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    Fixed bed reactor heat transfer structure
    1.
    发明授权
    Fixed bed reactor heat transfer structure 有权
    固定床反应器传热结构

    公开(公告)号：US09157689B2

    公开(公告)日：2015-10-13

    申请号：US14078040

    申请日：2013-11-12

    Applicant: Ceramatec, Inc.

    Inventor： Joseph J. Hartvigsen

    IPC: F28F7/00 ,  B01J8/00 ,  B01J8/02 ,  B01J19/00 ,  B01J19/24

    CPC classification number: F28F7/00 ,  B01J8/067 ,  B01J2208/00115 ,  B01J2208/0015 ,  B01J2208/00168 ,  B01J2208/00212 ,  B01J2208/00238 ,  B01J2208/00513 ,  B01J2208/065 ,  B01J2219/30223 ,  B01J2219/30242 ,  B01J2219/30408 ,  B01J2219/30416 ,  F28D2021/0022 ,  F28F1/40

    Abstract: An apparatus includes a heat transfer structure configured to be disposed at least partially within an enclosure of a fixed bed reactor and operable to transfer heat from a heat source to a heat sink. The heat transfer structure includes a plurality of fins each fin including a first end and a second end, the first end contacting an inner surface of the enclosure of the fixed bed reactor, the second end at least partially enclosed within the enclosure of the fixed bed reactor. A path of at least one of the plurality of fins comprises the shortest possible length between the first end of the at least one of the plurality of fins and the second end of the at least one of the plurality of fins.

    Abstract translation: 一种装置包括传热结构，其被配置为至少部分地设置在固定床反应器的外壳内并可操作以将热量从热源传递到散热器。 传热结构包括多个翅片，每个翅片包括第一端和第二端，第一端接触固定床反应器的外壳的内表面，第二端至少部分地封闭在固定床的外壳内 反应堆。 所述多个翅片中的至少一个的路径包括所述多个翅片中的所述至少一个翅片的所述第一端与所述多个翅片中的所述至少一个翅片的所述第二端之间的最短可能长度。

    Method of oxidation utilizing a gliding electric arc
    3.
    发明授权
    Method of oxidation utilizing a gliding electric arc 有权
    使用滑动电弧的氧化方法

    公开(公告)号：US08742285B2

    公开(公告)日：2014-06-03

    申请号：US13911181

    申请日：2013-06-06

    Applicant: Ceramatec, Inc.

    Inventor： Joseph J. Hartvigsen ,  Elangovan ,  Michele Hollist ,  Piotr Czernichowski

    IPC: B23K10/00

    CPC classification number: H05B7/005 ,  F23C99/001 ,  F23C2900/99005 ,  F23G5/085 ,  F23G2204/201 ,  H05H1/48

    Abstract: A method for oxidizing a combustible material. The method includes introducing a volume of the combustible material into a plasma zone of a gliding electric arc oxidation system. The method also includes introducing a volume of oxidizer into the plasma zone of the gliding electric arc oxidation system. The volume of oxidizer includes a stoichiometrically excessive amount of oxygen. The method also includes generating an electrical discharge between electrodes within the plasma zone of the gliding electric arc oxidation system to oxidize the combustible material.

    Abstract translation: 氧化可燃材料的方法。 该方法包括将可燃材料的体积引入到滑动电弧氧化系统的等离子体区域中。 该方法还包括将一定体积的氧化剂引入到滑动电弧氧化系统的等离子体区域中。 氧化剂的体积包括化学计量过量的氧气。 该方法还包括在滑动电弧氧化系统的等离子体区域内的电极之间产生放电，以氧化可燃材料。

    Method of Oxidation Utilizing a Gliding Electric Arc
    4.
    发明申请
    Method of Oxidation Utilizing a Gliding Electric Arc 有权
    使用滑行电弧的氧化方法

    公开(公告)号：US20130277355A1

    公开(公告)日：2013-10-24

    申请号：US13911181

    申请日：2013-06-06

    Applicant: Ceramatec, Inc.

    Inventor： Joseph J. Hartvigsen ,  Elangovan ,  Michele Hollist ,  Piotr Czernichowski

    IPC: H05B7/00

    CPC classification number: H05B7/005 ,  F23C99/001 ,  F23C2900/99005 ,  F23G5/085 ,  F23G2204/201 ,  H05H1/48

    Abstract: A method for oxidizing a combustible material. The method includes introducing a volume of the combustible material into a plasma zone of a gliding electric arc oxidation system. The method also includes introducing a volume of oxidizer into the plasma zone of the gliding electric arc oxidation system. The volume of oxidizer includes a stoichiometrically excessive amount of oxygen. The method also includes generating an electrical discharge between electrodes within the plasma zone of the gliding electric arc oxidation system to oxidize the combustible material.

    Abstract translation: 氧化可燃材料的方法。 该方法包括将可燃材料的体积引入到滑动电弧氧化系统的等离子体区域中。 该方法还包括将一定体积的氧化剂引入到滑动电弧氧化系统的等离子体区域中。 氧化剂的体积包括化学计量过量的氧气。 该方法还包括在滑动电弧氧化系统的等离子体区域内的电极之间产生放电，以氧化可燃材料。

    ADVANCED FISCHER TROPSCH SYSTEM
    5.
    发明申请
    ADVANCED FISCHER TROPSCH SYSTEM 有权
    高级FISCHER TROPSCH系统

    公开(公告)号：US20130216444A1

    公开(公告)日：2013-08-22

    申请号：US13767604

    申请日：2013-02-14

    Applicant: Ceramatec, Inc.

    Inventor： Joseph J. Hartvigsen ,  S. Elangovan ,  Lyman Joseph Frost

    IPC: F28F1/40 ,  B01J8/06

    CPC classification number: F28F1/40 ,  B01J8/067 ,  B01J2208/00513 ,  B01J2208/0084 ,  B01J2208/026 ,  C10G2/31 ,  F28F2215/10

    Abstract: A Fischer Tropsch (“FT”) unit that includes an FT tube that is packed with a catalyst. The catalyst is designed to catalyze an FT reaction to produce a hydrocarbon. An insert that is positioned within the FT tube. The insert comprises at least one cross-piece that contacts an inner surface of the FT tube and at least one cross-fin extending from the cross-piece. There may be a corresponding second cross-fin adjacent each cross-fin. Both the cross-fins and the second cross-fins may be disposed radially outwardly such that the edge of the cross-fins are closer to the inner surface of the FT tube than is the base of the cross-fins.

    Abstract translation: 包括装有催化剂的FT管的费托（“FT”）单元。 催化剂设计用于催化FT反应以产生烃。 位于FT管内的插入件。 所述插入件包括接触所述FT管的内表面的至少一个横截面件和从所述横向件延伸的至少一个横向翅片。 相邻的每个交叉鳍可以有相应的第二横鳍。 十字翅片和第二横鳍都可以径向向外设置，使得横鳍的边缘比翅片的底部更靠近FT管的内表面。

    FIXED BED REACTOR HEAT TRANSFER STRUCTURE
    7.
    发明申请
    FIXED BED REACTOR HEAT TRANSFER STRUCTURE 有权
    固定床反应器热传递结构

    公开(公告)号：US20140134067A1

    公开(公告)日：2014-05-15

    申请号：US14078040

    申请日：2013-11-12

    Applicant: Ceramatec, Inc.

    Inventor： Joseph J. Hartvigsen

    IPC: F28F7/00

    CPC classification number: F28F7/00 ,  B01J8/067 ,  B01J2208/00115 ,  B01J2208/0015 ,  B01J2208/00168 ,  B01J2208/00212 ,  B01J2208/00238 ,  B01J2208/00513 ,  B01J2208/065 ,  B01J2219/30223 ,  B01J2219/30242 ,  B01J2219/30408 ,  B01J2219/30416 ,  F28D2021/0022 ,  F28F1/40

    Abstract: An apparatus includes a heat transfer structure configured to be disposed at least partially within an enclosure of a fixed bed reactor and operable to transfer heat from a heat source to a heat sink. The heat transfer structure includes a plurality of fins each fin including a first end and a second end, the first end contacting an inner surface of the enclosure of the fixed bed reactor, the second end at least partially enclosed within the enclosure of the fixed bed reactor. A path of at least one of the plurality of fins comprises the shortest possible length between the first end of the at least one of the plurality of fins and the second end of the at least one of the plurality of fins.

    Abstract translation: 一种装置包括传热结构，其被配置为至少部分地设置在固定床反应器的外壳内并可操作以将热量从热源传递到散热器。 传热结构包括多个翅片，每个翅片包括第一端和第二端，第一端接触固定床反应器的外壳的内表面，第二端至少部分地封闭在固定床的外壳内 反应堆。 所述多个翅片中的至少一个的路径包括所述多个翅片中的所述至少一个翅片的所述第一端与所述多个翅片中的所述至少一个翅片的所述第二端之间的最短可能长度。

    COMPACT FT COMBINED WITH MICRO-FIBROUS SUPPORTED NANO-CATALYST
    8.
    发明申请
    COMPACT FT COMBINED WITH MICRO-FIBROUS SUPPORTED NANO-CATALYST 有权
    与微纤维支持的纳米催化剂组合的COMPACT FT

    公开(公告)号：US20130216445A1

    公开(公告)日：2013-08-22

    申请号：US13772080

    申请日：2013-02-20

    Applicant: Ceramatec, Inc.

    Inventor： Joseph J. Hartvigsen ,  S. Elangovan ,  Lyman Joseph Frost

    IPC: C07C1/04

    CPC classification number: C07C1/041 ,  B01J8/067 ,  B01J35/0013 ,  B01J35/06 ,  B01J2208/00194 ,  B01J2208/026 ,  B01J2219/0002 ,  C10G2/33 ,  C10G2/341 ,  F28D7/0025 ,  F28F1/12 ,  F28F7/02 ,  F28F13/003

    Abstract: A Fischer Tropsch (“FT”) unit includes at least one FT reactor tube. The FT reactor tube is configured to convert syngas into one or more hydrocarbon products. Inside the tube is a nano-sized catalyst particles dispersed in a micro-fibrous substrate. The FT reactor tube may be positioned within a cooling block that may be made of aluminum or another metal. The cooling block includes an aperture, wherein the FT reactor tube is housed within the aperture. At least one cooling channel is located on the cooling block. The cooling channel houses at least one cooling tube that is designed to dissipate the heat produced by the FT reaction.

    Abstract translation: Fischer Tropsch（“FT”）单元包括至少一个FT反应管。 FT反应器管被配置成将合成气转化为一种或多种烃产物。 管内部是分散在微纤维基质中的纳米级催化剂颗粒。 FT反应器管可以定位在可以由铝或另一种金属制成的冷却块内。 冷却块包括孔，其中FT反应器管容纳在孔内。 至少一个冷却通道位于冷却块上。 冷却通道容纳至少一个设计用于消散由FT反应产生的热量的冷却管。

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