公开(公告)号：NO20053270L

公开(公告)日：2005-08-15

申请号：NO20053270

申请日：2005-07-04

Applicant: OUTOKUMPU OY

Inventor： STRODER MICHAEL ,  SELT WOLFGANG ,  KAPPES TORSTEN

IPC: B01J8/00 ,  B01J8/18 ,  B01J8/24

Abstract: The invention relates to a method of controlling the process conditions, in particular the temperature, in a reactor ( 1 ) of a plant into which, in particular, granular material is introduced and transported through a conveying line ( 14 ) to the reactor ( 1 ). In order to keep the process conditions in the reactor as constant as possible, the material quantity transported in the conveying line ( 14 ) is determined and is used as control variable and/or disturbance variable for controlling the process conditions, in particular the temperature. A plant for carrying out this method is also described.

公开(公告)号：NO20053293D0

公开(公告)日：2005-07-05

申请号：NO20053293

申请日：2005-07-05

Applicant: OUTOKUMPU OY

Inventor： STRODER MICHAEL ,  STOCKHAUSEN WERNER ,  NUBER DIRK

IPC: B01J8/00 ,  B01J8/18 ,  C04B11/028 ,  F27B15/02 ,  F27B15/10 ,  F27B15/16 ,  B01J

Abstract: The present invention relates to a method for the heat treatment of fine-grained solids, in particular gypsum, in which the solids are heated to a temperature of 50 to 1000° C. in a fluidized bed reactor (1), and to a corresponding plant. To improve the energy utilization, it is proposed to introduce a first gas or gas mixture from below through a preferably central gas supply tube (3) into a mixing chamber (21) of the reactor (1), the gas supply tube (3) being at least partly surrounded by a stationary annular fluidized bed (2) which is fluidized by supplying fluidizing gas, and to adjust the gas velocities of the first gas or gas mixture as well as of the fluidizing gas for the annular fluidized bed (2) such that the particle Froude numbers in the gas supply tube (3) are between 1 and 100, in the annular fluidized bed (2) between 0.02 and 2 and in the mixing chamber (21) between 0.3 and 30.

公开(公告)号：NO20053290D0

公开(公告)日：2005-07-05

申请号：NO20053290

申请日：2005-07-05

Applicant: OUTOKUMPU OY

Inventor： ANASTASIJEVIC NIKOLA ,  STRODER MICHAEL ,  GERDES THORSTEN ,  WILLERT-PORADA MONICA

IPC: B01J8/38 ,  B01J19/12 ,  C04B2/10 ,  H05B6/78 ,  H05B6/80 ,  B01J

Abstract: This invention relates to a method for the thermal treatment of granular solids in a reactor ( 1 ) with swirl chamber ( 4 ), which in particular constitutes an flash reactor or suspension reactor, wherein the microwave radiation from a microwave source ( 2 ) is fed into the reactor ( 1 ) through a wave guide, and to a corresponding plant. To avoid deposits in the wave guide, the same constitutes a gas supply tube ( 3 ), a gas stream being additionally fed through the gas supply tube ( 3 ) into the swirl chamber ( 4 ).

公开(公告)号：NO20053269D0

公开(公告)日：2005-07-04

申请号：NO20053269

申请日：2005-07-04

Applicant: OUTOKUMPU OY

Inventor： HIRSCH MARTIN ,  STRODER MICHAEL ,  STOCKHAUSEN WERNER

IPC: B01J8/00 ,  B01J8/18 ,  B01J8/24 ,  B01J8/38 ,  C01B13/32 ,  C01F7/44 ,  F23C10/12 ,  F23C10/14 ,  C01F

Abstract: A plant for producing metal oxide from metal compounds includes a fluidized-bed reactor in which the metal compounds are heated by a combustion of a fuel to produce metal oxide. The fluidized-bed-reactor reactor includes at least one gas supply tube at least partly surrounded by an annular chamber in which a stationary annular fluidized bed is disposed, and a mixing chamber disposed above an orifice region of the gas supply tube. A gas flowing through the gas supply tube entrains solids from the stationary annular fluidized bed when passing through the orifice region.

公开(公告)号：PE20040454A1

公开(公告)日：2004-09-10

申请号：PE2003001277

申请日：2003-12-12

Applicant: OUTOKUMPU OY

Inventor： STRODER MICHAEL ,  ANASTASIJEVIC NIKOLA ,  GERDES THORSTEN ,  WILLERT-PORADA MONIKA

IPC: B01J8/24 ,  B01J8/36 ,  B01J8/38 ,  B01J8/42 ,  C22B1/10 ,  C22B5/14 ,  C22B11/02 ,  F26B3/08 ,  F26B3/084 ,  F26B3/34 ,  H05B6/78 ,  H05B6/80

Abstract: TAL QUE DICHO LECHO FLUIDIZADO SE ENCUENTRA EN UN REACTOR DE CAPA DE FLUIDIZACION EN EL CUAL RADIACIONES DE MICROONDAS SON ALIMENTADAS AL REACTOR DE CAPA DE FLUIDIZACION A TRAVES DE UNA GUIA DE ONDAS TUBULAR MAS EL APARATO CORRESPONDIENTE, CARACTERIZADO PORQUE EL ANGULO DE IRRADIACION DE LAS MICROONDAS CON RESPECTO AL EJE PRINCIPAL DEL REACTOR ES DE 10° A 50° PREFERENTEMENTE 10° A 20°; ESTO PARA MEJORAR LA EFICIENCIA DE LA IRRADIACION DE MICROONDAS.

公开(公告)号：BG107883A

公开(公告)日：2004-07-30

申请号：BG10788303

申请日：2003-06-05

Applicant: OUTOKUMPU OY

Inventor： STRODER MICHAEL ,  ZINGREBE HORST ,  VOLLMER HUBERT

IPC: B65G69/04 ,  C21B13/00 ,  F26B3/08 ,  F26B25/00 ,  F27B15/08 ,  F27D3/00

Abstract: According to the method, granular ore or ore concentrate is introduced into a kiln (1) for roasting the ore at temperatures of 400 to 1050 degrees C, whereby the ore in the kiln forms a stationary fluidised bed (3). The ore is projected onto the fluidised bed through an opening (16) in the kiln housing located above said fluidised bed, the ore being accelerated by the blades (14) of a rotating projection wheel. Said projection wheel (14) lies outside the kiln in the vicinity of the housing opening. Preferably, the speed of the projection wheel is variable and the projection wheel can be displaced and/or pivoted in relation to the kiln (1). 6 claims, 2 figures

公开(公告)号：AU2003296631A1

公开(公告)日：2004-07-14

申请号：AU2003296631

申请日：2003-12-10

Applicant: OUTOKUMPU OY

Inventor： STRODER MICHAEL ,  ANASTASIJEVIC NIKOLA ,  RUNKEL MARCUS

IPC: B01J8/18 ,  B01J8/26 ,  B01J8/28 ,  C22B1/10 ,  C22B15/00 ,  F27B15/02 ,  F27B15/08

Abstract: The invention relates to a method and a plant for the heat treatment of sulfidic ores, in which solids are heated to a temperature of approximately 450 to 1500° C. in a fluidized bed reactor ( 1 ). In order to improve the energy utilization, it is proposed to introduce a first gas or gas mixture from below through a gas supply tube ( 3 ) into a mixing chamber ( 7 ) of the reactor ( 1 ), the gas supply tube ( 3 ) being at least partly surrounded by a stationary annular fluidized bed ( 35 ) which is fluidized by supplying fluidizing gas. The gas velocities of the first gas or gas mixture as well as of the fluidizing gas for the annular fluidized bed ( 35 ) are adjusted such that the particle Froude numbers in the gas supply tube ( 3 ) are between 1 and 100, in the annular fluidized bed ( 35 ) between 0.02 and 2 and in the mixing chamber ( 7 ) between 0.3 and 30.

公开(公告)号：AU2003290002A1

公开(公告)日：2004-07-14

申请号：AU2003290002

申请日：2003-12-10

Applicant: OUTOKUMPU OY

Inventor： NUBER DIRK ,  STOCKHAUSEN WERNER ,  STRODER MICHAEL

IPC: B01J8/00 ,  B01J8/18 ,  C04B11/028 ,  F27B15/02 ,  F27B15/10 ,  F27B15/16

Abstract: The present invention relates to a method for the heat treatment of fine-grained solids, in particular gypsum, in which the solids are heated to a temperature of 50 to 1000° C. in a fluidized bed reactor (1), and to a corresponding plant. To improve the energy utilization, it is proposed to introduce a first gas or gas mixture from below through a preferably central gas supply tube (3) into a mixing chamber (21) of the reactor (1), the gas supply tube (3) being at least partly surrounded by a stationary annular fluidized bed (2) which is fluidized by supplying fluidizing gas, and to adjust the gas velocities of the first gas or gas mixture as well as of the fluidizing gas for the annular fluidized bed (2) such that the particle Froude numbers in the gas supply tube (3) are between 1 and 100, in the annular fluidized bed (2) between 0.02 and 2 and in the mixing chamber (21) between 0.3 and 30.

公开(公告)号：AU2003288060A1

公开(公告)日：2004-07-14

申请号：AU2003288060

申请日：2003-11-14

Applicant: OUTOKUMPU OY

Inventor： HASSELWANDER KLAUS ,  STRODER MICHAEL ,  SNEYD STUART

IPC: B01D53/12 ,  B01D53/50 ,  B01D53/68 ,  B01J8/18 ,  B01J8/24

Abstract: The present invention relates to a method for removing gaseous pollutants from exhaust gases, in which the gaseous pollutants react with a fine-grained reactant by forming solids in a fluidized-bed reactor (2), and to a corresponding plant. To achieve low pollutant concentrations in the clean gas with an almost stoichiometric consumption of reactant, it is proposed to introduce the exhaust gas from below through a preferably central gas supply tube ( 20 ) into a mixing chamber ( 21 ) of the reactor ( 2 ), the gas supply tube ( 20 ) being at least partly surrounded by a stationary annular fluidized bed ( 22 ) of reactant, which bed is fluidized by supplying fluidizing gas, and to adjust the the gas velocities of the exhaust gas and of the fluidizing gas for the annular fluidized bed ( 22 ) such that the Particle-Froude-Numbers in the gas supply tube ( 20 ) are between 1 and 100, in the annular fluidized bed ( 22 ) between 0.02 and 2, and in the mixing chamber ( 21 ) between 0.3 and 30.

公开(公告)号：AU3452902A

公开(公告)日：2002-06-18

申请号：AU3452902

申请日：2001-11-27

Applicant: OUTOKUMPU OY

Inventor： STRODER MICHAEL ,  ZINGREBE HORST ,  VOLLMER HUBERT

IPC: B65G69/04 ,  C21B13/00 ,  F26B3/08 ,  F26B25/00 ,  F27B15/08 ,  F27D3/00

Abstract: Granular ore or ore concentrate is charged into a furnace for calcining the ore at temperatures of 400 to 1050° C., the ore forming a stationary fluidized bed in the furnace. The ore is thrown onto the fluidized bed through an opening in the furnace housing disposed above the fluidized bed, the ore being accelerated by blades of a rotating impeller. The impeller is disposed outside the furnace in the vicinity of the opening of the housing. Preferably, the rotational speed of the impeller is variable, and the impeller is movable and/or pivotable with respect to the furnace.