中科微点-全球专利检索

  1. Login
  2. Sign Up

Search Results

33 records (took 0.021 seconds)

    MULTI-TUBE FIXED-BED REACTOR, ESPECIALLY FOR CATALYTIC GAS PHASE REACTIONS
    2.
    发明申请
    MULTI-TUBE FIXED-BED REACTOR, ESPECIALLY FOR CATALYTIC GAS PHASE REACTIONS 审中-公开
    管式反应器，尤其气相催化反应的

    公开(公告)号：WO0054877A3

    公开(公告)日：2001-04-05

    申请号：PCT/EP0002304

    申请日：2000-03-15

    Applicant: BASF AG ,  OLBERT GERHARD ,  CORR FRANZ ,  REUTER PETER ,  WAMBACH LUDWIG ,  HAMMON ULRICH

    Inventor： OLBERT GERHARD ,  CORR FRANZ ,  REUTER PETER ,  WAMBACH LUDWIG ,  HAMMON ULRICH

    IPC: B01J8/06 ,  B01J19/00 ,  B01J19/24 ,  C07C45/35 ,  C07C45/38

    CPC classification number: C07C45/35 ,  B01J8/067 ,  B01J19/0013 ,  B01J19/2425 ,  B01J2208/00212 ,  B01J2208/00221 ,  B01J2208/00256 ,  B01J2219/00094 ,  B01J2219/00103 ,  C07C45/38 ,  C07C47/22 ,  C07C47/127

    Abstract: The invention relates to a multi-tube fixed-bed reactor and to the use of a reactor of this type for carrying out catalytic gas phase reactions, especially for carrying out exothermic or endothermic catalytic gas phase reactions such as producing phthalic anhydride (PSA), acrylic acid (AA), methacrylic acid (MAA), acrolein, maleic anhydride (MSA), glyoxal, phosgene, hydrogen cyanide or vinyl formamide (VFA). According to the invention, in the case of larger reactors where a considerable reaction heat is produced or required and must be dissipated as a result of the numerous reaction tubes (17), the ratio of tube distribution t to tube outer diameter d?a? is made dependant on the reactor diameter or the tube bundle diameter d?RBa?. If the outer diameter of the reaction tube bundle (18) is more than 4 metres, a ratio of tube distribution t to tube outer diameter d?a? of at least 1.3 is preferred.

    Abstract translation: 本发明涉及一种管束反应器和用于进行气相催化反应，特别是用于进行放热或吸热催化气相反应如生产Phthalsälureanhydrid（PSA），丙烯酸（AA），甲基丙烯酸（MAA），丙烯醛，马来酸酐的使用这样的反应器中的（ MSA），乙二醛，光气，氢氰酸或乙烯基甲酰胺（VFA）。 根据本发明，在较大的反应器，其中，这是因为许多反应管（17）的已被获得的反应的高的热或需要，管间距的比率管外径d·A· 在反应器直径或管束外径d？RBA？ 让他们依赖。 具有大于4米反应管束（18）的外直径，管间距吨到管外径d的比·A· 优选为至少1.3。

    COUNTERFLOW REACTOR WITH A BUNDLE OF CONTACT TUBES
    3.
    发明申请
    COUNTERFLOW REACTOR WITH A BUNDLE OF CONTACT TUBES 审中-公开
    与联系人管逆流反应器

    公开(公告)号：WO0187476A8

    公开(公告)日：2001-12-13

    申请号：PCT/EP0104975

    申请日：2001-05-03

    Applicant: BASF AG ,  OLBERT GERHARD ,  CORR FRANZ

    Inventor： OLBERT GERHARD ,  CORR FRANZ

    IPC: C07D307/60 ,  B01J19/00 ,  B01J19/24 ,  C07C45/35 ,  C07C47/127 ,  C07C47/22 ,  C07C51/215 ,  C07C51/25 ,  C07C51/265 ,  C07C57/04 ,  C07C57/05 ,  C07D307/89 ,  F28F27/02 ,  C07D401/06 ,  C07D401/12 ,  C07D401/14 ,  C07D405/14

    CPC classification number: C07C51/252 ,  B01J19/0013 ,  B01J19/2425 ,  B01J2219/00094 ,  B01J2219/00103 ,  C07C45/35 ,  C07C47/127 ,  C07C51/215 ,  C07C51/265 ,  F28F27/02 ,  C07C47/22 ,  C07C57/145 ,  C07C57/04 ,  C07C63/16

    Abstract: The invention relates to a reactor (1) comprising a bundle of contact tubes (2). A heat-exchanging medium is guided through the area surrounding the contact tubes. Both ends of the reactor have annular ducts (3,4) with jacket orifices (5,6) for supplying or educting a heat-exchanging medium by means of at least one pump, optionally transferring the heat-exchanging medium or a partial current of the heat-exchanging medium via at least one external heat exchanger. The heat exchanging medium is fed to the lower annular duct (4) and is returned to the pump(s) via the upper annular duct (3). Deviating discs (7) alternately leave open a passage diameter at the centre or at the edge of the reactor. The lower annular duct (4) is split into two zones by means of a horizontal partition (8), said two zones communicating with each other via preferably homogeneously divided openings (9) with adjustable passage diameters.

    Abstract translation: 公开的是（1）具有接触管束（2），围绕通过该接触管的热交换介质循环回路与塞环线路通过一个反应器（3，4）在有夹套的孔的反应器的两端（5,6），用于传热介质的供给和排出 借助于一个或多个泵返回合适的话与所述热交换介质的转移或通过一个或多个外部热交换器中的热交换介质的一个子流，其特征在于，供给到下环形管线的热交换装置（4），并通过所述上部环线（3）（于）泵（一个或多个） 是，并用在反应器中心偏转板（7）交替和离开在反应器边缘，其中，所述下环形管线（4）由水平隔板（8）分成两个区域释放一个通道横截面，彼此（通过优选均匀分布的开口9 ）具有可调节的通道横截面连通。

    COUNTERFLOW REACTOR WITH A BUNDLE OF CONTACT TUBES
    4.
    发明申请
    COUNTERFLOW REACTOR WITH A BUNDLE OF CONTACT TUBES 审中-公开
    具有接触管束的逆流反应器

    公开(公告)号：WO0187476A1

    公开(公告)日：2001-11-22

    申请号：PCT/EP0104975

    申请日：2001-05-03

    Applicant: BASF AG ,  OLBERT GERHARD ,  CORR FRANZ

    Inventor： OLBERT GERHARD ,  CORR FRANZ

    IPC: C07D307/60 ,  B01J19/00 ,  B01J19/24 ,  C07C45/35 ,  C07C47/127 ,  C07C47/22 ,  C07C51/215 ,  C07C51/25 ,  C07C51/265 ,  C07C57/04 ,  C07C57/05 ,  C07D307/89 ,  F28F27/02 ,  C07D401/06 ,  C07D401/12 ,  C07D401/14 ,  C07D405/14

    CPC classification number: C07C51/252 ,  B01J19/0013 ,  B01J19/2425 ,  B01J2219/00094 ,  B01J2219/00103 ,  C07C45/35 ,  C07C47/127 ,  C07C51/215 ,  C07C51/265 ,  F28F27/02 ,  C07C47/22 ,  C07C57/145 ,  C07C57/04 ,  C07C63/16

    Abstract: The invention relates to a reactor (1) comprising a bundle of contact tubes (2). A heat-exchanging medium is guided through the area surrounding the contact tubes. Both ends of the reactor have annular ducts (3,4) with jacket orifices (5,6) for supplying or educting a heat-exchanging medium by means of at least one pump, optionally transferring the heat-exchanging medium or a partial current of the heat-exchanging medium via at least one external heat exchanger. The heat exchanging medium is fed to the lower annular duct (4) and is returned to the pump(s) via the upper annular duct (3). Deviating discs (7) alternately leave open a passage diameter at the centre or at the edge of the reactor. The lower annular duct (4) is split into two zones by means of a horizontal partition (8), said two zones communicating with each other via preferably homogeneously divided openings (9) with adjustable passage diameters.

    Abstract translation: 公开的是（1）具有接触管束（2），围绕通过该接触管的热交换介质循环回路与塞环线路通过一个反应器（3，4）在有夹套的孔的反应器的两端（5,6），用于传热介质的供给和排出 借助于一个或多个泵返回合适的话与所述热交换介质的转移或通过一个或多个外部热交换器中的热交换介质的一个子流，其特征在于，供给到下环形管线的热交换装置（4），并通过所述上部环线（3）（于）泵（一个或多个） 是，并用在反应器中心偏转板（7）交替和离开在反应器边缘，其中，所述下环形管线（4）由水平隔板（8）分成两个区域释放一个通道横截面，彼此（通过优选均匀分布的开口9 ）与可调节的通道横截面进行通信。

    5.
    发明专利
    未知

    公开(公告)号：BR0009000A

    公开(公告)日：2002-01-02

    申请号：BR0009000

    申请日：2000-03-15

    Applicant: BASF AG

    Inventor： OLBERT GERHARD ,  CORR FRANZ ,  REUTER PETER ,  WAMBACH LUDWIG ,  HAMMON ULRICH

    IPC: B01J8/06 ,  B01J19/00 ,  B01J19/24 ,  C07C45/35 ,  C07C45/38 ,  H01Q21/08 ,  B01J8/00

    Abstract: A multitube fixed bed reactor and the use of such a reactor for carrying out catalytic gas-phase reactions, in particular for carrying out exothermic and endothermic catalytic gas-phase reactions such as the preparation of phthalic anhydride (PA), acrylic acid, methacrylic acid (MAA), acrolein, maleic anhydride (MA), glyoxal, phosgene, hydrocyanic acid or vinyl formamide (VFA). In a relatively large multitube reactor in which a large amount of heat of reaction is generated owing to the numerous catalyst tubes ( 17 ) and has to be removed, it is proposed that the ratio of tube spacing t to external tube diameter d a be made dependent on the reactor diameter or on the external tube bundle diameter d RBa . At an external diameter of the catalyst tube bundle ( 18 ) of more than 4 meters, a ratio of tube spacing d to external tube diameter d a of at least 1.3 is preferred.

    Reactor with a bunch of heat-exchange tubes
    6.
    发明专利
    Reactor with a bunch of heat-exchange tubes 未知

    公开(公告)号：CZ2001524A3

    公开(公告)日：2001-07-11

    申请号：CZ2001524

    申请日：1999-08-06

    Applicant: BASF AG

    Inventor： CORR FRANZ ,  OLBERT GERHARD

    IPC: B01J8/06 ,  B01J19/00 ,  B01J19/24 ,  C07C45/27 ,  C07C47/127 ,  C07C51/16 ,  C07C51/25 ,  C07C51/255 ,  C07C57/04 ,  C07C57/05 ,  C07D401/06 ,  C07D401/12 ,  C07D401/14 ,  C07D405/14 ,  F28D7/16 ,  F28F9/02 ,  F28F9/22 ,  F28F27/02

    Abstract: The invention proposes a reactor (1) having a contact tube bundle (2) through whose space surrounding the contact tubes a heat-exchange medium circuit is passed, with ring lines (3, 4) at both ends of the reactor with jacket apertures (5, 6) for the supply and discharge of a heat-exchange medium by means of a pump via an external heat exchanger, where the heat-exchange medium is fed to the lower ring line (4) and is discharged to the heat exchanger via the upper ring line (3), and with baffle plates (7) which leave a passage cross section alternately in the reactor center and at the reactor edge. The upper (3) and lower (4) ring lines are each divided into an inner (11, 13) and an outer (12, 14) ring line by a cylindrical partition wall (8, 9), and the heat-exchange medium is fed to the outer lower ring line (14), via a region outside the reactor to the inner upper ring line (11), via the jacket apertures (5) of the latter to the region surrounding the contact tubes (2), via the jacket apertures (6) to the inner lower ring line (13) and subsequently via a region outside the reactor to the outer upper ring line (12).

    7.
    发明专利
    未知

    公开(公告)号：BR9912930A

    公开(公告)日：2001-05-08

    申请号：BR9912930

    申请日：1999-08-06

    Applicant: BASF AG

    Inventor： CORR FRANZ ,  OLBERT GERHARD

    IPC: B01J8/06 ,  B01J19/00 ,  B01J19/24 ,  C07C45/27 ,  C07C47/127 ,  C07C51/16 ,  C07C51/25 ,  C07C51/255 ,  C07C57/04 ,  C07C57/05 ,  C07D401/06 ,  C07D401/12 ,  C07D401/14 ,  C07D405/14 ,  F28D7/16 ,  F28F9/02 ,  F28F9/22 ,  F28F27/02

    Abstract: The invention proposes a reactor (1) having a contact tube bundle (2) through whose space surrounding the contact tubes a heat-exchange medium circuit is passed, with ring lines (3, 4) at both ends of the reactor with jacket apertures (5, 6) for the supply and discharge of a heat-exchange medium by means of a pump via an external heat exchanger, where the heat-exchange medium is fed to the lower ring line (4) and is discharged to the heat exchanger via the upper ring line (3), and with baffle plates (7) which leave a passage cross section alternately in the reactor center and at the reactor edge. The upper (3) and lower (4) ring lines are each divided into an inner (11, 13) and an outer (12, 14) ring line by a cylindrical partition wall (8, 9), and the heat-exchange medium is fed to the outer lower ring line (14), via a region outside the reactor to the inner upper ring line (11), via the jacket apertures (5) of the latter to the region surrounding the contact tubes (2), via the jacket apertures (6) to the inner lower ring line (13) and subsequently via a region outside the reactor to the outer upper ring line (12).

    Multi-tube fixed-bed reactor, especially for catalytic gas phase reactions
    8.
    发明专利
    Multi-tube fixed-bed reactor, especially for catalytic gas phase reactions 未知

    公开(公告)号：AU4538700A

    公开(公告)日：2000-10-04

    申请号：AU4538700

    申请日：2000-03-15

    Applicant: BASF AG

    Inventor： OLBERT GERHARD ,  CORR FRANZ ,  REUTER PETER ,  WAMBACH LUDWIG ,  HAMMON ULRICH

    IPC: B01J8/06 ,  B01J19/00 ,  B01J19/24 ,  C07C45/35 ,  C07C45/38 ,  H01Q21/08 ,  B01J8/00

    Abstract: A multitube fixed bed reactor and the use of such a reactor for carrying out catalytic gas-phase reactions, in particular for carrying out exothermic and endothermic catalytic gas-phase reactions such as the preparation of phthalic anhydride (PA), acrylic acid, methacrylic acid (MAA), acrolein, maleic anhydride (MA), glyoxal, phosgene, hydrocyanic acid or vinyl formamide (VFA). In a relatively large multitube reactor in which a large amount of heat of reaction is generated owing to the numerous catalyst tubes ( 17 ) and has to be removed, it is proposed that the ratio of tube spacing t to external tube diameter d a be made dependent on the reactor diameter or on the external tube bundle diameter d RBa . At an external diameter of the catalyst tube bundle ( 18 ) of more than 4 meters, a ratio of tube spacing d to external tube diameter d a of at least 1.3 is preferred.

    10.
    发明专利
    未知

    公开(公告)号：DE50104768D1

    公开(公告)日：2005-01-13

    申请号：DE50104768

    申请日：2001-05-03

    Applicant: BASF AG

    Inventor： OLBERT GERHARD ,  CORR FRANZ

    IPC: C07D307/60 ,  B01J19/00 ,  B01J19/24 ,  C07C45/35 ,  C07C47/127 ,  C07C47/22 ,  C07C51/215 ,  C07C51/25 ,  C07C51/265 ,  C07C57/04 ,  C07C57/05 ,  C07D307/89 ,  C07D401/06 ,  C07D401/12 ,  C07D401/14 ,  C07D405/14 ,  F28F27/02

    Abstract: In a reactor (1) which has a bundle of catalyst tubes (2) and in which a heat transfer medium is circulated through the space surrounding the catalyst tubes, with the ring lines (3, 4) at both ends of the reactor with openings (5, 6) through the wall for introduction or removal of a heat transfer medium by means of one or more pumps, where the heat transfer medium is introduced into the lower ring line (4) and is returned via the upper ring line (3) to the pump(s) and the heat transfer medium or a substream of the heat transfer medium may, if desired, be passed over one or more external heat exchangers, and with deflecting plates (7) which alternately leave free an open cross section in the middle of the reactor and at the edge of the reactor, the lower ring line (4) is divided by means of a horizontal dividing wall (8) into two regions between which material can pass via preferably uniformly distributed openings (9) having a regulatable open cross section.

Patent Agency Ranking