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    • 5. 发明公开
    • VERFAHREN UND VORRICHTUNG ZUR HERSTELLUNG VON SYNTHETISCHEN KOHLENWASSERSTOFFEN
    • EP3143102A1
    • 2017-03-22
    • EP15723903.9
    • 2015-05-13
    • CCP Technology GmbH
    • KÜHL, Olaf
    • C10G2/00C01B3/24C10J3/00
    • C10G2/32C01B3/24C01B2203/0266C01B2203/062C01B2203/0861C01B2203/1235C10G2/34C10J3/00C10J3/46C10J2300/0966C10J2300/0973C10J2300/1659C10J2300/1675
    • The invention relates to a method for producing synthetic hydrocarbons, wherein synthesis gas is produced in that, in a step a), carbon is brought in contact with water or a mixture of carbon and hydrogen is brought in contact with water, namely at a temperature of 800 - 1700 °C. Thereafter, in a step b), the synthesis gas is converted into synthetic, functionalized, and/or non-functionalized hydrocarbons by means of a Fischer-Tropsch process, wherein the synthesis gas is brought in contact with a suitable catalyst, and wherein water arises as a by-product, in which water a part of the synthetic hydrocarbons is dissolved. Then, in a step c), at least a part of the water produced as a by-product is fed to step a). The hydrocarbons dissolved in the water decompose into particulate carbon and hydrogen at the high temperature in step a). The carbon is converted into CO in the presence of water and at high temperature in step a). In this way, expensive purification of half of the water produced as a by-product in step b) is avoided. The expenditure for processing the product water can be reduced. The invention further relates to a plant suitable for performing the method.
    • 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。通过费 - 托法将合成气转化成合成的官能化和/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。 作为副产物生产的水的至少一部分被供给到初始步骤。 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,形成一部分合成气。 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。
    • 10. 发明公开
    • HOCHOFEN UND VERFAHREN ZUM BETRIEB EINES HOCHOFENS
    • EP3008218A1
    • 2016-04-20
    • EP14730814.2
    • 2014-06-05
    • CCP Technology GmbH
    • KÜHL, Olaf
    • C21B5/06C21B7/00
    • C21B5/06C10K3/026C10L1/02C10L1/04C10L2290/26C21B7/002C21B2100/22C21B2100/282C21B2100/62F27B1/10F27D17/001F27D17/008Y02P10/122Y02P10/128Y02P10/265Y02P10/283
    • The problem addressed by the invention is that of creating a blast furnace and a method for operating a blast furnace that are suitable for reducing the CO
      2 emission and the amount of additives and heating fuels compared to currently used metallurgical plants. This problem is solved by a process for processing metal ores, comprising the following steps: reducing a metal ore, in particular a metal oxide; producing a top gas containing CO
      2 in a blast-furnace shaft; discharging the top gas from the blast furnace; conducting at least part of the top gas directly or indirectly to a CO
      2 converter and reducing the CO
      2 contained in the top gas to CO in the CO
      2 converter; and conducting at least a first part of the CO from the CO
      2 converter into the blast-furnace shaft. In addition to the solution of the problem stated above, CO is produced by means of the process as a gaseous reductant that can be easily introduced into the blast-furnace shaft. A blast furnace for extracting metal that operates in accordance with the process comprises the following: a blast-furnace shaft having a first top-gas outlet and at least one CO inlet; a CO
      2 converter, which has a CO
      2 converter entry and a CO
      2 converter gas inlet for gases containing CO
      2 and is suitable for reducing CO
      2 to CO; wherein the top-gas outlet is connected directly or indirectly to the CO
      2 converter gas inlet; and wherein the CO
      2 converter has at least a first CO outlet for discharging a first part of the CO produced in the CO
      2 converter, the at least first CO outlet being connected directly or indirectly to the blast-furnace shaft.
    • 本发明涉及一种用于操作高炉的高炉和一种能够减少二氧化碳产生并减少施加的添加剂和加热材料的量与当前已知的冶金设备相比的方法。 金属矿石的金属制造方法解决了这个问题,包括以下步骤:还原金属矿,特别是金属氧化物; 在高炉井中生产含CO 2的炉煤; 从高炉轴排出炉气; 将至少一部分炉煤气直接或间接地引导到CO 2转化器中,并将CO 2转化器中所含的炉内气体中的CO 2还原成CO,将来自CO 2转化器的CO的至少一部分引入高炉炉中。 除了解决上述问题之外,该方法还产生可以容易地引入鼓风炉轴的气态还原剂CO。