REAKTOR ZUR DURCHFÜHRUNG EINER DREIPHASENREAKTION EINER FLÜSSIGEN UND EINER GASFÖRMIGEN PHASE AN EINEM KATALYSATORFESTBETT
    1.
    发明公开
    REAKTOR ZUR DURCHFÜHRUNG EINER DREIPHASENREAKTION EINER FLÜSSIGEN UND EINER GASFÖRMIGEN PHASE AN EINEM KATALYSATORFESTBETT 有权
    反应器对性能的三相反应液体和气相在催化剂固定床

    公开(公告)号:EP2170494A1

    公开(公告)日:2010-04-07

    申请号:EP08774160.9

    申请日:2008-06-20

    Applicant: BASF SE

    Abstract: The invention relates to a reactor (R) for performing a three-phase reaction of a fluid phase (1) and a gaseous phase (2) on a packed bed catalyst (F), the packed bed catalyst (F) being disposed horizontally in the reactor (R) and the fluid phase (1) and the gaseous phase (2) being fed through the reactor (R) from the bottom to the top, using a mixing and distributing device (MV) across the packed bed catalyst (F), characterized in that the mixing and distributing device (MV) comprises a trough distributor (TV) for the fluid phase (1) having trough-shaped channels (K) and drain tubes (A) in the trough-shaped channels (K) for the fluid phase (1), and a distributor floor (B) disposed below and at a distance from the trough distributor (TV) in which vertical spouts (T) are disposed, having one or more openings (P1) for the inlet of the gaseous phase (2) and one or more openings (P2) disposed below the openings (P1) for the inlet of the gaseous phase, for the inlet of the fluid phase (1) into the spouts (T), and the number and size of the openings (P2) for the inlet of the fluid phase (1) being designed such that the fluid level on the distribution floor (B) is adjusted to be below the openings (P1) for the inlet of the gaseous phase (2) and above the openings (P2) for the inlet of the fluid phase (1) for a prescribed inlet flow of fluid.

    REAKTOR ZUR DURCHFÜHRUNG EINER DREIPHASENREAKTION EINER FLÜSSIGEN UND EINER GASFÖRMIGEN PHASE AN EINEM KATALYSATORFESTBETT
    3.
    发明授权
    REAKTOR ZUR DURCHFÜHRUNG EINER DREIPHASENREAKTION EINER FLÜSSIGEN UND EINER GASFÖRMIGEN PHASE AN EINEM KATALYSATORFESTBETT 有权
    反应器对性能的三相反应液体和气相在催化剂固定床

    公开(公告)号:EP2170494B1

    公开(公告)日:2011-08-17

    申请号:EP08774160.9

    申请日:2008-06-20

    Applicant: BASF SE

    Abstract: The invention relates to a reactor (R) for performing a three-phase reaction of a fluid phase (1) and a gaseous phase (2) on a packed bed catalyst (F), the packed bed catalyst (F) being disposed horizontally in the reactor (R) and the fluid phase (1) and the gaseous phase (2) being fed through the reactor (R) from the bottom to the top, using a mixing and distributing device (MV) across the packed bed catalyst (F), characterized in that the mixing and distributing device (MV) comprises a trough distributor (TV) for the fluid phase (1) having trough-shaped channels (K) and drain tubes (A) in the trough-shaped channels (K) for the fluid phase (1), and a distributor floor (B) disposed below and at a distance from the trough distributor (TV) in which vertical spouts (T) are disposed, having one or more openings (P1) for the inlet of the gaseous phase (2) and one or more openings (P2) disposed below the openings (P1) for the inlet of the gaseous phase, for the inlet of the fluid phase (1) into the spouts (T), and the number and size of the openings (P2) for the inlet of the fluid phase (1) being designed such that the fluid level on the distribution floor (B) is adjusted to be below the openings (P1) for the inlet of the gaseous phase (2) and above the openings (P2) for the inlet of the fluid phase (1) for a prescribed inlet flow of fluid.

    KOLONNE MIT QUERSTROMBÖDEN UND FLÜSSIGKEITSVERTEILER
    4.
    发明公开
    KOLONNE MIT QUERSTROMBÖDEN UND FLÜSSIGKEITSVERTEILER 审中-公开
    KOLONNE MITQUERSTROMBÖDENUNDFLÜSSIGKEITSVERTEILER

    公开(公告)号:EP2144680A1

    公开(公告)日:2010-01-20

    申请号:EP08749645.1

    申请日:2008-04-22

    Applicant: BASF SE

    CPC classification number: B01D3/166 B01D3/008

    Abstract: The invention relates to a column for treating substance mixtures by intense contact with a liquid and gaseous phase, wherein on the inside the column has one or more cross-flow bottoms on which heat transfer elements (7) are disposed, through which a heat transfer medium flows, and wherein above one or more of said cross-flow bottoms fluid distributors (4, 5) are disposed, which have outflow openings (6) through which the fluid is evenly distributed via the heat transfer elements (7) beneath the fluid distributors (4, 5), and wherein the fluid distributors (4, 5) are disposed above the heat transfer elements (7) in the column such that they are located in the vicinity of the inflow line or outflow line of the heat transfer medium into the heat transfer elements (7).

    Abstract translation: 本发明涉及一种用于通过与液相和气相强烈接触来处理物质混合物的塔,其中在塔的内部具有一个或多个横流底部,在该底部上设置传热元件(7),通过该塔 介质流,并且其中设置有一个或多个所述横流底部流体分配器(4,5),其具有流出开口(6),流体通过所述流出开口(6)经由所述流体下方的传热元件(7)均匀分布 分配器(4,5),并且其中所述流体分配器(4,5)设置在所述塔中的传热元件(7)的上方,使得它们位于所述传热介质的流入管线或流出管线附近 进入传热元件(7)。

    BODEN FÜR EINE STOFFAUSTAUSCHKOLONNE
    7.
    发明公开
    BODEN FÜR EINE STOFFAUSTAUSCHKOLONNE 有权
    地面传质塔

    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

    Applicant: BASF SE

    Abstract: 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.

    VORRICHTUNG UND VERFAHREN ZUR GEWINNUNG HOCHREINER PRODUKTE AUS EINEM KOLONNENABZUG
    8.
    发明公开
    VORRICHTUNG UND VERFAHREN ZUR GEWINNUNG HOCHREINER PRODUKTE AUS EINEM KOLONNENABZUG 有权
    装置和方法获得高PURE产品从塔提取

    公开(公告)号:EP2214797A1

    公开(公告)日:2010-08-11

    申请号:EP08874459.4

    申请日:2008-11-19

    Applicant: BASF SE

    CPC classification number: B01D3/008 B01D3/14

    Abstract: The present invention relates to a fluid collector for use in a packing column, comprising at least one element for collecting (5) the fluid (element A) (5, 6) flowing out of the packing bed and at least one draw from the column (10), wherein all elements (5, 6) are at a distance from (7) the column wall (3) and optionally a separating wall, or at least one capture device is mounted above or in the fluid collector (5), so that fluid flowing downward on the wall in the collection direction is collected and passes by the elements A (5, 6). The invention further relates to a packing column for separating substance mixtures, comprising at least one fluid collector and draw according to the invention. The invention further relates to a method for separating one or more components from a substance mixture in at least one packing column according to the invention. The method is used particularly in order to obtain a highly pure product from a side draw or sump draw by means of the fluid collector according to the invention.

    VERFAHREN ZUR HERSTELLUNG VON SPEZIFIKATIONSGERECHTEM PHTHALSÄUREANHYDRID
    9.
    发明授权
    VERFAHREN ZUR HERSTELLUNG VON SPEZIFIKATIONSGERECHTEM PHTHALSÄUREANHYDRID 有权
    用于生产规范苯酐

    公开(公告)号:EP1838405B1

    公开(公告)日:2008-08-06

    申请号:EP05821914.8

    申请日:2005-12-31

    Applicant: BASF SE

    CPC classification number: C07C51/573 B01D3/14 C07D307/89 C07C63/16

    Abstract: The invention relates to a method for producing phthalic anhydride that conforms to specifications in a purification of crude phthalic anhydride by distillation at a reduced pressure. According to said method, the crude phthalic anhydride is supplied to the distillation column above a lateral outlet, the low-boilers are drawn off at the head of the column or in the vicinity of the head of the column and the phthalic anhydride that conforms to specifications is removed from the lateral outlet. The method uses a distillation column with a number of theoretical separation stages situated above the supply of the crude phthalic anhydride to the distillation column that lies between 10 and 20 and the column operates with a reflux ratio of between 0.1 and 0.5.

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