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    SANNER CYCLE ENERGY SYSTEM AND CONVERTER
    1.
    发明申请
    SANNER CYCLE ENERGY SYSTEM AND CONVERTER 审中-公开
    SANNER循环能源系统和转换器

    公开(公告)号：WO2012069636A2

    公开(公告)日：2012-05-31

    申请号：PCT/EP2011/071042

    申请日：2011-11-25

    Applicant: STATOIL ASA ,  SANNER, Gunnar

    Inventor： SANNER, Gunnar

    CPC classification number: F23L7/007 ,  C01B3/042 ,  C10G2/00 ,  C10G2/50 ,  C10G2300/4062 ,  C10G2300/4068 ,  F01K27/00 ,  F03G6/00 ,  F23J2215/50 ,  F24S21/00 ,  F24V99/00 ,  F28D20/003 ,  Y02E10/46 ,  Y02E20/326 ,  Y02E20/344 ,  Y02E60/364 ,  Y02P20/133 ,  Y02P20/134

    Abstract: The invention concerns an energy system (particular embodiment of Sanner cycle), comprising a first energy converting plant located at a first geographical position and a second energy converting plant located at a second geographical position, wherein the first energy converting plant is configured to produce hydrocarbon (HC) and oxygen (O 2 ) from carbon dioxide (CO 2 ) and water (H 2 O) using energy obtained from a non-fossil energy source, wherein the second energy converting plant is configured to produce power, electricity and/or heat by reacting HC and O 2 such as to form CO 2 and H 2 O, and wherein said energy system further comprises a transporting system configured to transport the HC produced in the first energy converting plant to the second energy converting plant and to transport the CO 2 produced in the second energy converting plant to the first energy converting plant. The invention is characterized in that the first energy converting plant is configured to extract the O 2 produced and that the transporting system is configured to transport said O 2 to the second energy converting plant. The energy system can also be set up in a network consisting of multiple first energy converting plants (Energy upload) and second energy converting plants (Energy offload) with transportation of energy carrying and energy depleted compounds in-between, forming a Sanner cycle network.

    Abstract translation: 本发明涉及能量系统（Sanner循环的特定实施例），其包括位于第一地理位置的第一能量转换设备和位于第二地理位置的第二能量转换设备，其中第一能量转换设备被配置为产生烃 （HC）和来自二氧化碳（CO 2）和水（H 2 O）的氧（O 2），其中使用从非化石能源获得的能量，其中所述第二能量转换装置被配置为通过HC反应来产生动力，电和/ 和O 2，以形成CO 2和H 2 O.并且其中所述能量系统还包括传送系统，其构造成将在第一能量转换装置中生产的HC运输到第二能量转换装置并运送在第二能量转换装置中产生的CO 2 到第一个能量转换厂。 本发明的特征在于，第一能量转换装置被配置为提取所产生的O 2，并且传送系统被配置为将所述O 2传送到第二能量转换装置。 能源系统还可以在由多个第一能量转换装置（能量上传）和第二能量转换装置（能量卸载）组成的网络中建立，其中能量运输和能量消耗化合物在其间传输，形成了Sanner循环网络。

    SANNER CYCLE ENERGY SYSTEM
    3.
    发明申请
    SANNER CYCLE ENERGY SYSTEM 审中-公开

    公开(公告)号：WO2012069635A3

    公开(公告)日：2012-05-31

    申请号：PCT/EP2011/071041

    申请日：2011-11-25

    Applicant: SANNER, Gunnar

    Inventor： SANNER, Gunnar

    IPC: F01K27/00 ,  C01B3/04 ,  C07C1/12 ,  C10G2/00 ,  F23L7/00 ,  F24J1/00

    Abstract: The invention concerns an energy system, comprising a first energy converting plant (10) located at a first geographical position and a second energy converting plant (20) located at a second geographical position, wherein the first energy converting (10) plant is configured to produce at least one energy carrying compound from at least one energy depleted compound using energy obtained from a non-fossil energy source, wherein the second energy converting plant (20) is configured to produce power, electricity and/or heat by reacting the at least one energy carrying compound such as to form the at least one energy depleted compound, and wherein said energy system further comprises a transporting system (30) configured to transport the at least one energy carrying compound produced in the first energy converting plant (10) to the second energy converting plant (20) and to transport the at least one energy depleted compound produced in the second energy converting plant (20) to the first energy converting plant (10). The energy system forms a closed loop with regard to the energy carrying and energy depleted compounds produced at the first and second energy converting plants (10, 20), wherein the at least one energy carrying compound produced in the first plant (10) is transported in the closed loop to the second plant (20) as to form a reactant at that plant, and wherein the at least one energy depleted compound produced in the second plant (20) is transported in the closed loop to the first plant (10) as to form a reactant at that plant. Energy conversion plants can also be set up in a network with transportation of energy carrying and energy depleted compounds in-between forming a Sanner cycle network.

    THERMAL REACTOR
    4.
    发明申请
    THERMAL REACTOR 审中-公开
    热反应器

    公开(公告)号：WO2016107868A1

    公开(公告)日：2016-07-07

    申请号：PCT/EP2015/081344

    申请日：2015-12-29

    Applicant: SANNER, Gunnar

    Inventor： SANNER, Gunnar

    IPC: C01B3/04 ,  B01J19/00 ,  C01B3/50 ,  C01B13/02

    CPC classification number: C01B3/042 ,  B01J3/002 ,  B01J19/0053 ,  B01J19/1812 ,  B01J19/1893 ,  B01J2219/00144 ,  B01J2219/00155 ,  C01B3/045 ,  C01B3/501 ,  C01B3/508 ,  C01B13/0251 ,  Y02E60/364

    Abstract: The present invention provides a thermal driven reactor comprising a reaction chamber tolerating to be heated above 500°C and tolerating an internal pressure of above 50 atm, wherein the reaction chamber comprises walls and at least part of said walls are configured to transfer heat energy into the reaction chamber, a reactant inlet in fluid communication with the reaction chamber and at least one sorber element movable between a position within the reaction chamber and a position in a desorption chamber in communication with the reaction chamber, and the fluid communication with the reaction chamber is closable so that the desorption chamber can be depressurized without influencing the pressure in the reaction chamber, and at least one reaction product conduit in fluid communication with the desorption chamber via a closable reaction product outlet, and a method for performing thermal reaction.

    Abstract translation: 本发明提供了一种热驱动的反应器，其包括耐受500℃以上加热的反应室，并且耐受大于50atm的内部压力，其中反应室包括壁，并且至少部分所述壁构造成将热能转移到 反应室，与反应室流体连通的反应物入口和可在反应室内的位置和与反应室连通的解吸室中的位置之间可移动的至少一个吸附器元件，以及与反应室的流体连通 是可以关闭的，使得解吸室可以减压而不影响反应室中的压力，以及至少一个通过可闭合的反应产物出口与解吸室流体连通的反应产物导管，以及进行热反应的方法。

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