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    23.
    发明专利
    未知

    公开(公告)号：EE05624B1

    公开(公告)日：2013-02-15

    申请号：EEP200900071

    申请日：2008-01-23

    Applicant: OUTOTEC OYJ

    Inventor： BLIGH ROGER ,  HILTUNEN PEKKA ,  KLETT CORNELIS ,  MISSALLA MICHAEL ,  REEB BERND ,  SACHAROW LILLI ,  STROEDER MICHAEL ,  STURM PETER

    IPC: B01J8/00 ,  B01J8/18 ,  F23C10/32

    Abstract: The method involves drawing off of a solid flow by a down pipe (6), and fluidizing the solid flow on a base (8) of the down pipe by a supply of carrier gas. The solid flow is transported to a high level by an ascending pipe (9) branched off by the down pipe, and dimension of the solid flow extracted by the ascending pipe is varied by variable supply of the carrier gas. The level of the flow or solid stock in a solid container is used as a controlled variable, and a volume flow of the carrier gas is used as a correcting variable of a control loop. Independent claims are also included for the following: (1) a method for regulating a temperature and/or mixing ratio in a mixing vessel (2) a device for regulating a level and/or solid stock in a solid container.

    Method and apparatus for controlling a stream of solids
    24.
    发明专利
    Method and apparatus for controlling a stream of solids 未知

    公开(公告)号：AU2008221091B2

    公开(公告)日：2012-07-05

    申请号：AU2008221091

    申请日：2008-01-23

    Applicant: OUTOTEC OYJ

    Inventor： SACHAROW LILLI ,  MISSALLA MICHAEL ,  HILTUNEN PEKKA ,  STURM PETER ,  REEB BERND ,  BLIGH ROGER ,  KLETT CORNELIS ,  STROEDER MICHAEL

    IPC: B01J8/00 ,  F23C10/32

    Abstract: There are described a method and an apparatus for controlling the level and/or the inventory in a fluidized bed in a fluidized-bed tank, wherein a stream of solids is withdrawn from the fluidized-bed tank via a downer, the stream of solids is fluidized at the bottom of the downer by supplying a conveying gas flow and is conveyed to the top through a riser branching off from the downer. The size of the stream of solids conveyed through the riser is varied by the variable supply of the conveying gas, wherein the level of the solids or the solids inventory in the solids tank is used as a control variable and the volume flow rate of the conveying gas is used as an actuating variable of a control circuit.

    25.
    发明专利
    未知

    公开(公告)号：EE200900070A

    公开(公告)日：2009-12-15

    申请号：EEP200900070

    申请日：2008-01-23

    Applicant: OUTOTEC OYJ

    Inventor： BLIGH ROGER ,  HILTUNEN PEKKA ,  KLETT CORNELIS ,  MISSALLA MICHAEL ,  REEB BERND ,  SACHAROW LILLI ,  STROEDER MICHAEL ,  STURM PETER

    IPC: B01J8/00 ,  F23C10/10

    Abstract: The method for the distribution of a solid flow (m 0) drawn-off from a cyclone or a fluidized bed container (1), comprises conducting the solid flow (m 0) over a first down pipe (7) and then fluidizing at the bottom of the down pipe by supplying a carrier gas, conveying a part of the solid flow (m 1) towards the top by the carrier gas over a first riser (9) branching off from the first down pipe, leading away the remaining part of the solid flow (m 0) over a second down pipe (13) adjacent itself to the first down pipe and then fluidizing at the bottom of the second down pipe. The method for the distribution of a solid flow (m 0) drawn-off from a cyclone or a fluidized bed container (1), comprises conducting the solid flow (m 0) over a first down pipe (7) and then fluidizing at the bottom of the down pipe by supplying a carrier gas, conveying a part of the solid flow (m 1) towards the top by the carrier gas over a first riser (9) branching off from the first down pipe, leading away the remaining part of the solid flow (m 0) over a second down pipe (13) adjacent itself to the first down pipe and then fluidizing at the bottom of the second down pipe by supplying the carrier gas, and conveying a part of the solid flow (m 2) towards the top by the carrier gas over a second riser (15) branching off from the second down pipe. The supply of the carrier gas is varied at the bottom of the first and/or the second down pipe. The pressure difference over the fluidized bed container is used as controlled variable for the supply of the carrier gas to the first or the second down pipe. The supply of the carrier gas is constantly held at the bottom of the first down pipe. The pressure difference between the bottom and the head of the first and/or the second down pipe is smaller than the pressure loss corresponding to the fluidized down pipe. The pressure at the bottom of each down pipe is larger than the pressure at the head of this down pipe. The conveying air is brought beneath the first and/or the second riser in each case over a downwardly arranged nozzle. The carrier gas is admitted with low volume flow for the interruption of the solid flow in a riser, so that the minimum fluidization speed is not exceeded in the riser. An independent claim is included for a device for the distribution of a solid flow drawn-off from a cyclone or a fluidized bed container.

    26.
    发明专利
    未知

    公开(公告)号：DE102008013505A1

    公开(公告)日：2009-09-24

    申请号：DE102008013505

    申请日：2008-03-10

    Applicant: OUTOTEC OYJ

    Inventor： ORTH ANDREAS ,  STROEDER MICHAEL ,  NEPPER JEAN-PAUL

    IPC: F27D17/00

    Abstract: A process for the production and/or treatment of at least one metal in a reactor includes discharging a waste gas stream via a waste gas conduit and after-treating the waste gas stream by supplying a cooling gas and/or a cooling gas mixture. The after-treating includes injecting the cooling gas and/or cooling gas mixture into the waste gas conduit on a side of the waste gas conduit facing the reactor, at a high velocity and substantially tangentially with respect to a main flow direction of the waste gas. A volume of the cooling gas and/or the cooling gas mixture injected into the waste gas conduit is adjusted so as to reduce a mixing temperature below a melting temperature of the molten particles and/or a condensation temperature of the vaporous constituents of the waste gas stream.

    Distribution of solid flow drawn-off from cyclone/fluidized bed container, by conducting solid flow over first down pipe and then fluidizing at bottom of down pipe by supplying carrier gas, and conveying a part of solid flow towards the top
    27.
    发明专利
    Distribution of solid flow drawn-off from cyclone/fluidized bed container, by conducting solid flow over first down pipe and then fluidizing at bottom of down pipe by supplying carrier gas, and conveying a part of solid flow towards the top 未知

    公开(公告)号：DE102007009759A1

    公开(公告)日：2008-08-28

    申请号：DE102007009759

    申请日：2007-02-27

    Applicant: OUTOTEC OYJ

    Inventor： BLIGH ROGER ,  HILTUNEN PEKKA ,  KLETT CORNELIS ,  MISSALLA MICHAEL ,  REEB BERND ,  SACHAROW LILLI ,  STROEDER MICHAEL ,  STURM PETER

    IPC: B01J8/18 ,  B01J8/24 ,  C01F7/44

    Abstract: The method for the distribution of a solid flow (m 0) drawn-off from a cyclone or a fluidized bed container (1), comprises conducting the solid flow (m 0) over a first down pipe (7) and then fluidizing at the bottom of the down pipe by supplying a carrier gas, conveying a part of the solid flow (m 1) towards the top by the carrier gas over a first riser (9) branching off from the first down pipe, leading away the remaining part of the solid flow (m 0) over a second down pipe (13) adjacent itself to the first down pipe and then fluidizing at the bottom of the second down pipe. The method for the distribution of a solid flow (m 0) drawn-off from a cyclone or a fluidized bed container (1), comprises conducting the solid flow (m 0) over a first down pipe (7) and then fluidizing at the bottom of the down pipe by supplying a carrier gas, conveying a part of the solid flow (m 1) towards the top by the carrier gas over a first riser (9) branching off from the first down pipe, leading away the remaining part of the solid flow (m 0) over a second down pipe (13) adjacent itself to the first down pipe and then fluidizing at the bottom of the second down pipe by supplying the carrier gas, and conveying a part of the solid flow (m 2) towards the top by the carrier gas over a second riser (15) branching off from the second down pipe. The supply of the carrier gas is varied at the bottom of the first and/or the second down pipe. The pressure difference over the fluidized bed container is used as controlled variable for the supply of the carrier gas to the first or the second down pipe. The supply of the carrier gas is constantly held at the bottom of the first down pipe. The pressure difference between the bottom and the head of the first and/or the second down pipe is smaller than the pressure loss corresponding to the fluidized down pipe. The pressure at the bottom of each down pipe is larger than the pressure at the head of this down pipe. The conveying air is brought beneath the first and/or the second riser in each case over a downwardly arranged nozzle. The carrier gas is admitted with low volume flow for the interruption of the solid flow in a riser, so that the minimum fluidization speed is not exceeded in the riser. An independent claim is included for a device for the distribution of a solid flow drawn-off from a cyclone or a fluidized bed container.

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