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1. 发明申请

WO2012095560A3 METHOD AND ARRANGEMENT FOR GASIFYING CARBON-BEARING MATERIALS 审中-公开
标题翻译：用于填充碳载体材料的方法和装置
公开(公告)号：WO2012095560A3
公开(公告)日：2012-09-07
申请号：PCT/FI2012050015
申请日：2012-01-09
申请人： ANDRITZ OY , MCKEOUGH PATERSON
发明人： MCKEOUGH PATERSON
IPC分类号： C10J3/46 , C01B3/24 , C01B3/36
CPC分类号： C10J3/463 , C01B3/34 , C01B3/382 , C01B2203/0244 , C01B2203/0283 , C10J3/04 , C10J3/10 , C10J3/46 , C10J3/48 , C10J3/54 , C10J3/64 , C10J3/721 , C10J3/84 , C10J2200/158 , C10J2300/092 , C10J2300/094 , C10J2300/0943 , C10J2300/0956 , C10J2300/0976 , C10J2300/0993 , C10J2300/1246 , C10J2300/169 , C10J2300/1807 , C10J2300/1853 , C10K3/005 , C10K3/006 , C10K3/023
摘要： The subject of the invention is a new method and arrangement for converting a carbon-bearing feed material into a gas having sufficiently small contents of tars and lighter hydrocarbons for the application in question. The method employs one or more fluidized-bed processing stages (A) and gas exiting one or more of these stages (4) is subjected to a reforming treatment (B) either in the presence or absence of catalyst. Gas exiting the reforming stage is mixed (C) with a stream of solids (6), the main component of which is bed material and another component of which is char, the said stream of solids having been led from one or more of the fluidized-bed processing stages, preferably from that to which the carbon-bearing feed material is fed. Downstream of the mixing stage, solids are separated (D) from the gas and then recycled (8) or led to one or more of the fluidized-bed processing stages. The method and arrangement enable heat to be transferred from the hot reformed gas to the gasification stage(s) in an efficient and cost-effective way
摘要翻译：本发明的主题是一种新的方法和装置，用于将含碳原料转化为具有足够小的焦油和轻质烃含量的气体用于所述应用。该方法采用一个或多个流化床处理阶段（A），离开一个或多个这些阶段（4）的气体在催化剂存在或不存在下进行重整处理（B）。离开重整阶段的气体与（6）的固体物流（6）混合，其主要成分是床料，另一种成分为炭，所述固体物流从一个或多个流化床优选地从进料碳载物料的加工阶段。在混合阶段的下游，固体与气体分离（D），然后再循环（8）或导致一个或多个流化床处理阶段。该方法和装置使得热能够以有效和成本有效的方式从热重整气体转移到气化阶段

2. 发明申请

WO2010058089A1 CO-CURRENT GASIFIER 审中-公开
标题翻译：同时燃烧气体
公开(公告)号：WO2010058089A1
公开(公告)日：2010-05-27
申请号：PCT/FI2009/050949
申请日：2009-11-23
申请人： GASEK OY , KANGASOJA, Eero
发明人： KANGASOJA, Eero
IPC分类号： C10J3/26 , C10J3/30
CPC分类号： C10J3/26 , C10J3/04 , C10J3/32 , C10J3/38 , C10J3/42 , C10J3/721 , C10J3/74 , C10J2200/15 , C10J2300/092 , C10J2300/0956 , C10J2300/0959 , C10J2300/1693
摘要： 15 Abstract The co-current gasifier has a fuel silo (14) for storing the fuel to be gasified, such as the wood chips. The bottom of the fuel silo is made up of the upper floor (16a), underneath which there is at least one gasification compartment (20) for gasifying the fuel. The gasification compartment has a combustion chamber, which has a triple wall structure comprising an internal jacket, an intermediate jacket and an external jacket. The upper floor has several holes (30) for conducting the fuel from the fuel silo to the gasification compartment/gasification compartments. The gasification of the fuel takes place in a small area between the lower part of the fuel silo and the upper part of the gasifier. The gasifier may have several gasification compartments, whereby the upper floor has one hole leading from the fuel silo to the gasification compartment for each gasification compartment. Preferably the gasification compartments are situated in a ring-like manner underneath the upper floor. Between the gasification compartment and the upper floor there is a ring-like cooling channel (18), through which the gasification air is conducted into the gasification compartment.In an embodiment of the invention there is further a lower floor and only one gasification compartment, which is situated underneath the lower floor. The upper and lower floors limit between them a cooling space, through which several concentric holes lead.
摘要翻译： 15摘要并流气化炉有一个燃料仓（14），用于储存待气化的燃料，如木屑。燃料仓的底部由上层（16a）构成，其下方有至少一个用于使燃料气化的气化室（20）。气化室具有燃烧室，其具有包括内部护套，中间护套和外部护套的三重壁结构。上层具有用于将燃料从燃料仓导入气化室/气化室的几个孔（30）。燃料的气化发生在燃料仓的下部和气化器的上部之间的一小部分区域中。气化器可以具有几个气化室，由此上层具有从燃料仓到达每个气化室的气化室的一个孔。优选地，气化隔室位于上层的下方环状。在气化室和上层之间有一个环形冷却通道（18），气化空气通过该通道进入气化室。在本发明的一个实施方案中，还有一个下层和仅一个气化室，位于下层的下方。上下两层之间限制了一个冷却空间，几个同心孔穿过它们。

3. 发明申请

WO2008044216A1 METHOD AND APPARATUS FOR GASIFICATION OF ORGANIC WASTE IN BATCHES 审中-公开
标题翻译：用于气化有机废物的方法和装置
公开(公告)号：WO2008044216A1
公开(公告)日：2008-04-17
申请号：PCT/IB2007/054148
申请日：2007-10-12
申请人： PROTERRGO, INC. , TSANTRIZOS, Panayotis
发明人： TSANTRIZOS, Panayotis
IPC分类号： C10J3/04 , C10J3/44
CPC分类号： C10J3/44 , C10J3/04 , C10J3/723 , C10J2300/0946 , C10J2300/1215 , C10J2300/1246 , C10K1/003 , C10K1/007 , C10K1/101 , C10K1/20 , C10K1/32 , Y02P20/129
摘要： A gasification reactor for processing organic waste in batches comprises a primary gasification reactor (62) that includes a primary gasification chamber (18) and a surrounding combustion chamber (19), a secondary gasification chamber (21), a synthesis gas decontamination unit (42) and a combustible gas selector (41). The waste is loaded into the primary gasification chamber through a latched opening and heated from the combustion of a fuel in the combustion chamber (19) to convert the waste to a synthesis gas. The gasification chamber (18) has an intake (20) for introducing pre-heated process air (1) therein. The combustion chamber operates either with a conventional fuel (9) or with the produced synthesis gas (6). The secondary gasification chamber (21) thermally treats the synthesis gas (2) to eliminate tars. The decontamination unit (42) scrubs the synthesis gas of contaminants including particulates and acid gases. The clean synthesis gas (6) is directed to the combustible gas selector (41) which selectively feeds either the combustible fluid (9) or the synthesis gas (6) to the burner (40).
摘要翻译：用于分批处理有机废物的气化反应器包括主气化反应器（62），其包括初级气化室（18）和周围燃烧室（19），二次气化室（21），合成气净化单元（42））和可燃气体选择器（41）。废物通过锁定开口装载到主气化室中，并从燃烧室（19）中的燃料的燃烧加热，以将废物转化为合成气。气化室（18）具有用于在其中引入预热过程空气（1）的进气口（20）。燃烧室与常规燃料（9）或所生产的合成气（6）一起操作。二次气化室（21）热处理合成气（2）以消除焦油。去污单元（42）洗涤包括微粒和酸性气体在内的污染物的合成气。清洁的合成气（6）被引导到可燃气体选择器（41），其将可燃流体（9）或合成气（6）选择性地供给到燃烧器（40）。

4. 发明申请

WO2003089369A1 水素製造方法、水素製造装置、水素供給施設、及び発電方法审中-公开
标题翻译：氢生产方法，氢生产设备，氢供应设备和用于产生电力的方法
公开(公告)号：WO2003089369A1
公开(公告)日：2003-10-30
申请号：PCT/JP2003/003940
申请日：2003-03-28
申请人： JFEエンジニアリング株式会社 , 鈴木実 , 岩崎克博 , 中山剛
发明人：鈴木実 , 岩崎克博 , 中山剛
IPC分类号： C01B3/02
CPC分类号： C10J3/466 , C01B3/56 , C01B2203/043 , C01B2203/047 , C10J3/04 , C10J3/78 , C10J2300/0973 , C10J2300/0979 , C10J2300/1671 , C10J2300/1675 , C10J2300/1807 , C10K1/02 , Y02P20/129
摘要：高温が必要な水素製造を各種熱プロセスから排出される比較的低温の廃熱エネルギーを利用して安価に実現でき、装置の立ち上げ立ち下げが容易で運転費・設備費を抑えられる水素製造方法、並びに水素製造装置、その水素供給施設を提供する。その解決手段として、熱源との熱交換により流体を加熱し、反応前の水素製造装置内の圧力に対して5倍以上の圧力の高圧ガスとする工程と、高圧ガス内を瞬間的に水素製造装置内に開放して衝撃波を発生させる工程と、衝撃波を発生させる前に原料を水素製造装置内に供給する工程と、発生させた衝撃波により原料を衝撃圧縮して加熱し水素製造する工程とを有する水素製造方法であり、並びに該方法を実現するための水素製造装置、水素供給施設である。
摘要翻译：一种氢生产方法，其包括通过与热源进行热交换来加热流体的步骤，从而将其转化为在反应之前的氢气制备装置中的压力为五倍或更多压力的高压气体，步骤立即将高压气体的内部打开到氢气生产装置的内部，从而产生冲击波，在产生冲击波之前将原料供应到氢气生产装置的内部，并且产生冲击的步骤 - 通过产生的冲击波对原材料进行加压，从而产生氢; 以及用于实施该方法的氢气制备装置和氢气供应装置。该方法允许以低成本利用相对较低温度的废热进行常规需要高温热源的氢的生产，以及启动和关闭中的容易操作，以及从而能够抑制氢制造装置的运转成本和设备成本。

5. 发明申请

WO2015022083A3 C-CONVERTER HAVING A FILTERING FUNCTION 审中-公开
标题翻译：具有过滤功能的C转换器
公开(公告)号：WO2015022083A3
公开(公告)日：2015-04-23
申请号：PCT/EP2014025004
申请日：2014-08-12
申请人： CCP TECHNOLOGY GMBH
发明人： KÜHL OLAF
IPC分类号： B01D46/00 , C01B32/40 , C10J3/04 , C10K1/02
CPC分类号： C10J3/04 , C01B31/18 , C01B32/40 , C10J3/20 , C10J2300/0933 , C10J2300/095 , C10J2300/0969 , C10J2300/0976 , C10J2300/1238 , C10J2300/165 , C10J2300/183 , C10J2300/1853 , C10K1/024 , Y02P20/129
摘要： In previously known apparatuses using CO or synthesis gas, where a hot particle flow is supplied into a converter in form of an aerosol, incomplete chemical conversion in the converter may occur. Furthermore, heat losses may occur, which compromises efficiency, and particles may deposit, which leads to interruptions during operation. These problems are solved by a C-converter comprising at least one aerosol converter inlet for an aerosol comprising a first gas and particles containing carbon; at least one converter gas inlet for a second gas; at least two converter chamber outlets and at least two converter chambers which are adapted to be filled with particles between a minimum and a maximum particle filling degree. The C- converter further comprises at least one diverting device which is adapted to selectively connect a fraction of the converter chambers a) to at least one of the aerosol converter inlets for aerosol or b) to at least one of the converter gas inlets for the second gas or may disconnect the converter chambers therefrom; and at least one discharging device which is adapted to selectively connect a fraction of the converter chambers to at least one of the converter outlets or to disconnect the converter chambers therefrom. Aerosols containing particles may be converted by means of the C-converter without interruption, and a high conversion degree of the materials supplied into the converter is obtained. Furthermore, an apparatus for producing CO or synthesis gas is disclosed, wherein the C-converter may be used. Methods for operating the C-converter and the apparatus for producing CO or synthesis gas are also disclosed.
摘要翻译：在先前已知的使用CO或合成气的设备中，其中热粒子流以气溶胶形式供应到转换器中，可能发生转换器中的不完全化学转化。此外，可能发生热损失，这会损害效率，并且颗粒可能沉积，这会导致操作过程中的中断。这些问题通过一种C转换器解决，该C转换器包括用于气雾剂的至少一个气雾剂转换器入口，该气雾剂包括第一气体和含碳颗粒; 至少一个用于第二气体的转换器气体入口; 至少两个转换器腔室出口和至少两个转换器腔室，所述至少两个转换器腔室适于填充最小颗粒填充度和最大颗粒填充度之间的颗粒。 C转换器还包括至少一个转向装置，该转向装置适于选择性地将转换器腔室a）的一部分连接到用于气雾剂的气雾转换器入口中的至少一个，或者b）用于转换器气体入口中的至少一个，第二气体或可以从其中断开转换器腔室; 以及至少一个放电装置，其适于将一部分转换器腔室选择性地连接到至少一个转换器出口或将转换器腔室与其分离。含有颗粒的气溶胶可以通过C转换器无中断地转换，并且获得供应到转换器中的材料的高转换度。此外，公开了一种用于生产CO或合成气的设备，其中可以使用C转换器。还公开了用于操作C转换器和用于生产CO或合成气的设备的方法。

6. 发明申请

WO2012093030A1 SYSTEM AND METHOD FOR PRODUCING SYNGAS FROM CARBON BASED MATERIAL 审中-公开
标题翻译：用于生产基于碳的材料的方法的系统和方法
公开(公告)号：WO2012093030A1
公开(公告)日：2012-07-12
申请号：PCT/EP2011/073453
申请日：2011-12-20
申请人： HIGH TECH ENERGIE SRO , DE BELLIS, Michele
发明人： DE BELLIS, Michele
IPC分类号： C10B21/10 , C10J3/66 , C10J3/72
CPC分类号： C10J3/66 , C10B21/10 , C10J3/04 , C10J3/723 , C10J2300/0916 , C10J2300/0956 , C10J2300/0959 , C10J2300/1606 , C10J2300/1675
摘要： The present invention relates to a system and method for producing "Syngas" (1) from carbon based material comprising means for feeding (10) the material into the system (1), means for combustion of the material, adapted to produce Syngas, means for use (20) of the Syngas and means for extraction of the combustion residues, wherein the means for combustion of the material comprise: a sealed combustion chamber, with temperatures between 300 and 600 °C, capable of decomposing the organic molecules of the carbon based material into a mixture of gases and into ash; a device for injection of gas (330) into the combustion chamber; a device for monitoring the quantity of gas introduced/to be introduced into the combustion chamber, capable of guaranteeing a correct sub - stoichiometric ratio for decomposition of the organic molecules.
摘要翻译：本发明涉及一种用于从碳基材料制造“合成气”（1）的系统和方法，该系统和方法包括用于将材料（10）进料到系统（1）中的装置，适于产生合成气的材料的燃烧装置用于合成气的（20）和用于提取燃烧残余物的装置，其中用于燃烧的燃料的装置包括：密封的燃烧室，温度在300和600℃之间，能够分解碳的有机分子将其作为气体和灰分的混合物; 用于将气体（330）注入燃烧室的装置; 用于监测引入/引入燃烧室的气体的量的装置，能够确保有机分子的分解的正确的亚化学计量比。

7. 发明申请

WO2010052667A3 DEVICE AND METHOD FOR GASIFICATION AND/OR PYROLYSIS, OR EVAPORATION OF A COMBUSTIBLE MATERIAL 审中-公开
标题翻译：用于气化和/或热解或可燃材料的蒸发的装置和方法
公开(公告)号：WO2010052667A3
公开(公告)日：2010-11-04
申请号：PCT/IB2009054934
申请日：2009-11-06
申请人： MULCAHY NATHANIEL
发明人： MULCAHY NATHANIEL
IPC分类号： F24B1/20 , C10J3/02 , C10J3/04 , C10J3/26 , C10J3/74 , F24B5/02
CPC分类号： C10J3/02 , C10J3/04 , C10J3/26 , C10J3/74 , C10J2200/31 , C10J2300/092
摘要： The device comprises: an inner chamber (56) which has an upper aperture or mouth (36) and is delimited by a lateral wall (20) and by a base wall (19), and which is intended to contain a primary fuel to be subjected to gasification and/or pyrolysis or vaporization to generate combustible gases; an outer chamber (58) delimited by an outer lateral wall (22) positioned coaxially with the outside of the lateral wall (20) of the inner chamber (56), by a base wall (14) which is located under the base wall (19) of the combustion chamber (56) and which has at least one aperture (28) communicating with the external environment, and by a top wall which unites the outer (22) and inner (20) lateral walls, in such a way that the outer chamber (58) comprises a lower portion positioned under the inner chamber (56) and an upper annular portion (59) which surrounds the inner chamber (56); a plurality of circumferentially staggered lower passages (50) through which the base of the inner chamber (56) communicates with the surrounding annular portion (59) of the outer chamber (58); and - a plurality of circumferentially staggered upper passages (39) through which the top of the annular portion (59) of the outer chamber (58) communicates with the top of the inner chamber (56).
摘要翻译：该装置包括：内室（56），其具有上孔或开口（36）并且由侧壁（20）和底壁（19）限定，并且其旨在包含主燃料经历气化和/或热解或蒸发以产生可燃气体; 由外壁（22）限定的外室（58），所述外侧壁（22）通过位于底壁下方的底壁（14）与所述内室（56）的侧壁（20）的外侧同轴地定位具有与外部环境连通的至少一个孔口（28）的燃烧室（56），以及与外部（22）和内部（20）侧壁结合的顶壁，使得所述外室（58）包括位于所述内室（56）下方的下部和围绕所述内室（56）的上环形部分（59）。多个周向交错的下通道（50），内室（56）的基部通过该下通道与外室（58）的周围环形部分（59）连通; 以及 - 多个周向交错的上通道（39），外室（58）的环形部分（59）的顶部通过该上通道与内室（56）的顶部连通。

8. 发明申请

WO02004345A1 METHOD FOR HYDROGEN PRODUCTION 审中-公开
标题翻译：氢生产方法
公开(公告)号：WO02004345A1
公开(公告)日：2002-01-17
申请号：PCT/SG2001/000137
申请日：2001-06-29
IPC分类号： B01J23/78 , B01J37/08 , C01B3/04 , C01B32/40 , C01B32/50 , C10J3/04 , C01B3/06 , C01B3/26
CPC分类号： B82Y30/00 , B01J23/78 , B01J37/084 , C01B3/045 , C01B32/40 , C01B32/50 , C10J3/04 , C10J2200/06 , C10J2300/093 , C10J2300/0986 , C10J2300/183 , Y02E60/364 , Y02P20/52
摘要： The present work provides a new route for production of hydrogen via water and preformed carbon materials at a relatively low temperature. The preformed carbon materials comprise carbon nanotubes or nanofibers bonded to a transition metal and are obtained by the catalytic decomposition of hydrocarbons in a reductive atmosphere in the presence of the transition metal catalyst. Experimental results demonstrate that the transition metal bonded to the carbon nanotubes or nanofibers has a high activity for the production of hydrogen at temperatures around 450 DEG C.
摘要翻译：本工作为在相对低的温度下通过水和预制碳材料生产氢气提供了新的途径。预成型碳材料包括碳纳米管或结合到过渡金属的纳米纤维，并且通过在还原气氛中在过渡金属催化剂的存在下催化分解烃而获得。实验结果表明，结合到碳纳米管或纳米纤维的过渡金属在450℃左右的氢气生产中具有很高的活性。

9. 发明申请

WO1991009095A1 INTERMITTENTLY-FED HIGH-PRESSURE GASIFIER 审中-公开
标题翻译： INTERMITTENIGFED高压气化器
公开(公告)号：WO1991009095A1
公开(公告)日：1991-06-27
申请号：PCT/US1990001229
申请日：1990-03-09
申请人： CATERPILLAR INC.
发明人： CATERPILLAR INC. , BAILEY, John, M. , ZADOKS, Abraham, L.
IPC分类号： C10J03/78
CPC分类号： C10J3/04 , C10J3/06 , C10J3/44 , C10J3/78 , C10J2300/1606 , C10J2300/1643 , C10J2300/1693 , C10K1/00 , C10K1/004 , F02B1/04
摘要： An improved gasifier (40) adapted for gasifying a predetermined charge (56, 56a) of non-gaseous fuel into fuel gas (26). Each charge of non-gaseous fuel, which may have optional conditioning materials (46, 48, 70) added to it, is intermittently fed to a gasifier chamber (42, 42a) where each charge is partially burned with high-pressure air (18) supplied thereto. High-pressure and temperature fuel gas (26) is produced which is cleansed prior to passing out of the gasifier chamber (42, 42a). After gasification of the charge (56, 56a) of fuel is ended, the gasifier chamber (42, 42a) is vented. The residue of the burned charge in the gasifier chamber (42, 42a) is removed, along with the contaminated or reacted conditioning materials, and replaced by a fresh charge. The subject invention provides a feasible way of continuously fueling an internal combustion engine (12) with gasified fuel and is compact enough to be practical for even mobile applications.
摘要翻译：一种改进的气化器（40），适用于将非气态燃料的预定装料（56,56a）气化成燃料气体（26）。向其中添加可选择的调节材料（46,48,70）的非气态燃料的每次充电被间歇地供给到气化器室（42,42a），其中每个电荷部分地被高压空气燃烧（18 ）。产生高压和高温燃料气体（26），其在通过气化器室（42,52）之前被清洁。在燃料的装料（56,56a）气化结束之后，气化器室（42,52）被排出。在气化器室（42,42a）中的燃烧装料的残留物与被污染或反应的调理材料一起被去除，并被新鲜电荷代替。本发明提供了一种用气化燃料连续燃烧内燃机（12）的可行方法，并且足够紧凑以适用于甚至移动应用。

10. 发明申请

WO2015022083A2 C-CONVERTER HAVING A FILTERING FUNCTION 审中-公开
标题翻译：具有滤波功能的C转换器
公开(公告)号：WO2015022083A2
公开(公告)日：2015-02-19
申请号：PCT/EP2014/025004
申请日：2014-08-12
申请人： CCP TECHNOLOGY GMBH
发明人： KÜHL, Olaf
IPC分类号： B01D46/00
CPC分类号： C10J3/04 , C01B31/18 , C01B32/40 , C10J3/20 , C10J2300/0933 , C10J2300/095 , C10J2300/0969 , C10J2300/0976 , C10J2300/1238 , C10J2300/165 , C10J2300/183 , C10J2300/1853 , C10K1/024 , Y02P20/129
摘要： In previously known apparatuses using CO or synthesis gas, where a hot particle flow is supplied into a converter in form of an aerosol, incomplete chemical conversion in the converter may occur. Furthermore, heat losses may occur, which compromises efficiency, and particles may deposit, which leads to interruptions during operation. These problems are solved by a C-converter comprising at least one aerosol converter inlet for an aerosol comprising a first gas and particles containing carbon; at least one converter gas inlet for a second gas; at least two converter chamber outlets and at least two converter chambers which are adapted to be filled with particles between a minimum and a maximum particle filling degree. The C- converter further comprises at least one diverting device which is adapted to selectively connect a fraction of the converter chambers a) to at least one of the aerosol converter inlets for aerosol or b) to at least one of the converter gas inlets for the second gas or may disconnect the converter chambers therefrom; and at least one discharging device which is adapted to selectively connect a fraction of the converter chambers to at least one of the converter outlets or to disconnect the converter chambers therefrom. Aerosols containing particles may be converted by means of the C-converter without interruption, and a high conversion degree of the materials supplied into the converter is obtained. Furthermore, an apparatus for producing CO or synthesis gas is disclosed, wherein the C-converter may be used. Methods for operating the C-converter and the apparatus for producing CO or synthesis gas are also disclosed.
摘要翻译：在使用CO或合成气的先前已知的装置中，其中热的颗粒流以气溶胶的形式供应到转化器中，可能发生转化器中的不完全的化学转化。此外，可能发生热损失，其损害效率，并且颗粒可能沉积，这导致在操作期间的中断。这些问题由包括至少一个用于气溶胶的气溶胶转化器入口的C转换器解决，所述气溶胶包含第一气体和含有碳的颗粒; 用于第二气体的至少一个转换器气体入口; 至少两个转炉室出口和至少两个转化器室，其适于填充最小和最大颗粒填充度之间的颗粒。 C转换器还包括至少一个转向装置，其适于选择性地将转换器腔室a）的一部分连接到用于气溶胶的气溶胶转换器入口中的至少一个或b）至少一个转换器气体入口或者可以从其间断开转换器室; 以及至少一个排放装置，其适于选择性地将一部分转换器室连接到至少一个转换器出口或者从其中断开转换器室。含有颗粒的气溶胶可以通过C转换器而不间断地转化，并且获得提供给转化器的材料的高转化度。此外，公开了一种用于生产CO或合成气的设备，其中可以使用C转换器。还公开了用于操作C转换器和用于生产CO或合成气的装置的方法。

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