公开(公告)号：EP1828084B1

公开(公告)日：2008-06-18

申请号：EP05850281.6

申请日：2005-12-15

申请人： Uhde GmbH

发明人： HAFENSCHER, Harald ,  WEIS, Reinhold ,  BENJE, Michael

IPC分类号： C07C17/02 ,  C07C19/045

CPC分类号： B01J19/2435 ,  B01F3/04503 ,  B01F5/0206 ,  B01F5/0451 ,  B01F5/0456 ,  B01F5/106 ,  B01J19/0053 ,  C07C17/02 ,  C07C19/045

摘要： The invention relates to a method for producing high-purity 1,2-dichloroethane from dissolved chlorine and dissolved ethylene which are brought into contact with each other using a circulating liquid reaction medium which essentially consists of 1,2-dichloroethane and a catalyst and passes through at least one vertical reaction loop. The two limbs of the loop are connected to a gas-phase stripping container which is arranged at the top and from which the reaction product is outwardly transferred either in a gaseous or liquid form or both in a gaseous form and in a liquid form. The addition points for the addition of chlorine and dissolved ethylene are arranged in the limb of the loop in which the liquid rises. The addition point for dissolved chlorine is always arranged downstream of the ethylene addition point. At least one addition point for liquid 1,2-dichloroethane follows each chlorine addition point, and the addition of the liquid 1,2-dichloroethane is carried out under kinetic energy which is high enough to enable a vigorous mixture of 1,2-dichloroethane, dissolved chlorine and ethylene to be carried out. Preferably, the liquid 1,2-dichloroethane is added by means of at least one jet mixer.

公开(公告)号：EP1919603A2

公开(公告)日：2008-05-14

申请号：EP06795829.8

申请日：2006-08-30

申请人： The Procter and Gamble Company

发明人： WILLIAMS, Roger, Phillip ,  MCLAUGHLIN, Jon, Kevin

IPC分类号： B01F15/04 ,  B01F13/10 ,  G05D11/13 ,  G05B19/19 ,  F04B13/02

CPC分类号： F04B13/02 ,  B01F5/0453 ,  B01F5/0456 ,  B01F13/1055 ,  B01F15/042 ,  G05D11/132

摘要： An apparatus (10) and method for combining multiple materials into a stream. The multiple materials may include both a major material and one or more minor materials. The minor materials are added using inlet tubes (141) . The major and minor materials are added at transient or steady state flow rates, depending upon a command from a control signal . The apparatus and method utilize a control system which does not have flow control valves, flow control feedback loops or a dynamic mix tank. The actual flow rates track the commanded flow rates, but deviate by an error. The claimed arrangement provides a time-based error believed to be unobtainable in the prior art.

公开(公告)号：EP1645316A3

公开(公告)日：2007-09-05

申请号：EP05024832.7

申请日：2001-06-06

申请人： Toyota Jidosha Kabushiki Kaisha

发明人： Shimazu, Takashi

IPC分类号： B01B1/00 ,  B01F3/02 ,  B01J19/24 ,  C01B3/48 ,  F28C3/08 ,  F28D9/00 ,  F28D21/00 ,  F28F13/00 ,  H01M8/06

CPC分类号： H01M8/0631 ,  B01B1/005 ,  B01F3/022 ,  B01F3/04049 ,  B01F5/0453 ,  B01F5/0456 ,  B01F2005/0034 ,  B01J4/002 ,  B01J8/0278 ,  B01J8/0492 ,  B01J8/0496 ,  B01J19/2485 ,  B01J19/249 ,  B01J19/26 ,  B01J2208/00168 ,  B01J2208/00194 ,  B01J2208/00212 ,  B01J2208/00362 ,  B01J2208/0053 ,  B01J2208/00849 ,  B01J2219/00087 ,  B01J2219/00092 ,  B01J2219/00096 ,  B01J2219/00117 ,  B01J2219/00128 ,  B01J2219/00159 ,  B01J2219/00763 ,  B01J2219/2453 ,  B01J2219/2458 ,  B01J2219/2459 ,  B01J2219/2462 ,  B01J2219/2485 ,  C01B3/16 ,  C01B3/48 ,  C01B2203/0205 ,  C01B2203/0227 ,  C01B2203/0283 ,  C01B2203/0288 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0844 ,  C01B2203/085 ,  C01B2203/0883 ,  C01B2203/0894 ,  C01B2203/12 ,  C01B2203/1205 ,  C01B2203/1223 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/1276 ,  C01B2203/1294 ,  C01B2203/1604 ,  C01B2203/1638 ,  C01B2203/82 ,  F28C3/08 ,  F28D7/1615 ,  F28D9/0062 ,  F28D9/0093 ,  F28D21/0015 ,  F28D2021/0043 ,  F28F13/003 ,  F28F13/187 ,  H01M8/0612 ,  H01M8/0618

摘要： A fuel reforming apparatus (20) for reforming hydrocarbon-based fuel into hydrogen-rich fuel gas comprises a reforming reactor (30) for reforming the hydrocarbon-based fuel into a reformed gas containing hydrogen and carbon monoxide; a water gas shift reactor (34) for converting steam and carbon monoxide into hydrogen and carbon dioxide; a connector (32) for connecting the reforming reactor (30) and the water gas shift reactor (34) to allow the reformed gas from the reforming reactor (30) to be fed to the water gas shift reactor (32), the connector including a reformed gas permeable member disposed proximate to the reforming reactor (30); and liquid water feeding means (31) for feeding liquid water to the reformed gas permeable member. The reformed gas permeable member has a plurality of gaps or capillaries capable of passing the reformed gas from the reforming reactor (30).

公开(公告)号：EP1726355A3

公开(公告)日：2007-08-01

申请号：EP06008568.5

申请日：2006-04-25

申请人： Linde Aktiengesellschaft

发明人： Obermeyer, Heinz-Dieter, Dr. ,  Ranke, Harald, Dr. ,  Reinhardt, Hans-Jürgen, Dr. ,  Wellenhofer, Anton

IPC分类号： B01F3/02 ,  B01F5/04

CPC分类号： B01F3/02 ,  B01F5/0453 ,  B01F5/0456 ,  B01F5/0463 ,  B01F2005/0034

摘要： Die Erfindung betrifft ein Verfahren und eine Vorrichtung zum Mischen eines ersten und eines zweiten Gases mit einer Hauptleitung (1) zur Führung des ersten Gases, einer Zuleitung (4) für das zweite Gas, wobei sich die Zuleitung (4) bis in das Innere der Hauptleitung (1) erstreckt und an ihrem Ende im Wesentlichen parallel zur Symmetrieachse (5) der Hauptleitung (1) verläuft, und einem Düsenkopf (6), der an seinem hinteren Ende (8) mit der Zuleitung (4) verbunden ist. Der Düsenkopf (6) besitzt Austrittskanäle (13) für das zweite Gas, die um einen Winkel zwischen 15° und 75° gegen die Symmetrieachse (5) der Hauptleitung (1) geneigt sind.

公开(公告)号：EP1784251A1

公开(公告)日：2007-05-16

申请号：EP04764808.4

申请日：2004-09-03

申请人： Crenano Gmbh

发明人： SCHÜLER, Rolf

IPC分类号： B01F3/08 ,  B01F3/04 ,  B01F3/12 ,  B01F5/06 ,  B01F5/04 ,  B01J19/24

CPC分类号： B01F3/0807 ,  B01D19/0094 ,  B01F3/0446 ,  B01F3/0815 ,  B01F3/12 ,  B01F5/0415 ,  B01F5/0453 ,  B01F5/0456 ,  B01F5/0611 ,  B01F5/0646 ,  B01F5/0655 ,  B01F2005/0034 ,  B01F2005/0631 ,  B01F2005/0634 ,  B01F2005/0637 ,  B01F2215/0052 ,  B01F2215/0098 ,  C02F1/20 ,  C02F1/34 ,  C02F2103/42 ,  C02F2303/04

摘要： The invention relates to a device for the molecular integration or disintegration of solid, liquid and/or gaseous flowing, entrained and/or countercurrent components by means of cavitation in order to modify, build or disintegrate molecular compounds. The invention allows to obtain stable mixtures from immiscible or difficult-to-mix components or to separate such mixtures. The supercavitation molecular reactor allows to build up or disintegrate or modify, with low expenditure in terms of energy, even complex compounds that so far have not been accessible to modification and/or production or only by very extensive multiple processes and a large amount of technical complexity.

公开(公告)号：EP1726355A2

公开(公告)日：2006-11-29

申请号：EP06008568.5

申请日：2006-04-25

申请人： Linde Aktiengesellschaft

发明人： Obermeyer, Heinz-Dieter, Dr. ,  Ranke, Harald, Dr. ,  Reinhardt, Hans-Jürgen, Dr. ,  Wellenhofer, Anton

IPC分类号： B01F3/02 ,  B01F5/04

CPC分类号： B01F3/02 ,  B01F5/0453 ,  B01F5/0456 ,  B01F5/0463 ,  B01F2005/0034

摘要： Die Erfindung betrifft ein Verfahren und eine Vorrichtung zum Mischen eines ersten und eines zweiten Gases mit einer Hauptleitung (1) zur Führung des ersten Gases, einer Zuleitung (4) für das zweite Gas, wobei sich die Zuleitung (4) bis in das Innere der Hauptleitung (1) erstreckt und an ihrem Ende im Wesentlichen parallel zur Symmetrieachse (5) der Hauptleitung (1) verläuft, und einem Düsenkopf (6), der an seinem hinteren Ende (8) mit der Zuleitung (4) verbunden ist. Der Düsenkopf (6) besitzt Austrittskanäle (13) für das zweite Gas, die um einen Winkel zwischen 15° und 75° gegen die Symmetrieachse (5) der Hauptleitung (1) geneigt sind.

摘要翻译： 在混合两种气体的过程中，第一气体（15）流过主管（1）并且第二气体经由次级管道（4）进料到喷射头（6），在喷射头（6）中被分为更小的流（16 ）。 然后将第二气体的部分流动以15度和75度之间的角度释放到第一气体（15）的迎面而来的流动中。 二次气流（16）没有旋转矢量。 主要气体是空气，二级气体是氧气。 空气以1000-200000m 3 /小时的速率与氧气以5000-100000m 3 /小时混合。 包括气体混合组件的独立权利要求。

公开(公告)号：EP1162171B1

公开(公告)日：2005-11-16

申请号：EP01113836.9

申请日：2001-06-06

申请人： Toyota Jidosha Kabushiki Kaisha

发明人： Shimazu, Takashi

IPC分类号： C01B3/48

CPC分类号： H01M8/0631 ,  B01B1/005 ,  B01F3/022 ,  B01F3/04049 ,  B01F5/0453 ,  B01F5/0456 ,  B01F2005/0034 ,  B01J4/002 ,  B01J8/0278 ,  B01J8/0492 ,  B01J8/0496 ,  B01J19/2485 ,  B01J19/249 ,  B01J19/26 ,  B01J2208/00168 ,  B01J2208/00194 ,  B01J2208/00212 ,  B01J2208/00362 ,  B01J2208/0053 ,  B01J2208/00849 ,  B01J2219/00087 ,  B01J2219/00092 ,  B01J2219/00096 ,  B01J2219/00117 ,  B01J2219/00128 ,  B01J2219/00159 ,  B01J2219/00763 ,  B01J2219/2453 ,  B01J2219/2458 ,  B01J2219/2459 ,  B01J2219/2462 ,  B01J2219/2485 ,  C01B3/16 ,  C01B3/48 ,  C01B2203/0205 ,  C01B2203/0227 ,  C01B2203/0283 ,  C01B2203/0288 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0844 ,  C01B2203/085 ,  C01B2203/0883 ,  C01B2203/0894 ,  C01B2203/12 ,  C01B2203/1205 ,  C01B2203/1223 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/1276 ,  C01B2203/1294 ,  C01B2203/1604 ,  C01B2203/1638 ,  C01B2203/82 ,  F28C3/08 ,  F28D7/1615 ,  F28D9/0062 ,  F28D9/0093 ,  F28D21/0015 ,  F28D2021/0043 ,  F28F13/003 ,  F28F13/187 ,  H01M8/0612 ,  H01M8/0618

公开(公告)号：EP0504550B1

公开(公告)日：1996-05-15

申请号：EP92100975.9

申请日：1992-03-10

申请人： H.KRANTZ - TKT Gesellschaft mit beschränkter Haftung

发明人： Staeckling, Frank ,  Griepentrog, Joachim

IPC分类号： B01F5/04

CPC分类号： B01F5/0456 ,  B01F5/0453 ,  B01F5/0458

公开(公告)号：EP3364004A1

公开(公告)日：2018-08-22

申请号：EP16855132.3

申请日：2016-05-27

申请人： Yanmar Co., Ltd.

发明人： INOUE Tsuyoshi ,  KOBAYASHI Ryota

IPC分类号： F01N3/08 ,  F01N3/24

CPC分类号： F01N3/2892 ,  B01F3/04049 ,  B01F5/0451 ,  B01F5/0456 ,  B01F5/0616 ,  B01F5/0618 ,  B01F2005/0628 ,  B01F2005/0637 ,  B01F2005/0638 ,  B01F2005/0639 ,  F01N3/2066 ,  F01N3/24 ,  F01N13/0093 ,  F01N2240/20 ,  F01N2340/02 ,  F01N2590/02 ,  F01N2610/02 ,  F01N2610/1453 ,  Y02T10/24

摘要： An object of this invention is to provide an exhaust gas purification device with which a decrease in reduction (denitrification) efficiency can be reduced. An exhaust gas purification device of this invention for a ship 1 includes: a reducing agent injector 61 of a reducing agent supply device supplying a reducing agent to an exhaust gas passing through an exhaust pipe of an engine 21 to be mounted in the ship; an exhaust mixer 62 mixing the exhaust gas and the reducing agent in a location downstream of the reducing agent injector 61 in an exhaust gas traveling direction; and selective catalytic reduction devices 34, 35 facilitating reduction of NOx in the exhaust gas of the engine 21 in a location downstream of the exhaust mixer 62 in the exhaust gas traveling direction. Multiple reducing agent injectors 61 are provided, and respectively have injection ports arranged at equal intervals along a circumferential direction of the exhaust pipe.

公开(公告)号：EP2799402B1

公开(公告)日：2018-03-07

申请号：EP12850865.2

申请日：2012-11-21

申请人： Gomes De Oliveira, João Carlos ,  Gomes De Oliveira Netto, Procópio ,  Gomes De Oliveira, Felipe

发明人： Gomes De Oliveira, João Carlos ,  Gomes De Oliveira Netto, Procópio ,  Gomes De Oliveira, Felipe

IPC分类号： C02F1/24 ,  C02F1/52 ,  C02F1/56 ,  C02F7/00 ,  C02F9/00 ,  E02B3/02

CPC分类号： C02F9/00 ,  B01F5/0456 ,  B01F13/0255 ,  B03D1/1462 ,  B03D1/24 ,  C02F1/006 ,  C02F1/24 ,  C02F1/52 ,  C02F1/5281 ,  C02F1/56 ,  C02F7/00 ,  C02F2103/001 ,  C02F2103/007 ,  E02B1/003 ,  E02B3/02 ,  E02B3/023 ,  E02B5/085 ,  E02B8/023 ,  Y02A10/28 ,  Y02W10/15

摘要： "IMPROVEMENT ON FACILITY FOR REMOVAL OF MATERIALS AND / OR POLLUTING SUBSTANCES CONTAINED IN WATERCOURSES", applied to facility comprising : the implementation of a sandbox arranged at the bottom and in a stretch of the watercourse, followed by a floating garbage fence arranged substantially transversely to the watercourse; whereas downstream and at a certain distance from this garbage fence is provided a suspended and transverse metallic structure to the watercourse, in which curtains for selective injection and automatically set in motion are mounted, arranged spaced and interspersed by homogenization diffusers, these curtains are responsible for the injection of coagulants; by the injection of polymers into the watercourse to be treated, and ahead there is a phase for release of microbubbles of air, causing a flotation of these aggregate particles; allowing that from this flotation stretch arises, along the watercourse, a superficial agglomeration of the floated material, and the conduction by flexible and longitudinal barriers formed by synthetic membranes of this floated material to a transverse alignment of dredging modules, that extend through the entire watercourse's width promoting the concentration of floated material and its removal. This improvement consisting of all equipment (3, 4,7) originally installed transversally the watercourse, which are subject to partial or total removal from this transverse condition, allowing the clearance of part and/or entire bed of the watercourse.