公开(公告)号：US20070129449A1

公开(公告)日：2007-06-07

申请号：US10582699

申请日：2004-12-13

Applicant: Norbert Topf ,  Guenter Liebisch

Inventor： Norbert Topf ,  Guenter Liebisch

IPC: F27B15/00 ,  C07C27/00 ,  B32B5/02 ,  C07C27/06

CPC classification number: C10J3/482 ,  C10J3/06 ,  C10J3/54 ,  C10J2300/09 ,  C10J2300/0909 ,  C10J2300/0973 ,  C10J2300/1284 ,  C10J2300/16 ,  C10J2300/1637 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1671 ,  C10J2300/1684 ,  C10J2300/1884 ,  C25B1/04 ,  C25B15/08 ,  Y02E60/366 ,  Y02P20/129

Abstract: The invention relates to a method and installation for producing liquid energy carriers from a solid carbon carrier by means of gasifying a solid carbon carrier. The installation is at least comprised of a drying device (1), a gasification apparatus (2), a synthesizing device (3) for synthesizing the liquid energy carrier, a device (4) for effecting the electrolysis of water for producing oxygen serving as a gasification agent and hydrogen for the synthesis process, and of a combustion apparatus (5), which is connected to the output of the gasification apparatus (2) for carbon-containing gasification residues (I) and to the oxygen outlet (C2) of the device for effecting the electrolysis of water (4). According to the invention, at least a portion of the waste steam from the drying device and at least a portion of the residual gas arising during synthesis are fed to the gasification process in the gasification apparatus. In addition, the carbon-containing residuals (I) from the gasification apparatus (2) and a portion of the oxygen (C2) produced in the device for effecting the electrolysis of water (4) can be fed to a combustion apparatus (5), and the carbon dioxide-containing and oxygen-containing waste gas from the combustion apparatus (K) can be fed to the combustion apparatus (2) in the form of a gasification agent.

Abstract translation: 本发明涉及一种通过气化固体碳载体从固体碳载体生产液体能量载体的方​​法和装置。 该装置至少包括干燥装置（1），气化装置（2），用于合成液体能量载体的合成装置（3），用于进行用于产生氧气的水的电解的装置（4） 用于合成过程的气化剂和氢气，以及与用于含碳气化残渣（I）的气化装置（2）的输出端连接到氧气出口（C 2）的燃烧装置（5） 用于实现水的电解的装置（4）。 根据本发明，来自干燥装置的废蒸汽的至少一部分和合成期间产生的至少一部分残留气体被供给到气化装置中的气化过程。 此外，来自气化装置（2）的含碳残渣（I）和用于进行水的电解（4）的装置中产生的氧气（C 2）的一部分可以被供给到燃烧装置（5） ），来自燃烧装置（K）的含二氧化碳和含氧废气可以以气化剂的形式供给到燃烧装置（2）。

公开(公告)号：US07456226B2

公开(公告)日：2008-11-25

申请号：US10582699

申请日：2004-12-13

Applicant: Norbert Topf ,  Guenter Liebisch

Inventor： Norbert Topf ,  Guenter Liebisch

IPC: C07C27/00

CPC classification number: C10J3/482 ,  C10J3/06 ,  C10J3/54 ,  C10J2300/09 ,  C10J2300/0909 ,  C10J2300/0973 ,  C10J2300/1284 ,  C10J2300/16 ,  C10J2300/1637 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1671 ,  C10J2300/1684 ,  C10J2300/1884 ,  C25B1/04 ,  C25B15/08 ,  Y02E60/366 ,  Y02P20/129

Abstract: The invention relates to a method and installation for producing liquid energy carriers from a solid carbon carrier by means of gasifying a solid carbon carrier. The installation is at least comprised of a drying device, a gasification apparatus, a synthesizing device for synthesizing the liquid energy carrier, a device for effecting the electrolysis of water for producing oxygen serving as a gasification agent and hydrogen for the synthesis process, and of a combustion apparatus, which is connected to the output of the gasification apparatus for carbon-containing gasification residues and to the oxygen outlet of the device for effecting the electrolysis of water. According to the invention, at least a portion of the waste steam from the drying device and at least a portion of the residual gas arising during synthesis are fed to the gasification process in the gasification apparatus. In addition, the carbon-containing residuals from the gasification apparatus and a portion of the oxygen produced in the device for effecting the electrolysis of water can be fed to a combustion apparatus, and the carbon dioxide-containing and oxygen-containing waste gas from the combustion apparatus can be fed to the combustion apparatus in the form of a gasification agent.

Abstract translation: 本发明涉及一种通过气化固体碳载体从固体碳载体生产液体能量载体的方​​法和装置。 该装置至少包括干燥装置，气化装置，用于合成液体能量载体的合成装置，用于产生用作气化剂的氧的电解电解和用于合成过程的氢的装置，以及 燃烧装置，其连接到用于含碳气化残渣的气化装置的输出端和用于进行电解的装置的氧气出口。 根据本发明，来自干燥装置的废蒸汽的至少一部分和合成期间产生的至少一部分残留气体被供给到气化装置中的气化过程。 此外，来自气化装置的含碳残渣和用于实现水的电解的装置中产生的一部分氧气可以被供给到燃烧装置，并且来自所述二氧化碳的含氧废气 燃烧装置可以以气化剂的形式供给到燃烧装置。

公开(公告)号：US5961673A

公开(公告)日：1999-10-05

申请号：US981016

申请日：1997-12-23

Applicant: Norbert Topf ,  Guenter Reichert ,  Dieter Hahn ,  Guenter Liebisch

Inventor： Norbert Topf ,  Guenter Reichert ,  Dieter Hahn ,  Guenter Liebisch

IPC: C10J3/02 ,  C10J3/24 ,  C10J3/26 ,  C10J3/80 ,  C10J1/28 ,  B09B3/00 ,  C07C1/00

CPC classification number: C10J3/80 ,  C10J3/24 ,  C10J3/26 ,  C10J3/32 ,  C10J3/36 ,  C10J3/723 ,  C10J3/74 ,  C10J3/86 ,  C10K1/024 ,  C10J2300/1606 ,  C10J2300/1671

Abstract: The invention concerns a process and apparatus for gasifying carbon-containing products, in particular waste and residues conditioned or processed in a suitable way. Gasification takes place in a mixed flow composed of a counter flow, direct flow and transverse flow. A portion of the gasifying agent is introduced through an inclined grate in the form of a step grate and thrust grating and ash is removed at the bottom end of the grate. Fuel gas is drawn off above the upper level of the grate on the side opposite the lateral feed of the gasifying agent. The gasification apparatus is enclosed in a double-layer insulating/cooling system in which air is used as the insulator and coolant. The gasification process is regulated by the temperature profile of the gasification apparatus, the position of the principal gasification zone is adjusted by ash discharge, the gasification temperature is regulated by the flow of gasifying agent and the output is regulated by the width of the gasification zone. The fuel gas produced is used preferably for generating electricity in a work machine. Exhaust gases are purified preferably with the aid of an active coke filter.

Abstract translation: PCT No.PCT / DE96 / 01122 Sec。 371 1997年12月23日第 102（e）1997年12月23日PCT PCT 1996年6月26日PCT公布。 出版物WO97 / 01618 日期1997年1月16日本发明涉及一种用于气化碳含量产物，特别是以适当方式调理或加工的废物和残余物的方法和装置。 气化发生在由逆流，直流和横向流组成的混合流中。 气化剂的一部分通过倾斜的炉排以阶梯式格栅和推力格栅的形式引入，并且在炉排的底端除去灰分。 燃料气体在与气化剂的侧向进料相对的一侧的炉排上方排出。 气化装置封闭在双层绝热/冷却系统中，其中使用空气作为绝缘体和冷却剂。 气化过程由气化装置的温度曲线调节，主气化区的位置由灰分排放调节，气化温度由气化剂流量调节，输出由气化区的宽度 。 生产的燃料气体优选用于在工作机器中发电。 优选地，借助于活性焦炭过滤器净化废气。