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1.发明公开High capacity purification of thermally unstable compounds 审中-公开HochleistungsfähigeReinigung thermisch instabiler Verbindungen
公开(公告)号：EP1426086A1
公开(公告)日：2004-06-09
申请号：EP03257278.6
申请日：2003-11-18
摘要： Separations processes and apparati capable of purifying thermally sensitive materials at high capacity. An apparatus having a rectification section (3) and a stripping section (4) with the stripping section (4) having a stripping tray (1020) with 5 to 50 % open area (1000), a pressure drop from 0.02 psi to 0.2 psi and a tray efficiency during operation of the column which is equal to or greater than 20%.
摘要翻译： 分离过程和装置能够以高容量净化热敏材料。 一种具有精馏段（3）和汽提部分（4）的装置，其中汽提部分（4）具有汽提塔板（1020），其具有5至50％开放面积（1000），压降为0.02psi至0.2psi 以及塔的操作期间的托盘效率等于或大于20％。
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2.发明授权VERTICAL STAGED POLYCONDENSATION REACTOR CONTAINING SPLIT FLOW REACTOR TRAYS 失效垂直PROGRESSIVE缩聚反应器含楼层，分流
公开(公告)号：EP0758266B1
公开(公告)日：1998-07-22
申请号：EP95918269.2
申请日：1995-04-21
CPC分类号： B01J19/24 , B01D3/166 , B01D3/20 , B01D3/24 , B01J19/006 , B01J2219/00085 , B01J2219/00135 , B01J2219/00166 , B01J2219/00168 , B01J2219/0077 , B01J2219/00777
摘要： This invention relates to a vertically disposed polymerization reactor (2) having a series of essentially circular tray assemblies (10); each tray assembly (10) having a central open vapor chimney (18) and two split-flow paths (26) each split-flow path (26) containing one reverse flow path wherein the liquid polymer flow is reversed by means of a substantially semi-circular turnaround region (24); said trays (10) having a liquid polymer tray inlet (14) and a liquid polymer tray outlet (16) for conducting a flow of the liquid polymer by means of a hyraulic gradient; each tray assembly (10) being open at the top for escape of vapor from the liquid polymer flow to the central open vapor chimney (18); and said trays (10) arranged in vertical disposition one above the other.
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公开(公告)号：EP1800726A4
公开(公告)日：2010-07-14
申请号：EP05772551
申请日：2005-08-15
申请人： KANSAI CHEM ENG
IPC分类号： B01D3/26
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4.发明公开Process for carrying out mass transfer between a liquid phase and a gaseous phase 审中-公开Prozessfürden Stoffaustausch zwischen einerFlüssigphaseund einer Gasphase
公开(公告)号：EP1733773A1
公开(公告)日：2006-12-20
申请号：EP05013121.8
申请日：2005-06-17
申请人： METHANOL CASALE S.A.
发明人： Filippi, Ermanno , Tarozzo, Mirco , Rizzi, Enrico
CPC分类号： B01J8/0415 , B01D3/141 , B01D3/16 , B01D3/166 , B01D3/22 , B01J8/0496 , B01J2208/0015
摘要： A process for carrying out mass transfer between a liquid phase (Fl) and a gaseous phase (Fg) in a filled-type column comprising an outer shell (2) in which at least one basket (3a,3b) is housed for containing the filling crossed by said phases is distinguished in that it comprises the step of subjecting said liquid phase (Fl) and said gaseous phase (Fg) to an indirect heat exchange (21) in said at least one basket (3a,3b) through at least one heat exchanger (21) embedded in said filling. In such a way increased mass transfer efficiency between the aforementioned phases is achieved with the consequent possibility of reduction of the size of the column intended to carry out such a process.
摘要翻译： 在包括外壳（2）的填充柱中的液相（F1）和气相（Fg）之间进行质量传递的方法，其中容纳至少一个筐（3a，3b）以容纳 不同之处在于，所述相交叉的填充的区别在于，其包括使所述液相（F1）和所述气相（Fg）在所述至少一个筐（3a，3b）中经由至少一个筐（3a，3b）中的间接热交换 一个热交换器（21）嵌入所述填充物中。 以这种方式提高上述相之间的传质效率，从而降低了旨在实施这种方法的色谱柱尺寸的可能性。
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公开(公告)号：EP0277230A1
公开(公告)日：1988-08-10
申请号：EP87906486.0
申请日：1987-07-28
CPC分类号： B01D3/10 , B01D3/146 , B01D3/166 , B01D3/30 , B01D3/38 , B01D3/4261 , B01J19/1862 , B01J2219/00063 , B01J2219/00065 , B01J2219/00069 , B01J2219/00083 , B01J2219/00103 , B01J2219/00132 , B01J2219/00155 , B01J2219/00162 , B01J2219/00164 , B01J2219/00168 , B01J2219/00182 , C11C3/12
摘要： Améliorations concernant la détermination et la régulation d'un procédé d'hydrogénation en continu, consistant à obtenir des courbes de viscosité et des courbes d'opacité pour les comparer à des courbes connues d'insaturation d'hydrogène et des caractéristiques de plasticité. Avec un équipement amélioré d'hydrogénation permettant de mettre en oeuvre la réaction d'hydrogénation en continu en combinaison avec des stations de prévention d'auto-oxydation et de désodorisation, la présente invention fournit un procédé global et les commandes pour réaliser une hydrogénation précise d'huiles comestibles.
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公开(公告)号：EP2067512A2
公开(公告)日：2009-06-10
申请号：EP09152870.3
申请日：2003-11-18
摘要： Separations processes and apparati capable of purifying thermally sensitive materials at high capacity. An apparatus having a rectification section and a stripping section with the stripping section having a stripping tray with 5 to 50 % open area, a pressure drop from 0.02 psi to 0.2 psi and a tray efficiency during operation of the column which is equal to or greater than 20%.
摘要翻译： 分离过程和设备能够以高容量净化热敏性材料。 具有精馏段和汽提段的装置，其中汽提段具有汽提塔盘，其具有5-50％的开口面积，0.02psi至0.2psi的压降和塔运行期间塔盘效率等于或大于 超过20％。
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公开(公告)号：EP0758266A1
公开(公告)日：1997-02-19
申请号：EP95918269.0
申请日：1995-04-21
CPC分类号： B01J19/24 , B01D3/166 , B01D3/20 , B01D3/24 , B01J19/006 , B01J2219/00085 , B01J2219/00135 , B01J2219/00166 , B01J2219/00168 , B01J2219/0077 , B01J2219/00777
摘要： This invention relates to a vertically disposed polymerization reactor (2) having a series of essentially circular tray assemblies (10); each tray assembly (10) having a central open vapor chimney (18) and two split-flow paths (26) each split-flow path (26) containing one reverse flow path wherein the liquid polymer flow is reversed by means of a substantially semi-circular turnaround region (24); said trays (10) having a liquid polymer tray inlet (14) and a liquid polymer tray outlet (16) for conducting a flow of the liquid polymer by means of a hyraulic gradient; each tray assembly (10) being open at the top for escape of vapor from the liquid polymer flow to the central open vapor chimney (18); and said trays (10) arranged in vertical disposition one above the other.
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公开(公告)号：EP0277230A4
公开(公告)日：1989-10-12
申请号：EP87906486
申请日：1987-07-28
申请人： RIVERS JACOB BOYD JR
发明人： RIVERS JACOB BOYD JR
IPC分类号： B01D3/10 , B01D3/14 , B01D3/16 , B01D3/30 , B01D3/38 , B01D3/42 , B01J19/18 , C11C3/12 , B01D3/00 , B01D17/00 , C11C3/02
CPC分类号： B01D3/10 , B01D3/146 , B01D3/166 , B01D3/30 , B01D3/38 , B01D3/4261 , B01J19/1862 , B01J2219/00063 , B01J2219/00065 , B01J2219/00069 , B01J2219/00083 , B01J2219/00103 , B01J2219/00132 , B01J2219/00155 , B01J2219/00162 , B01J2219/00164 , B01J2219/00168 , B01J2219/00182 , C11C3/12
摘要： Improvements in determining and controlling a continuous hydrogenation process comprising the obtaining of viscosity operating curves and opacity operating curves for comparison to known hydrogen unsaturation curves and plasticity characterics. With improved hydrogenation equipment for carrying out the continuous hydrogenation reaction in combination with deodorization and auto-oxydation prevention stations, the present invention provides an overall process and controls for precision hydrogenation of edible oils.
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公开(公告)号：EP2780093A1
公开(公告)日：2014-09-24
申请号：EP12784023.9
申请日：2012-11-14
申请人： BASF SE
CPC分类号： B01D3/324 , B01D3/166 , B01D3/18 , B01D3/22 , B01F3/04468 , B01F3/04496
摘要： The invention relates to a base for a mass transfer column, comprising gas through-openings which are distributed over the base (1) and at least one baffle plate (11) for directing the flow of liquid flowing on the base, said base (1) being loadable with a liquid via at least one inlet (3). The base has at least one inlet (3), at least one separating weir (5) which separates the inflowing liquid into two flows, and at least two outlets (12) or at least two inlets (3) and at least one outlet (12) for the liquid. Each flow flows along a flow path (7; 9) to an outlet (12). The invention further relates to a mass transfer column which contains the base and to a use of the base and the mass transfer column.
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公开(公告)号：EP1800726A1
公开(公告)日：2007-06-27
申请号：EP05772551.7
申请日：2005-08-15
发明人： NODA, Hideo,KANSAI CHEMICAL ENGINEERING CO.,LTD. , YAMAJI, H.,KANSAI CHEMICAL ENGINEERING CO. LTD. , KURATANI, N.,KANSAI CHEMICAL ENGINEERING CO. LTD , KATAOKA, Kunio, KANSAI CHEMICAL ENGINEERING CO.LTD
IPC分类号： B01D3/26
摘要： The present invention provides a multi-structured internal heat exchange-type distillation column comprising at least an outermost heat exchange section, an intermediate section, and an innermost heat exchange section, in which the innermost heat exchange section is isolated from the intermediate section, the outermost heat exchange section is also isolated from the intermediate section, the outermost heat exchange section and the innermost heat exchange section are in communication with one another through at least two vapor tunnel connecting ports, a channel is formed inside the outermost heat exchange section in such a manner that, in a case where at least one of the vapor tunnel connecting ports serves as an inlet for vapor from the innermost heat exchange section into the outermost heat exchange section, and the other vapor tunnel connecting port serves as an outlet for vapor from the outermost heat exchange section back to the innermost heat exchange section, the vapor can smoothly flow in one-way traffic from the inlet toward the outlet, and either the outermost heat exchange section and the innermost heat exchange section, or the intermediate section, is a rectifying section, and the other is a stripping section. The distillation column of the present invention has excellent efficiency of internal heat exchange.
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