳回收的电化学电池，同时具有中间室的连续氢气生产，具有与离子渗透膜直接接触的网状阳极的无电解质阳极室，直接接触的端块 与阳极接触，其中端块提供阳极背后的气体逸出路径，具有与离子可渗透膜直接接触的网状阴极的无电解质阴极室和与阴极直接接触的端块，其中端块提供气体 阴极后面的逃生路线。 施加到用于产生氢气的电化学电池的电流也降低碱性水的pH以产生没有额外的电流或功率的二氧化碳。 还公开了连续酸化碱性水源和连续氢气生产回收二氧化碳的相关方法。

    EXTRACTION OF CARBON DIOXIDE AND HYDROGEN FROM SEAWATER AND HYDROCARBON PRODUCTION THEREFROM
    4.
    发明申请
    EXTRACTION OF CARBON DIOXIDE AND HYDROGEN FROM SEAWATER AND HYDROCARBON PRODUCTION THEREFROM 有权
    二氧化碳和氢气从海水中萃取和碳氢化合物生产

    公开(公告)号：US20130206605A1

    公开(公告)日：2013-08-15

    申请号：US13838074

    申请日：2013-03-15

    申请人： Felice DiMascio ,  Dennis R. Hardy ,  Heather D. Willauer ,  M. Kathleen Lewis ,  Frederick Williams

    发明人： Felice DiMascio ,  Dennis R. Hardy ,  Heather D. Willauer ,  M. Kathleen Lewis ,  Frederick Williams

    IPC分类号： C25B1/04

    CPC分类号： C25B9/10 ,  C01B31/20 ,  C01B32/50 ,  C10G2/50 ,  C10G2300/42 ,  C10G2400/08 ,  C25B1/04 ,  C25B1/10 ,  C25B9/08 ,  C25B15/02 ,  C25B15/08 ,  Y02E60/366 ,  Y02W10/37

    摘要： Apparatus for seawater acidification including an ion exchange, cathode and anode electrode compartments and cation-permeable membranes that separate the electrode compartments from the ion exchange compartment. Means is provided for feeding seawater through the ion exchange compartment and for feeding a dissociable liquid media through the anode and cathode electrode compartments. A cathode is located in the cathode electrode compartment and an anode is located in the anode electrode compartment and a means for application of current to the cathode and anode is provided. A method for the acidification of seawater by subjecting the seawater to an ion exchange reaction to exchange H+ ions for Na+ ions. Carbon dioxide may be extracted from the acidified seawater. Optionally, the ion exchange reaction can be conducted under conditions which produce hydrogen as well as carbon dioxide. The carbon dioxide and hydrogen may be used to produce hydrocarbons.

    摘要翻译： 用于海水酸化的装置，包括离子交换器，阴极和阳极电极隔室以及将电极隔室与离子交换隔室分离的阳离子可透过膜。 提供用于通过离子交换室供给海水并且用于通过阳极和阴极隔室供给可离解的液体介质的装置。 阴极位于阴极电极室中，并且阳极位于阳极电极室中，并且提供用于向阴极和阳极施加电流的装置。 通过使海水进行离子交换反应以交换Na +离子的H +离子来使海水酸化的方法。 可以从酸化的海水中提取二氧化碳。 任选地，离子交换反应可以在产生氢气以及二氧化碳的条件下进行。 二氧化碳和氢气可用于生产碳氢化合物。

    Extraction of Carbon Dioxide and Hydrogen From Seawater and Hydrocarbon Production Therefrom
    6.
    发明申请
    Extraction of Carbon Dioxide and Hydrogen From Seawater and Hydrocarbon Production Therefrom 审中-公开
    从海水中提取二氧化碳和氢气及其生产

    公开(公告)号：US20110281959A1

    公开(公告)日：2011-11-17

    申请号：US12958963

    申请日：2010-12-02

    申请人： Feice DiMascio ,  Dennis R. Hardy ,  Heather D. Willauer ,  M. Kathleen Lewis ,  Frederick Williams

    发明人： Feice DiMascio ,  Dennis R. Hardy ,  Heather D. Willauer ,  M. Kathleen Lewis ,  Frederick Williams

    IPC分类号： C07C1/12 ,  C02F1/461 ,  C25B1/02 ,  C25B9/00

    CPC分类号： C25B9/10 ,  C01B32/50 ,  C10G2/50 ,  C10G2300/42 ,  C10G2400/08 ,  C25B1/04 ,  C25B1/10 ,  C25B9/08 ,  C25B15/02 ,  C25B15/08 ,  Y02E60/366 ,  Y02W10/37

    摘要： Apparatus for seawater acidification including an ion exchange, cathode and anode electrode compartments and cation-permeable membranes that separate the electrode compartments from the ion exchange compartment. Means is provided for feeding seawater through the ion exchange compartment and for feeding a dissociable liquid media through the anode and cathode electrode compartments. A cathode is located in the cathode electrode compartment and an anode is located in the anode electrode compartment and a means for application of current to the cathode and anode is provided. A method for the acidification of seawater by subjecting the seawater to an ion exchange reaction to exchange H+ ions for Na+ ions. Carbon dioxide may be extracted from the acidified seawater. Optionally, the ion exchange reaction can be conducted under conditions which produce hydrogen as well as carbon dioxide. The carbon dioxide and hydrogen may be used to produce hydrocarbons.

    摘要翻译： 用于海水酸化的装置，包括离子交换器，阴极和阳极电极隔室以及将电极隔室与离子交换隔室分离的阳离子可透过膜。 提供用于通过离子交换室供给海水并且用于通过阳极和阴极隔室供给可离解的液体介质的装置。 阴极位于阴极电极室中，并且阳极位于阳极电极室中，并且提供用于向阴极和阳极施加电流的装置。 通过使海水进行离子交换反应以交换Na +离子的H +离子来使海水酸化的方法。 可以从酸化的海水中提取二氧化碳。 任选地，离子交换反应可以在产生氢气以及二氧化碳的条件下进行。 二氧化碳和氢气可用于生产碳氢化合物。

    Catalytic Support for use in Carbon Dioxide Hydrogenation Reactions
    7.
    发明申请
    Catalytic Support for use in Carbon Dioxide Hydrogenation Reactions 有权
    催化支持用于二氧化碳氢化反应

    公开(公告)号：US20110105630A1

    公开(公告)日：2011-05-05

    申请号：US12914237

    申请日：2010-10-28

    申请人： Robert W. Dorner ,  Heather D. Willauer ,  Dennis R. Hardy

    发明人： Robert W. Dorner ,  Heather D. Willauer ,  Dennis R. Hardy

    IPC分类号： C07C1/00 ,  B01J21/04 ,  B01J37/00 ,  B01J37/08 ,  B01J37/02

    CPC分类号： B01J37/03 ,  B01J21/04 ,  B01J23/10 ,  B01J23/24 ,  B01J23/63 ,  B01J23/83 ,  B01J23/8892 ,  B01J35/002 ,  B01J35/1019 ,  B01J37/0201 ,  B01J37/08 ,  B01J37/16 ,  C10G2/50 ,  C10K3/026

    摘要： A catalyst support which may be used to support various catalysts for use in reactions for hydrogenation of carbon dioxide including a catalyst support material and an active material capable of catalyzing a reverse water-gas shift (RWGS) reaction associated with the catalyst support material. A catalyst for hydrogenation of carbon dioxide may be supported on the catalyst support. A method for making a catalyst for use in hydrogenation of carbon dioxide including application of an active material capable of catalyzing a reverse water-gas shift (RWGS) reaction to a catalyst support material, the coated catalyst support material is optionally calcined, and a catalyst for the hydrogenation of carbon dioxide is deposited on the coated catalyst support material. A process for hydrogenation of carbon dioxide and for making syngas comprising a hydrocarbon, esp. methane, reforming step and a RWGS step which employs the catalyst composition of the present invention and products thereof.

    摘要翻译： 催化剂载体，其可用于支持用于二氧化碳的氢化反应的各种催化剂，包括催化剂载体材料和能够催化与催化剂载体材料相关联的反向水煤气变换（RWGS）反应的活性材料。 用于二氧化碳氢化的催化剂可以负载在催化剂载体上。 一种用于制备用于二氧化碳氢化的催化剂的方法，包括将能够催化反向水煤气变换（RWGS）反应的活性物质应用于催化剂载体材料，任选地煅烧所述涂覆的催化剂载体材料和催化剂 因为二氧化碳的氢化沉积在涂覆的催化剂载体材料上。 一种用于二氧化碳的氢化和用于制备包含烃的合成气的方法， 甲烷，重整步骤和使用本发明的催化剂组合物的RWGS步骤及其产物。

    Method for assessing distillate fuel stability by oxygen overpressure
    8.
    发明授权
    Method for assessing distillate fuel stability by oxygen overpressure 失效
    通过氧气超压评估馏出燃料稳定性的方法

    公开(公告)号：US5162235A

    公开(公告)日：1992-11-10

    申请号：US371782

    申请日：1989-06-27

    申请人： Dennis R. Hardy ,  Erna J. Beal ,  Jack C. Burnett

    发明人： Dennis R. Hardy ,  Erna J. Beal ,  Jack C. Burnett

    IPC分类号： G01N5/00 ,  G01N33/28

    CPC分类号： G01N5/00 ,  G01N33/2805 ,  Y10S44/903 ,  Y10T436/21 ,  Y10T436/214 ,  Y10T436/25375

    摘要： Reactions leading to insoluble sediments formation in distillate fuel are accelerated by forcing oxygen into solution in the fuel at pressures of between about 90 and 110 psig and then stressing the fuel under conditions of accelerated storage at temperatures of between about 40.degree. C. to 100.degree. C. The method then makes use of gravimetric determination of the total insolubles formed. The stability of the fuel over a period of time as well as its comparative stability to other fuels can then be predicted from the amount of insolubles formed. The method can be carried out by using a specialized pressure vessel.

    摘要翻译： 导致在馏出燃料中形成不溶性沉积物的反应通过在大约90-110psig的压力下迫使氧气在燃料中溶解，然后在加速储存的条件下在约40℃至100℃的温度下加压燃料而加速 然后，该方法利用形成的总不溶物的重量测定。 然后可以从形成的不溶物的量来预测燃料在一段时间内的稳定性以及其对其他燃料的比较稳定性。 该方法可以通过使用专门的压力容器进行。

    Regeneration of solid absorbant fuel stability enhancing material
    9.
    依法登记的发明
    Regeneration of solid absorbant fuel stability enhancing material 失效

    公开(公告)号：USH1071H

    公开(公告)日：1992-07-07

    申请号：US628113

    申请日：1990-12-13

    申请人： Margaret A. Wechter ,  Dennis R. Hardy

    发明人： Margaret A. Wechter ,  Dennis R. Hardy

    IPC分类号： B01J19/00 ,  C10L10/00

    CPC分类号： B01J19/002 ,  C10L10/06

    摘要： Liquid hydrocarbon fuels such as diesel fuel and aviation jet fuel are stabilized by insertion of solid porous stabilizing foam into storage tanks. Fuel-insoluble particles resulting from degradation of the fuel which form during prolonged storage are absorbed by the foam. The absorbed particles are removed from the foam by contacting it with a polar solvent. The foam thus regenerated is re-used for continued stabilization of stored liquid hydrocarbon fuels. The polar solvent having fuel-insoluble particles dissolved therein is recovered by distillation for re-use.

    SYNTHESIS OF HYDROCARBONS VIA CATALYTIC REDUCTION OF CO2
    10.
    发明申请
    SYNTHESIS OF HYDROCARBONS VIA CATALYTIC REDUCTION OF CO2 有权
    通过二氧化碳的催化还原来合成碳氢化合物

    公开(公告)号：US20110268617A1

    公开(公告)日：2011-11-03

    申请号：US13181566

    申请日：2011-07-13

    申请人： Nick E. Tran ,  Dennis R. Hardy ,  Samuel G. Lambrakos ,  John G. Michopoulos

    发明人： Nick E. Tran ,  Dennis R. Hardy ,  Samuel G. Lambrakos ,  John G. Michopoulos

    IPC分类号： B01J19/00

    CPC分类号： C10G2/50 ,  B01J8/0285 ,  B01J8/067 ,  B01J2208/00044 ,  B01J2208/0007 ,  B01J2208/00176 ,  C01B3/042 ,  C01B2203/062 ,  C10G2/00 ,  C10G2/32 ,  C10G2/332 ,  C10G2/334 ,  Y02E60/364 ,  Y02P20/142

    摘要： A method of: introducing hydrogen and a feed gas containing at least 50 vol % carbon dioxide into a reactor containing a Fischer-Tropsch catalyst; and heating the hydrogen and carbon dioxide to a temperature of at least about 190° C. to produce hydrocarbons in the reactor. An apparatus having: a reaction vessel for containing a Fischer-Tropsch catalyst, capable of heating gases to at least about 190° C.; a hydrogen delivery system feeding into the reaction vessel; a carbon dioxide delivery system for delivering a feed gas containing at least 50 vol % carbon dioxide feeding into the reaction vessel; and a trap for collecting hydrocarbons generated in the reaction vessel.

    摘要翻译： 一种将含有至少50体积％二氧化碳的氢气和进料气体引入含有费 - 托催化剂的反应器中的方法; 并将氢气和二氧化碳加热到至少约190℃的温度以在反应器中产生烃。 一种装置，具有：用于容纳费 - 托催化剂的反应容器，其能够将气体加热至至少约190℃; 供给到反应容器中的氢输送系统; 用于将含有至少50体积％二氧化碳的进料气体输送到反应容器中的二氧化碳输送系统; 以及用于收集在反应容器中产生的烃的捕集阱。