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公开(公告)号：EP0286704B1
公开(公告)日：1990-09-19
申请号：EP87105521.6
申请日：1987-04-14
CPC分类号： F28D7/08 , F01M2001/1092 , F16N39/02 , F28D2021/0089 , Y10S165/395
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公开(公告)号：EP0131502B1
公开(公告)日：1988-01-27
申请号：EP84401324.3
申请日：1984-06-25
发明人： Rogier, Serge , Guigonis,Jacques
CPC分类号： F28F21/04 , F28F7/02 , Y10S165/395 , Y10S165/905
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公开(公告)号：EP0286704A1
公开(公告)日：1988-10-19
申请号：EP87105521.6
申请日：1987-04-14
CPC分类号： F28D7/08 , F01M2001/1092 , F16N39/02 , F28D2021/0089 , Y10S165/395
摘要： Die Erfindung betrifft einen Wärmetauscher (1) für zwei fluide Medien, insbesondere Flüssigkeiten, mit einem mit einem Deckel (4) verschließbarem Gehäuse (2) mit Zu- und Abläufen für die beiden Medien und mit einem Einsatz (3) für die getrennte Führung der beiden Medien unter Wärmeaustausch, wobei zumindest der Einsatz (3) als Druckgußteil herstellbar ist, bei welchem der Einsatz (3) im wesentlichen aus einem die Kanäle für die beiden Medien in Form von hohen, schmalen Kammern (51 - 53, 51ʹ bis 53ʹ; 61 - 61ʹʹʹ) bildenden, mäandrierend verlaufenden Wandungszug (30) gebildet ist, wobei benachbarte Kammern (51 - 53, 51ʹ - 53ʹ; 61 - 61ʹʹʹ) abwechselnd von dem einen und dem anderen Medium durchströmt sind, und bei welchem die Kammern (51 - 53, 51ʹ - 53ʹ; 61 - 61ʹʹʹ) jeweils durch eine gemeinsame, mit dem Wandungszug (30) einstückige, alle Kammern (51 - 53, 51ʹ - 53ʹ; 61 - 61ʹʹʹ) in der Höhe unterteilende Zwischenwandung (34) in nacheinander durchströmte, in zwei Ebenen angeordnete Teilkammern (51 - 53, 51ʹ - 53ʹ; 61 - 61ʹʹʹ) geteilt sind.
摘要翻译： 本发明涉及一种热交换器（1），用于两种流体介质，尤其是液体，可封闭的有盖（4）壳体（2）与入口和出口的两个媒体和插入件（3）的单独的指导 热交换的情况下两个媒体，至少所述插入件（3）被生产为压铸部件，其特征在于，所述插入件（3）基本上由在高，中，窄腔室（51-53形式的信道的两种介质，51“〜53的 ）61 '' '通过一个流量和其他介质交替 - 61;形成 - ;' 61 61 '' '）成形（曲折延伸Wandungszug 30），其中相邻的室（51 - - 53 51' 53' 是，并且其中所述腔室（51 - 53，51 ' - 53'; 61 - 61 '' '）在每种情况下通过一个联合成一体，与Wandungszug（30）中，所有的腔室（51 - 53，51' - 53' ; 61-61“”“）（在分割的中间壁34）的高度流经相继在两个平面昂 eordnete局部腔室（51 - 53，51 ' - 53'; 61-61 ''“）被划分。
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公开(公告)号：EP0131502A1
公开(公告)日：1985-01-16
申请号：EP84401324.3
申请日：1984-06-25
发明人： Rogier, Serge , Guigonis,Jacques
CPC分类号： F28F21/04 , F28F7/02 , Y10S165/395 , Y10S165/905
摘要： Echangeur de chaleur; cet échangeur à fluides séparés comporte un corps monolithique, moulé en matière réfractaire, qui comprend en son sein, venus de moulage, au moins un canal (2) pour le fluide à réchauffer et au moins un canal (5) pour le fluide à refroidir en relation mutuelle d'échange de chaleur.
Application à toutes industries avec des fluides corrosifs ou abrasifs, pour basses ou hautes températures.-
5.发明公开Ceramic recuperative heat exchanger and a method for producing the same 失效Keramischer Rekuperator和Verfahren zu dessen Herstellung。
公开(公告)号：EP0037236A1
公开(公告)日：1981-10-07
申请号：EP81301265.5
申请日：1981-03-24
申请人： NGK INSULATORS, LTD.
发明人： Oda, Isao , Matsuhisa, Tadaaki
CPC分类号： F28F7/02 , F28F21/04 , Y10S165/395 , Y10T428/24149
摘要： A ceramic honeycomb type recuperative heat exchanger has a large number of parallel channels defined by partition walls, in which fluids to be heat-exchanged are passed through respective channels, wherein the sectional shape of the channels and the thickness of the partition walls are uniform, the open frontal area of the heat transmitting portion where the fluids are heat-exchanged is more than 60%, and the porosity of the ceramic material forming the partition walls is not more than 10%.
Such a heat-exchanger is suitably produced by extruding a ceramic raw batch material into a honeycomb structural body, drying the shaped honeycomb structural body, prior to or after a firing step, cutting off partition walls in given rows of the honeycomb structural body in the axial direction of the channels to a given depth from the end surface of the honeycomb structural body, and sealing only the end surfaces of said rows.摘要翻译： 陶瓷蜂窝式回热换热器具有大量由隔壁限定的平行通道，其中待热交换的流体通过相应的通道，其中通道的截面形状和分隔壁的厚度是均匀的， 热交换流体的传热部的开口面积大于60％，形成隔壁的陶瓷材料的孔隙率不大于10％。 ...这样的热交换器适当地通过在烧制步骤之前或之后将陶瓷原料批料材料挤压成蜂窝结构体，干燥成形蜂窝结构体而制成，从而切断给定行中的分隔壁 蜂窝结构体在通道的轴向方向上从蜂窝结构体的端面到给定的深度，并且仅密封所述行的端面。
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6.发明授权
公开(公告)号：EP1444475B1
公开(公告)日：2007-07-11
申请号：EP02768180.8
申请日：2002-09-25
申请人： NORSK HYDRO ASA
CPC分类号： F28F9/0278 , F23C13/00 , F23C2900/03001 , F23C2900/13001 , F28F7/02 , Y10S165/395
摘要： The present invention concerns a method with associated equipment for feeding two gases into and out of a multi-channel monolithic structure. The two gases will normally be two gases with different chemical and/or physical properties. The gases, here called gas 1 and gas 2, are fed by means of a manifold head into channels for gas 1 and gas 2 respectively. Gas 1 and gas 2 are distributed in the monolith in such a way that at least one of the channel walls is a shared or joint wall for gas 1 and gas 2. The walls that are joint walls for the two gases will then constitute a contact area between the two gases that is available for mass and/or heat exchange. This means that the gases must be fed into channels that are spread over the entire cross-sectional area of the monolith. The present invention makes it possible to utilise the entire contact area or all of the monolith's channel walls directly for heat and/or mass transfer between gas 1 and gas 2. This means that the channel for one gas will always have the other gas on the other side of its channel walls, i.e. all adjacent or neighbouring channels for gas 1 contain gas 2 and vice versa. The present invention will be particularly applicable for making compact ceramic membrane structures and/or heat exchanger structures that must handle gases at high temperature. Typical applications are oxygen-conducting ceramic membranes, heat exchangers for gas turbines and heat exchanger reformers for production of synthetic gas.
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公开(公告)号：EP0221049A1
公开(公告)日：1987-05-13
申请号：EP84902953.0
申请日：1984-06-28
发明人： STENLUND, Stig, Göte
CPC分类号： F28F3/02 , F01M2011/0025 , F28D7/106 , F28F1/42 , F28F1/422 , F28F9/22 , F28F2210/02 , F28F2260/02 , Y10S165/395 , Y10S165/903
摘要： Echangeur thermique pour l'échange thermique entre deux milieux (Ma, Mb), s'écoulant chacun à travers l'une des deux chambres (A, B) séparées par une paroi de séparation (5) imperméable au milieu et à base d'un matériau thermiquement conducteur. L'intérieur de chaque chambre d'écoulement ou d'au moins une chambre d'écoulement, est divisé en un grand nombre de passages d'écoulement de milieu, connectés en parallèle par rapport à l'écoulement de milieu les traversant. Les passages d'écoulement (13 et 17) sont de section transversale essentiellement rectangulaire et dotés d'une zone d'écoulement conçue quant au milieu la traversant de telle manière que l'écoulement dans les passages est essentiellement laminaire sur toute la longueur des passages, sans zone turbulente centrale. Les parois des passages déterminant les passages d'écoulement sont à base d'un matériau fortement thermiquement conducteur et font partie intégrante de la paroi de séparation (5) située entre les deux chambres d'écoulement (A, B) ou sont en contact de conduction thermique avec celle-ci. La largeur (s) des passages d'écoulement parallèles à la paroi de séparation est d'au maximum 1,5 mm et de préférence inférieure à 1,0 mm. La hauteur (h) des passages d'écoulement, et donc des parois des passages à angles droits par rapport à la paroi de séparation est normalement inférieure à 8 mm et se situe souvent entre 2 et 5 mm, alors que l'épaisseur des parois des passages est normalement inférieure à 1 mm.
摘要翻译： 用于两个介质（Ma，Mb）之间进行热交换的热交换器，每个介质流过两个室（A，B）中的一个，由介质不透水的分隔壁（5）隔开，并基于 导热材料。 每个流动室或至少一个流动室的内部被分成大量介质流动通道，该介质流动通道与通过其中的介质流平行连接。 流动通道（13和17）具有基本上矩形的横截面并且具有为穿过其中的介质设计的流动区，使得通道中的流动沿着通道的整个长度基本上是层状的。 ，没有中央湍流区。 限定流动通道的通道的壁基于高导热材料并且形成位于两个流动室（A，B）之间或彼此接触的分隔壁（5）的整体部分。 与它的热传导。 平行于分隔壁的流动通道的宽度最多为1.5mm，优选小于1.0mm。 流动通道的高度（h）以及与分隔壁成直角的通道壁的高度（h）通常小于8毫米，通常在2至5毫米之间，而壁厚 通道通常小于1毫米。
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公开(公告)号：EP0037236B1
公开(公告)日：1984-06-13
申请号：EP81301265.5
申请日：1981-03-24
申请人： NGK INSULATORS, LTD.
发明人： Oda, Isao , Matsuhisa, Tadaaki
CPC分类号： F28F7/02 , F28F21/04 , Y10S165/395 , Y10T428/24149
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9.发明公开
公开(公告)号：EP1444475A1
公开(公告)日：2004-08-11
申请号：EP02768180.8
申请日：2002-09-25
申请人： NORSK HYDRO ASA
CPC分类号： F28F9/0278 , F23C13/00 , F23C2900/03001 , F23C2900/13001 , F28F7/02 , Y10S165/395
摘要： The present invention concerns a method with associated equipment for feeding two gases into and out of a multi-channel monolithic structure. The two gases will normally be two gases with different chemical and/or physical properties. The gases, here called gas 1 and gas 2, are fed by means of a manifold head into channels for gas 1 and gas 2 respectively. Gas 1 and gas 2 are distributed in the monolith in such a way that at least one of the channel walls is a shared or joint wall for gas 1 and gas 2. The walls that are joint walls for the two gases will then constitute a contact area between the two gases that is available for mass and/or heat exchange. This means that the gases must be fed into channels that are spread over the entire cross-sectional area of the monolith. The present invention makes it possible to utilise the entire contact area or all of the monolith's channel walls directly for heat and/or mass transfer between gas 1 and gas 2. This means that the channel for one gas will always have the other gas on the other side of its channel walls, i.e. all adjacent or neighbouring channels for gas 1 contain gas 2 and vice versa. The present invention will be particularly applicable for making compact ceramic membrane structures and/or heat exchanger structures that must handle gases at high temperature. Typical applications are oxygen-conducting ceramic membranes, heat exchangers for gas turbines and heat exchanger reformers for production of synthetic gas.
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公开(公告)号：EP0221049B1
公开(公告)日：1988-11-23
申请号：EP84902953.3
申请日：1984-06-28
申请人： HYPECO AB
发明人： STENLUND, Stig, Göte
IPC分类号： F28D9/00
CPC分类号： F28F3/02 , F01M2011/0025 , F28D7/106 , F28F1/42 , F28F1/422 , F28F9/22 , F28F2210/02 , F28F2260/02 , Y10S165/395 , Y10S165/903
摘要： A heat exchanger for the exchange of heat between two media (Ma, Mb), each of which flows through a respective one of two chambers (A, B) mutually separated by a medium-impervious partition wall (5) made of thermal conductive material. The interior of each of the flow chambers, or at least of one flow chamber, is divided into a large number of medium-flow passages, which are connected in parallel with respect to the flow of medium passing therethrough. The flow passages (13, and 17) have a substantially rectangular cross-section having a flow area which is so adapted in respect of the medium flowing therethrough that the flow in the passages is substantially laminar throughout the whole length of the passages, without a central turbulent zone. The passage walls defining the flow passages comprise a highly thermal-conductive material and are formed integrally with, or in good heat-conducting contact with the partition wall (5) located between the two flow chambers (A, B). The width (s) of the flow passages parallel with the partition wall is at most 1.5 mm and preferably less than 1.00 mm. The height (h) of the flow passages, and therewith the passage walls, at right angles to the partition wall is normally less than 8 mm and often 2-5 mm, while the thickness of the passage walls is normally less than 1 mm.
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