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    • 42. 发明专利
    • Preparing catalyst molded body, useful e.g. in ammoxidation of propene to acrylonitrile, comprises mixing starting mass having fine particles of bismuth mixed oxide with another starting mass, and forming geometrical molded bodies
    • DE102008042060A1
    • 2009-06-18
    • DE102008042060
    • 2008-09-12
    • BASF SE
    • RAICHLE ANDREASCREMER ULRICHHORSTMANN CATHARINAROSOWSKI FRANKMUELLER-ENGEL KLAUS JOACHIM
    • B01J23/31B01J35/02
    • Preparing geometrical catalyst molded body (I) containing bismuth-molybdenum-iron oxide (II), comprises preparing fine particles of bismuth mixed oxide (III), as starting mass (A1); producing an aqueous mixture under the use of source of the molybdenum-iron oxide element (IV); passing the sources to a dissipation degree Q; producing a starting mass (A2) by drying and adjusting the dissipation degree of the mixture; mixing the starting masses (A1) and (A2) to obtain a starting mass (A3); forming geometrical molded bodies from the starting mass (A3); and thermally treating the molded bodies. Preparation of geometrical catalyst molded body (I) containing bismuth-molybdenum-iron oxide of formula (((Bi 1Z 1> bO x) aZ 0> cMo 12Fe dZ 2> eZ 3> fZ 4> gZ 5> hZ 6> iO y) 1) (II) as active mass, comprises preparing fine particles of bismuth mixed oxide of formula (Bi 1Z 1> bO x) (III) with an average particle diameter (d 50), as starting mass (A1), under the condition that the particle diameter (d 50) of A1 is 1-100 mu m; producing an aqueous mixture under the use of source of the elements different by oxygen of a part T, which is molybdenum-iron oxide of formula ([Z 0> cMo 12Fe dZ 2> eZ 3> fZ 4> gZ 5> hZ 6> iO y] 1) (IV); passing the sources used in the production of the aqueous mixture to a dissipation degree Q, which has a particle diameter (d 90) of = 5 mu m, where the aqueous mixture contains the elements of Z 0>, molybdenum, iron, Z 2>, Z 3>, Z 4>, Z 5>and Z 6>in stoichiometry of formula (Z 0> cMo 12Fe dZ 2> eZ 3> fZ 4> gZ 5> hZ 6> i) (V); producing a starting mass (A2) with a particle diameter (d 90) of 10-400 mu m, by drying and adjusting the dissipation degree of the aqueous mixture; mixing the starting mass (A1) and starting mass (A2), or starting mass (A1), starting mass (A2) and fine particles of molding auxiliary agent to obtain a starting mass (A3) with stoichiometric bismuth-molybdenum-iron multielement oxide of formula ((Bi 1Z 1> b) aZ 0> cMo 12Fe dZ 2> eZ 3> fZ 4> gZ 5> hZ 6> i) (VI); forming geometrical molded bodies from the fine particles of the starting mass (A3); and thermally treating the molded bodies at high temperature, where (I) has a stoichiometric coefficient, which is greater than 0 and >= 0.8. Z 0>Y or lanthanides excluding La and Ce; Z 1>W or Mo; Z 2>Ni or Co; Z 3>an alkali metal, alkaline earth metal or Tl; Z 4>Ln, Ce, Zn, P, As, B, Sb, Sn, V, Cr or Bi; Z 5>Si, Al, Ti, W or Zr; Z 6>Cu, Ag or Au; a : 0.05-6; b : 0.1-10; c : >= 0.001; d : 0.01-5; e : 1-10; f : 0.01-2; g : 0-5; h : 0-50; i : 0-1; and x, y : numbers, which are determined by the valency and frequency of the elements different from oxygen in (I). An independent claim is included for the geometrical catalyst molded body obtained by the above process.
    • 43. 发明专利
    • Producing a ring like oxidic mold, useful e.g. in partial gas phase oxidation of e.g. an organic compound, comprising mechanical packing of a powdery material which is brought into the fill space of a die made of a metal compound
    • DE102008040093A1
    • 2008-12-18
    • DE102008040093
    • 2008-07-02
    • BASF SE
    • EGER KNUTFAUST JENS UWEBORCHERT HOLGERSTREIBERT RALFMUELLER-ENGEL KLAUS JOACHIMRAICHLE ANDREAS
    • B22F3/12B30B11/02
    • Producing a ring like oxidic mold, comprising mechanical packing of a powdery material which is brought into the fill space of a die made out of components that contain at least one metal compound, which is convertible into a metal oxide through a thermal treatment at >= 100[deg] C or at least comprises one metal oxide, or at least one metal oxide and at least one such metal compound. Producing a ring like oxidic mold, comprising mechanical packing of a powdery material which is brought into the fill space of a die made out of components that contain at least one metal compound, which is convertible into a metal oxide through a thermal treatment at >= 100[deg] C or at least comprises one metal oxide, or at least one metal oxide and at least one such metal compound, to form a ring like precursor mold, in which the fill space is present in a die bore which passes through the die material with a vertical axis of drill B from top to bottom and through the inner wall of the die bore, the upper front surface of lower stamp which has been introduced from below movable up and down along the axis of drill B in the die bore, on which the powdery material which has been introduced into the fill space lies, the length of the axis of drill B in an axial initial distance A above the upper front surfaces of the lower stamp present lower front surfaces movable up and down along the axis of drill B introduced upper stamp, whose lower front surfaces moves in the powdery material introduced in the fill space, and the coat surface is limited by a guided tool sprig MF which is guided from the geometrical middle of the upper front surface of the lower stamp outwardly along the axis of drill which reaches up to the geometrical middle of the lower front surface of the upper stamp, so that the axial initial distance A of both the front surfaces is limited for the packing along the axis of drill B to a pre-determined axial end distance E that one can sink the lower stamp and such that the position of the lower stamp is retained or the lower stamp additionally lifts, where: the geometric form of the coat surface of the lower stamp whose coat surface corresponds to a circular cylinder I; the geometric form of the coat surface of the upper stamp corresponds to a circular cylinder II; in the geometrical middle of the upper front surface of the lower stamp a tool die MB-U has been designed which passes through from top towards the bottom through the lower stamp; in the initial distance A both the front surfaces of the tool sprig MF protrudes from top to bottom through the die bore MB-U until it reaches the geometrical middle of the lower front surfaces of the lower stamp; the tool sprig MF from bottom to top has the geometric form of a circular cylinder Z with a circular cylindrical coat surface MZ; the length of the contours of the circular cylinder Z is smaller that the length of the contours of the circular cylinder I as also smaller than the contours of the circular cylinder II; the position of the tool sprig MF and the position of the dies including that of the die bore on the length of the axis of drill B are fixed relative to each other during the process; in the geometric middle of the lower front surfaces of the lower stamp a tool bore MB-O is designed which goes into the upper stamp and which is connected to at least one outlet of the upper stamp, which can accept the tool sprig MF during a shortening of the initial distance A on the end distance E in a necessary circumference and which can protrude into the tool sprig in at an initial distance A; the symmetry axes of the die bore, of the circular cylinder I, the circular cylinder II, the tool bore MB, the tool sprig MF and the tool bore MB-U lie on a line which runs vertically through the die bore; the die bore has a longitudinal section along its axis of drill, on which length I the geometric form of the inner wall of the die bore whose coat surface correspond to that of a circular cylinder KZ and on whose upper end there is a die bore connected on a longitudinal section II which is directed towards the top, which has the length II; the upper stamp is taken off from the designed ring like precursor molds and the ring like precursor molds are removed from the die bore by lifting the lower stamp after the end of the packing; and also a subsequent procedure of thermal treatment of the ring like precursor molds at >= 100[deg] C during which at least a partial quantity of its components disintegrates during the building of a gaseous compound and/or chemically transformed and the ring like oxidic mold builds itself, where the geometric form of the inner wall of the die bore on the length II of the longitudinal section II from bottom to top whose coat surfaces corresponds to the frustum which extends from bottom to top, whose cross section surface on its lower end of the cross sectional surface of the circular cylinder KZ corresponds to its upper end, provided that by achieving the end distance E the lower front surface of the lower stamp is not present in the longitudinal section II and the upper front surface of the upper stamp is not present in the longitudinal section I, so that the ring like precursor molds which have been built between both the front surfaces by the mechanical packing of the powdery material is partially present in the longitudinal section II while reaching the end distance E. Independent claims are included for: (1) the ring like oxidic mold obtained by the above process; and (2) a tube bundle reactor whose reactor tube contains the ring like oxidic mold.
    • 46. 发明专利
    • Procedure for continuous separation of target product in the form of fine particle of crystallisate, comprises indirectly operating a heat exchanger having primary and secondary areas, which are spatially separated with one another
    • DE102007043759A1
    • 2008-09-11
    • DE102007043759
    • 2007-09-13
    • BASF SE
    • HEILEK JOERGHAMMON ULRICHMUELLER-ENGEL KLAUS JOACHIMSCHLIEPHAKE VOLKERBAUMANN DIETER
    • B01D9/02C07C57/07
    • The procedure for continuous separation of target product (X) in the form of fine particle of crystallisate from a liquid phase (P) existing from the target product (X) and/or by the target product of different constituents, comprises indirectly operating a heat exchanger having primary and secondary areas, which are spatially separated with one another through a material divider that serves as an area for transmitting heat from the secondary area to the primary area by passing a stream at the liquid phase (P) in the secondary area of the heat exchanger. The procedure for continuous separation of target product (X) in the form of fine particle of crystallisate from a liquid phase (P) existing from the target product (X) and/or by the target product of different constituents, comprises indirectly operating a heat exchanger having primary and secondary areas, which are spatially separated with one another through a material divider that serves as an area for transmitting heat from the secondary area to the primary area by passing a stream at the liquid phase (P) in the secondary area of the heat exchanger during the primary area flows throughable simultaneously to a liquid cooling medium so that it forms fine particles of crystallisate of the target product in the secondary area under disposition of a liquid residual phase from the liquid phase (P). The total mole fraction of the liquid phase has the value of M b, p ges at the constituent (B i). The liquid residual phase (R) contains ingredients with a total mole fraction of M b, r (ges) greater than M b, p (ges) in comparison with the liquid phase (P). The content of residual phase in the target product is 70 wt.%. The cooling medium is suspended by fine particles of crystallisate of the target product in the liquid residual phase under receiving a suspension (S) having a crystallization grade (Y). The secondary area of the heat exchanger continuously takes the suspension with the temperature T s (aus). The suspension of fine particle crystallisate from the extracted suspension in load of discharge device is introduced with temperature (TS) to a mixing buffer container by a pump and the liquid phase is separated from the suspension contained in the discharge device. The temperature of the suspension in the buffer container is elevated from the way of secondary area in the buffer container and/or pipelines of the buffer container by external energy source at a value of T(pu) above of T s(aus) and/or the total mole fraction of the ingredients is increased in the liquid residual phase of the suspension in the buffer container through external additive in the ingredients at a value of M b, p u (ges) above of M b, r (ges). The T(pu)-T s(aus) is greater than or equal to 0.1 K. The increasing of M b, r ges at M b, r (ges) is greater than or equal to 0.1%. The content of the liquid residual phase at the target product is greater than or equal 90 wt.%. The crystallization grade (Y) is 0.20-0.40.
    • 50. 发明专利
    • BRPI0716552A2
    • 2013-09-24
    • BRPI0716552
    • 2007-09-17
    • BASF SE
    • BLECHSCHMITT MICHAELHAMMON ULRICHMARTIN FRIEDRICH-GEORGMUELLER-ENGEL KLAUS JOACHIMZEHNER PETER
    • B01F33/40B01J19/24B01J19/26F04F5/10
    • Mixing a liquid or suspension beneath a gas space in a closed container comprises supplying a stream of the liquid or suspension as a drive jet for a submerged ejector which aspirates gas from the gas space and discharges the gas together with the drive jet into the liquid or suspension in the container. Independent claims are also included for: (1) container comprising a liquid or suspension beneath a gas space and an ejector with a drive nozzle and a suction chamber in communication with the gas space; (2) container comprising a liquid or suspension beneath a gas space and an ejector jet nozzle having a drive nozzle surrounded by a suction chamber discharging into a mixing nozzle and an impulse exchange chamber into which the outlet of the mixing nozzle is directed, and a connection between the suction chamber and the gas space; (3) ejector jet nozzle having a drive nozzle surrounded by a suction chamber discharging into a mixing nozzle and an impulse exchange chamber into which the outlet of the mixing nozzle is directed, where the transition between the mixing nozzle and the impulse exchange chamber is provided with a jacket fitted with a dip pipe or a connector for a dip pipe; (4) mixing a liquid or suspension beneath a gas space in a closed container by supplying a stream of another liquid or suspension as a drive jet for a submerged ejector which aspirates gas from the gas space and discharges the gas together with the drive jet into the liquid or suspension in the container.