1.
    发明专利
    未知

    公开(公告)号:DE602004026866D1

    公开(公告)日:2010-06-10

    申请号:DE602004026866

    申请日:2004-05-17

    Abstract: The invention relates to a process for preparing caprolactam by admixture of cyclohexanone oxime to a reaction mixture comprising caprolactam and sulfuric acid using a mixing device, said mixing device comprising (i) a tube through which the reaction mixture can flow, and (ii) channels disposed around the tube, said channels opening into the tube, said process comprising: passing the reaction mixture through the tube, and feeding the cyclohexanone oxime into the reaction mixture through one or more of said channels, wherein Re>5000, Re being the Reynolds number as defined by rho.V.D/eta, wherein rho=density (in kg/m 3 ) of the reaction mixture that is fed to the tube V=velocity of the reaction mixture, V being defined as W/A, wherein W is the flow rate (in m 3 /s) of the reaction mixture that is fed into the tube and A is the cross section area of the tube (in m 2 ) at the level where said channels open into the tube D=diameter of the tube at the level where said channels open into the tube (in m) eta=viscosity of the reaction mixture that is fed into the tube (in Pa.s).

    3.
    发明专利
    未知

    公开(公告)号:DE602004026730D1

    公开(公告)日:2010-06-02

    申请号:DE602004026730

    申请日:2004-07-16

    Abstract: The invention relates to a process for purifying caprolactam, said process comprising (a) subjecting the caprolactam to a hydrogenation by treating the caprolactam with hydrogen in the presence of a heterogeneous nickel containing hydrogenation catalyst, (b) distilling at least a portion of the hydrogenated caprolactam in a distillation column containing nickel in an amount sufficiently low such that DeltaPAN Ni Ni =DeltaPAN-DeltaPAN Ni=0 , DeltaPAN=increase of the PAN number of caprolactam during distilling, DeltaPAN Ni=0 increase of the PAN number of caprolactam during distilling under the same conditions in a distillation column free of nickel. Nickel is removed from the caprolactam solution prior to the distillation step.

    5.
    发明专利
    未知

    公开(公告)号:DE602004009173T2

    公开(公告)日:2008-06-26

    申请号:DE602004009173

    申请日:2004-05-17

    Abstract: The invention relates to a process for preparing caprolactam by admixture of cyclohexanone oxime to a reaction mixture comprising caprolactam and sulfuric acid using a mixing device, said mixing device comprising (i) a tube through which the reaction mixture can flow, and (ii) channels disposed around the tube, said channels opening into the tube, said process comprising: passing the reaction mixture through the tube, and feeding the cyclohexanone oxime into the reaction mixture through one or more of said channels, wherein Re>5000, Re being the Reynolds number as defined by rho.V.D/eta, wherein rho=density (in kg/m 3 ) of the reaction mixture that is fed to the tube V=velocity of the reaction mixture, V being defined as W/A, wherein W is the flow rate (in m 3 /s) of the reaction mixture that is fed into the tube and A is the cross section area of the tube (in m 2 ) at the level where said channels open into the tube D=diameter of the tube at the level where said channels open into the tube (in m) eta=viscosity of the reaction mixture that is fed into the tube (in Pa.s).

    6.
    发明专利
    未知

    公开(公告)号:DE602004009173D1

    公开(公告)日:2007-11-08

    申请号:DE602004009173

    申请日:2004-05-17

    Abstract: The invention relates to a process for preparing caprolactam by admixture of cyclohexanone oxime to a reaction mixture comprising caprolactam and sulfuric acid using a mixing device, said mixing device comprising (i) a tube through which the reaction mixture can flow, and (ii) channels disposed around the tube, said channels opening into the tube, said process comprising: passing the reaction mixture through the tube, and feeding the cyclohexanone oxime into the reaction mixture through one or more of said channels, wherein Re>5000, Re being the Reynolds number as defined by rho.V.D/eta, wherein rho=density (in kg/m 3 ) of the reaction mixture that is fed to the tube V=velocity of the reaction mixture, V being defined as W/A, wherein W is the flow rate (in m 3 /s) of the reaction mixture that is fed into the tube and A is the cross section area of the tube (in m 2 ) at the level where said channels open into the tube D=diameter of the tube at the level where said channels open into the tube (in m) eta=viscosity of the reaction mixture that is fed into the tube (in Pa.s).

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