公开(公告)号：EP2806231A4

公开(公告)日：2015-06-24

申请号：EP12866258

申请日：2012-09-17

申请人： CHOI SUNG-HWAN

发明人： CHOI SUNG-HWAN

IPC分类号： F24H1/36 ,  F24H1/18 ,  F24H1/28 ,  F24H9/00

CPC分类号： F24H1/186 ,  F24H1/18 ,  F24H1/287 ,  F24H8/00 ,  F24H9/0005 ,  F24H9/0031 ,  F28D7/1676 ,  F28D20/0034 ,  F28F1/40 ,  Y02B30/102 ,  Y02E60/142

公开(公告)号：EP2742303A2

公开(公告)日：2014-06-18

申请号：EP12743135.1

申请日：2012-07-31

申请人： Outotec OYJ

发明人： DAUM, Karl-Heinz ,  STORCH, Hannes ,  SCHALK, Wolfram

IPC分类号： F28D7/16

CPC分类号： F28D7/16 ,  F28D7/1676 ,  F28D9/0006

摘要： A heat exchanger, in particular for use in the contact group of a sulfuric acid plant, includes a chamber (2) in which a tube bundle (12) is arranged on a circular ring, wherein between the tube bundle (12) and a chamber casing (13) surrounding the tube bundle (12) a gas space (15) is formed, a gas supply opening (6) provided in the chamber casing (13) for introducing a gas into the gas space (15) substantially radially relative to the tube bundle (12), and a gas outlet opening which adjoins an interior space (16) enclosed by the tube bundle (12) in substantially axial direction. A uniform approach flow of the tube bundle (12) is achieved in that the center (Z
R ) of the tube bundle (12) is offset with respect to the center (Z
K ) of the chamber casing (13) in a direction opposite to the gas supply opening (6).

公开(公告)号：EP2072938A3

公开(公告)日：2011-03-23

申请号：EP08157829.6

申请日：2008-06-09

申请人： A.M. S.R.L.

发明人： Vanini, Giuseppe

IPC分类号： F28D7/16 ,  F28D21/00 ,  F28F9/18 ,  B23K20/12 ,  F24H1/40 ,  F24H8/00 ,  F24H9/00

CPC分类号： F28D7/1676 ,  B23K20/1255 ,  B23K20/1265 ,  B23K2201/14 ,  F22B7/08 ,  F24H1/403 ,  F24H8/00 ,  F24H9/0026 ,  F28D21/0007 ,  F28F9/18 ,  F28F2275/062 ,  Y02B30/102

摘要： A heat exchanger for a boiler comprises a plurality of exchanger conduits (2; 2') adjacent and parallel to an axis (X), that are fixed at opposite ends (2a, 2b) to manifold means (3, 4; 3', 4') arranged for conveying a fluid (F) to be heated through said exchanger conduits (2; 2'), characterised in that said exchanger conduits (2; 2') are arranged around said axis (X) so as to form an internal space (5; 5') arranged for receiving combustion fumes (S) entering said exchanger (1) and for enabling a substantially radial and uniform distribution of said combustion fumes (S) exiting through said exchanger conduits (2; 2').

摘要翻译： 用于锅炉的热交换器包括与轴线（X）相邻并平行的多个交换器导管（2; 2'），其在相对端（2a，2b）处固定到歧管装置（3,4; 3'， 4'），其布置成通过所述交换器管道（2; 2'）输送待加热的流体（F），其特征在于，所述交换器管道（2; 2'）围绕所述轴线（X）布置，以形成 布置成用于接收进入所述交换器（1）的燃烧烟雾（S）并且用于使所述燃烧烟雾（S）从所述交换器导管（2; 2'）排出的基本上径向均匀分布的内部空间（5; 5'）。

公开(公告)号：EP2025913B1

公开(公告)日：2011-01-05

申请号：EP08165549.0

申请日：2006-11-22

申请人： BORGWARNER EMISSION SYSTEMS SPAIN, S.L.

发明人： Castaño Gonzàles, Carlos Manuel ,  Grande Fernández, José Antonio

IPC分类号： F02M25/07

CPC分类号： F28F27/02 ,  F02M26/26 ,  F02M26/32 ,  F28D7/1638 ,  F28D7/1676 ,  F28D21/0003 ,  F28F2250/06

公开(公告)号：EP1795801B1

公开(公告)日：2009-11-11

申请号：EP04773355.5

申请日：2004-09-15

申请人： Nomura Reinetsu Yugengaisha

发明人： NOMURA, Shuzo, Taisei-Haimu 102

IPC分类号： F22G1/16 ,  F28D1/06 ,  F22G3/00

CPC分类号： F22G3/007 ,  F28D7/1676 ,  F28F9/26 ,  F28F13/12

公开(公告)号：EP1288604B1

公开(公告)日：2009-10-14

申请号：EP02017009.8

申请日：2002-07-27

申请人： Behr GmbH & Co. KG

发明人： Emrich, Karsten

IPC分类号： F28D9/00

CPC分类号： F28D7/1676 ,  F02B29/0412 ,  F02B29/0462 ,  F28D7/06 ,  F28D9/0012 ,  F28D2021/0082 ,  F28F1/32 ,  F28F1/34 ,  F28F2215/00 ,  Y02T10/146

公开(公告)号：EP1705447A3

公开(公告)日：2006-12-27

申请号：EP06011074.9

申请日：2003-10-10

申请人： Modine Manufacturing Company

发明人： Valensa, Jeroen ,  Reinke, Michael J. ,  Voss, Mark G.

IPC分类号： F28D9/00 ,  H01M8/02

CPC分类号： H01M8/04074 ,  C01B3/382 ,  C01B3/48 ,  F28D7/1676 ,  F28D9/005 ,  F28D9/0075 ,  F28F9/22 ,  F28F2250/102 ,  H01M8/04014 ,  H01M8/0631 ,  Y02P20/129

摘要： A fuel processing system (36) for a proton exchange membrane type fuell cell system comprises a heat exchanger (50) for transferring heat between first and second fluids (52) and (54) having a maximum operating mass flow rate through the heat exchanger (50) and mass flow rates that are substantially proportional to each other. The heat exchanger (50) provides essentially constant outlet temperatures for the first and second fluids (52,54) for all of the flow rates within the operating spectrum of the heat exchanger (50) without the use of an active control system.

公开(公告)号：EP1429101A2

公开(公告)日：2004-06-16

申请号：EP03028552.2

申请日：2003-12-11

申请人： Modine Manufacturing Company

发明人： Meshenky, Steven, P.

IPC分类号： F28F1/02 ,  F28D7/16 ,  F28D1/053

CPC分类号： F28F9/0202 ,  F02B29/0462 ,  F28D1/05366 ,  F28D7/1676 ,  F28D7/1692 ,  F28D2001/0273 ,  F28D2021/0082 ,  F28F1/022 ,  F28F2250/02 ,  Y02T10/146

摘要： A heat-exchanger assembly (10), which can be advantageously employed as an intercooler for an air-charging system for an internal combustion engines includes a plurality of generally wedge-shaped coolant tubes (16,116) through which coolant is directed for effecting cooling of compressed air flowing about the tubes. In order to promote efficient operation, each of the wedge-shaped cooling tubes (16,116) includes a plurality of coolant passages (32,132) of substantially identical hydraulic diameter or cross-sectional area, thereby promoting uniform flow of coolant through each coolant tube. Each coolant tube (16,116) includes outer walls which may be of a substantially uniform thickness, or which may increase in thickness across the width of the tube.

摘要翻译： 可以有利地用作用于内燃机的空气充气系统的中间冷却器的热交换器组件（10）包括多个大致楔形的冷却剂管（16,116），冷却剂通过该多个冷却剂管引导以实现冷却 围绕管流动的压缩空气。 为了促进有效的操作，每个楔形冷却管（16,116）包括具有基本相同的水力直径或横截面面积的多个冷却剂通道（32,132），从而促进冷却剂通过每个冷却剂管的均匀流动。 每个冷却剂管（16,116）包括外壁，其可以具有基本上均匀的厚度，或者可以在管的宽度上增加厚度。

公开(公告)号：EP0792683B1

公开(公告)日：2003-06-25

申请号：EP97103093.7

申请日：1997-02-26

申请人： PRAXAIR TECHNOLOGY, INC.

发明人： Kingsley, Jeffrey Paul

IPC分类号： B01J19/18 ,  B01J10/00 ,  B01J14/00 ,  B01J19/00

CPC分类号： C07C51/235 ,  B01J8/22 ,  B01J14/00 ,  B01J19/0013 ,  B01J19/006 ,  B01J19/0066 ,  B01J19/18 ,  B01J19/1875 ,  B01J2219/00081 ,  B01J2219/00085 ,  B01J2219/00094 ,  B01J2219/00103 ,  B01J2219/0011 ,  B01J2219/00768 ,  B01J2219/00779 ,  F28D7/1676 ,  F28D2021/0022 ,  F28F27/02

摘要： A shell and tube heat exchanger reactor with forced circulation is used to improve heat and mass transfer for exothermic liquid-liquid, gas-liquid and gas-liquid-solid reactions. Enhanced productivity and selectivity are obtained.

公开(公告)号：EP4421151A1

公开(公告)日：2024-08-28

申请号：EP23165609.1

申请日：2023-03-30

申请人： Linde GmbH ,  BASF SE ,  ARVOS GmbH ,  SABIC Global Technologies B.V.

发明人： Sinn, Tobias ,  Eberstein, Christopher ,  Bruder, David ,  Zellhuber, Mathieu ,  Schmidt, Gunther ,  Haunert, Andrea ,  Hetzer, Jens ,  Linnenkohl, Andreas ,  Schlieter, Thorsten ,  Stückrath, Karsten ,  Weidenfeller, Jörg ,  Broekhuis, Robert Roger ,  Schroer, Joseph William

IPC分类号： C10G9/00 ,  C10G9/36 ,  F28D7/10 ,  F28D7/16

CPC分类号： C10G9/002 ,  C10G9/36 ,  C10G2400/2020130101 ,  F28D2021/007520130101 ,  F28D7/106 ,  F28D7/1676 ,  F28D7/0075 ,  F28F9/0273

摘要： A method to produce olefins comprising preheating a reaction feed, firing a conversion reactor, subjecting the reaction feed to a conversion in the conversion reactor, withdrawing a product gas from the conversion reactor, and cooling the product gas withdrawn from the conversion reactor is proposed, wherein said preheating and said cooling comprises transferring heat from said product gas or a part thereof to said reaction feed or a part thereof using a thermal energy recovery assembly comprising one or more inner passages and one or more outer passages coaxially surrounding said inner passage(s), said preheating and said cooling further comprises passing said reaction feed or said part thereof through said outer passage(s) of said thermal energy recovery assembly and passing said product gas or said part thereof through said inner passage(s) of said thermal energy recovery assembly, said thermal energy recovery assembly comprises one or more heat transfer enhancement structures to enhance heat transfer from said inner passage(s) to said outer passage(s), said firing the reactor comprises providing an oxidator gas at an oxidator gas temperature level of more than 400 °C using an oxidator gas preheating system and combusting a fuel gas comprising hydrogen using said oxidator gas at the fuel gas temperature level, and said thermal energy recovery assembly is configured to meet a set of operating constraints including a first temperature constraint relating to an outside temperature of a containment of said inner passage of said thermal energy recovery assembly and a second temperature constraint relating to an inside temperature of the containment of said inner passage of said thermal energy recovery assembly. Corresponding apparatus is also disclosed.