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    METHOD AND APPARATUS FOR PRODUCING H2-RICH SYNTHESIS GAS
    3.
    发明申请
    METHOD AND APPARATUS FOR PRODUCING H2-RICH SYNTHESIS GAS 有权
    用于生产氢气合成气的方法和装置

    公开(公告)号：US20170057818A1

    公开(公告)日：2017-03-02

    申请号：US15307898

    申请日：2015-05-13

    申请人： CCP Technology GmbH

    发明人： Olaf Kuhl

    IPC分类号： C01B3/24 ,  C01B3/12 ,  C10K3/04 ,  C10G2/00

    CPC分类号： C01B3/24 ,  C01B3/12 ,  C01B2203/0272 ,  C01B2203/0283 ,  C01B2203/0288 ,  C01B2203/049 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/0805 ,  C01B2203/0844 ,  C01B2203/0861 ,  C01B2203/0883 ,  C01B2203/1276 ,  C01B2203/141 ,  C01B2203/145 ,  C10G2/30 ,  C10G2/32 ,  C10G2/34 ,  C10J2300/1618 ,  C10J2300/1853 ,  C10K3/04 ,  Y02P20/129

    摘要： A method for producing ¾-rich synthesis gas comprises the following steps: decomposing a hydrocarbon-containing fluid into an H2/C-aerosol in a first hydrocarbon converter by supplying energy which is at least partly provided in the form of heat; introducing at least a first stream of the H2/C-aerosol into a first sub-process which comprises the following steps: directing at least a part of the H2/C-aerosol from the first hydrocarbon converter into a first C-converter; introducing CO2 into the first C-converter and mixing the CO2 with the H2/C-aerosol introduced into the first C-converter; converting the mixture of H2/C-aerosol and CO2 into a synthesis gas at a temperature of 800 to 1700° C.; mixing additional H2 with the synthesis gas for the production of H2-rich synthesis gas. In a second sub-process running in parallel with the first sub-process, hydrogen H2 and carbon dioxide CO2 are produced from a hydrocarbon-containing fluid, wherein at least a portion of the CO2 produced in the second sub-process is introduced into the first C-converter; and wherein at least a portion of the H2 produced in the second sub-process is mixed with the synthesis gas from the first C-converter. The CO2 which is needed for the conversion of C in the first C-converter can thereby be provided independently of an external source, and the entire operational sequence is easily controllable.

    摘要翻译： 一种生产富氘合成气的方法包括以下步骤：通过提供至少部分以热的形式提供的能量将烃类流体分解成第一烃转化器中的H 2 / C-气溶胶; 将至少第一流的H2 / C-气溶胶引入到第一子过程中，其包括以下步骤：将来自第一烃转化器的H 2 / C-气溶胶的至少一部分引导到第一C转换器中; 将CO 2引入到第一C转化器中并将CO 2与引入到第一C转换器中的H 2 / C气溶胶混合; 将H 2 / C气溶胶和CO 2的混合物在800至1700℃的温度下转化为合成气; 将额外的H2与合成气混合，用于生产富H2合成气。 在与第一子方法并行运行的第二子方法中，氢气H2和二氧化碳CO 2由含烃流体产生，其中在第二子方法中产生的CO 2的至少一部分被引入 第一个C转换器; 并且其中在所述第二子过程中产生的所述H 2的至少一部分与来自所述第一C转换器的合成气混合。 因此，可以独立于外部源来提供在第一C转换器中转换C所需的CO 2，并且整个操作顺序容易控制。

    Apparatus and method for producing a synthesis gas
    4.
    发明授权
    Apparatus and method for producing a synthesis gas 有权

    公开(公告)号：US10906806B2

    公开(公告)日：2021-02-02

    申请号：US15570392

    申请日：2016-04-29

    申请人： CCP Technology GmbH

    发明人： Olaf Kuhl

    IPC分类号： C01B3/24 ,  B01J19/08 ,  B01J19/26 ,  C10K3/04

    摘要： The apparatus described herein comprises a first reaction chamber having an inlet for a hydrocarbon medium, particularly a gas having the composition CnHm, and an outlet. Means for decomposing the hydrocarbons into carbon particles and hydrogen by introducing heat are provided between the inlet and the outlet in the first reaction chamber. The apparatus also comprises a second reaction chamber having an elongated configuration and having a first inlet at one end and an outlet at the opposite end, wherein the first inlet of the second reaction chamber is connected with the outlet of the first reaction chamber, and wherein the second reaction chamber comprises a widening flow cross-section (measured perpendicular to the longitudinal dimension of the second reaction chamber) between the inlet and the outlet. In addition, at least one second inlet into the second reaction chamber is provided, wherein the second inlet can be connected to a source for CO2 and/or H2O. Preferably, the second inlet is connected with a source of CO2, and therefore CO2 is injected therewith during operation. A method for operating this apparatus is also described. The energy balance of a synthesis gas production can be improved with the apparatus and the method for operating compared with known methods.

    Blast furnace and method for operating a blast furnace
    5.
    发明授权
    Blast furnace and method for operating a blast furnace 有权

    公开(公告)号：US10526670B2

    公开(公告)日：2020-01-07

    申请号：US14955105

    申请日：2015-12-01

    申请人： CCP TECHNOLOGY GMBH

    发明人： Olaf Kuhl

    IPC分类号： C21B5/06 ,  C01B32/40 ,  C21B7/00 ,  F27B1/10 ,  F27D17/00

    摘要： The present blast furnace and method for operating a blast furnace are able to reduce CO2 production and the amount of applied additives and heating material. The method for metal production of metal ores comprising the following steps: reducing a metal ore, particularly a metal oxide, and thereby producing furnace gas containing CO2 in a blast furnace shaft; discharging the furnace gas from the blast furnace shaft; directing at least a portion of the furnace gas into a CO2 converter and reducing the CO2 in the furnace gas into CO; directing at least a portion of the CO from the CO2 converter into the blast furnace shaft. The method produces CO as a gaseous reduction agent which may be easily introduced into the blast furnace shaft. Further, a blast furnace for metal production by reducing a metal ore designed for operating according to the method is described.

    Blast furnace and method for operating a blast furnace
    6.
    发明授权
    Blast furnace and method for operating a blast furnace 有权

    公开(公告)号：US10287643B2

    公开(公告)日：2019-05-14

    申请号：US15039444

    申请日：2014-11-27

    申请人： CCP Technology GmbH

    发明人： Olaf Kuhl

    IPC分类号： C21B5/06 ,  C21B5/00 ,  H01M8/22 ,  B01D53/84 ,  C12M1/02 ,  C12P7/08 ,  B01D53/90 ,  B01D53/86 ,  C21B7/00 ,  C12M1/00 ,  B01D53/62 ,  H01M8/0612 ,  C12P7/06

    摘要： A process for processing metal ore includes: reducing a metal ore, particularly a metallic oxide, in a blast furnace shaft; producing furnace gas containing CO2, in the blast furnace shaft; discharging the furnace gas from the blast furnace shaft; directing at least a portion of the furnace gas directly or indirectly into a CO2-converter; and converting the CO2 contained in the furnace gas into an aerosol consisting of a carrier gas and C-particles in the CO2-converter in the presence of a stoichiometric surplus of C; directing at least a first portion of the aerosol from the CO2-converter into the blast furnace shaft; and introducing H2O into the blast furnace shaft. By virtue of the reaction C+H2O→CO2+2H, nascent hydrogen is produced in the blast furnace which causes rapid reduction of the metal ore. The speed of reduction of the metal ore is thus increased, and it is possible to increase either the throughput capacity of the blast furnace or to reduce the size of the blast furnace. An aerosol in the form of a fluid is easily introducible into the blast furnace shaft.

    METHOD AND DEVICE FOR PRODUCING SYNTHETIC HYDROCARBONS
    7.
    发明申请
    METHOD AND DEVICE FOR PRODUCING SYNTHETIC HYDROCARBONS 审中-公开
    用于生产合成烃的方法和装置

    公开(公告)号：US20170051210A1

    公开(公告)日：2017-02-23

    申请号：US15308151

    申请日：2015-05-13

    申请人： CCP TECHNOLOGY GMBH

    发明人： Olaf Kuhl

    IPC分类号： C10G2/00 ,  C10J3/46

    CPC分类号： C10G2/32 ,  C01B3/24 ,  C01B2203/0266 ,  C01B2203/062 ,  C01B2203/0861 ,  C01B2203/1235 ,  C10G2/34 ,  C10J3/00 ,  C10J3/46 ,  C10J2300/0966 ,  C10J2300/0973 ,  C10J2300/1618 ,  C10J2300/1659 ,  C10J2300/1675

    摘要： A method producing synthetic hydrocarbons includes producing synthesis gas. An initial step, carbon or a mixture of carbon and hydrogen is brought into contact with water at a temperature of 800-1700° C. The synthesis gas is converted into synthetic functionalised and/or non-functionalised hydrocarbons by means of a Fischer Tropsch process wherein it is brought into contact with a suitable catalyst, and wherein water in which a portion of the synthetic hydrocarbons is dissolved results as a by-product. At least a portion of the water that is produced as a by-product is supplied to the initial step. The hydrocarbons that are dissolved in the water decompose into particle-like carbon and hydrogen at the high temperature. The carbon is converted into CO in the presence of water and at a high temperature and forms a portion of the synthesis gas that is produced. In this way, a costly process for cleaning half of the water that is produced as a by-product is avoided.

    摘要翻译： 生产合成烃的方法包括生产合成气。 初始步骤，碳或碳与氢的混合物在800-1700℃的温度下与水接触。合成气通过费 - 托法转化为合成官能化和/或非官能化烃 其中其与合适的催化剂接触，并且其中部分合成烃溶解的水作为副产物产生。 将作为副产物生产的水的至少一部分供给到初始步骤。 溶解在水中的烃在高温下分解成颗粒状碳和氢。 在水和高温存在下将碳转化为CO，并形成所生成的一部分合成气。 以这种方式，避免了作为副产物生产的用于清洁一半水的昂贵的方法。

    PROCESS AND SYSTEM FOR GENERATING SYNTHESIS GAS
    8.
    发明申请
    PROCESS AND SYSTEM FOR GENERATING SYNTHESIS GAS 审中-公开
    用于产生合成气的方法和系统

    公开(公告)号：US20160089654A1

    公开(公告)日：2016-03-31

    申请号：US14964851

    申请日：2015-12-10

    申请人： CCP TECHNOLOGY GMBH

    发明人： Olaf Kuhl

    IPC分类号： B01J19/24 ,  B01J19/12 ,  B01J19/00 ,  C01B3/24

    摘要： A method and an apparatus for generating synthesis gas using hydrocarbons and water are described. In further embodiments of the method and the apparatus, synthesis gases having any desired CO/hydrogen ratio and/or synthetic functionalised and/or non-functionalised hydrocarbons are generated. With this method, a hydrocarbon containing fluid may be transformed into a synthesis gas having variable hydrogen content without generating significant amounts of CO2. Further, hydrogen and different forms of carbon may be obtained as by-products.

    摘要翻译： 描述了使用烃和水产生合成气的方法和装置。 在该方法和装置的其它实施方案中，产生具有任何所需CO /氢比和/或合成官能化和/或非官能化烃的合成气。 通过这种方法，可以将含烃流体转化为具有可变氢含量的合成气，而不产生显着量的CO 2。 此外，作为副产物可以获得氢气和不同形式的碳。