PL424587A1 - Method of and the device for roasting dry ore particles in a fluidized-bed layer - Google Patents
Method of and the device for roasting dry ore particles in a fluidized-bed layerInfo
- Publication number
- PL424587A1 PL424587A1 PL424587A PL42458716A PL424587A1 PL 424587 A1 PL424587 A1 PL 424587A1 PL 424587 A PL424587 A PL 424587A PL 42458716 A PL42458716 A PL 42458716A PL 424587 A1 PL424587 A1 PL 424587A1
- Authority
- PL
- Poland
- Prior art keywords
- particles
- fluidized
- ore particles
- bed layer
- dry ore
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/02—Roasting processes
- C22B1/10—Roasting processes in fluidised form
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1818—Feeding of the fluidising gas
- B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1836—Heating and cooling the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/44—Fluidisation grids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
- F27B15/02—Details, accessories, or equipment peculiar to furnaces of these types
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
- F27B15/02—Details, accessories, or equipment peculiar to furnaces of these types
- F27B15/08—Arrangements of devices for charging
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/0015—Plates; Cylinders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00654—Controlling the process by measures relating to the particulate material
- B01J2208/00681—Agglomeration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00752—Feeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00769—Details of feeding or discharging
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00991—Disengagement zone in fluidised-bed reactors
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- Dispersion Chemistry (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
Abstract
Wynalazek odnosi się do sposobu prażenia cząstek rudy obejmujących węgiel i/lub siarkę, w którym w celu wyprażenia cząstki wprowadza się do reaktora (11). Ponadto, wprowadza się zawierający tlen gaz, przy czym cząstki praży się w złożu fluidalnym w temperaturze od 500 do 1000°C przez co najmniej 10 sekund i przy czym wyprażone cząstki usuwa się z reaktora. Cząstki te charakteryzują się zawartością wody wynoszącą maksymalnie 2% wag. i są wtryskiwane pneumatycznie do złoża fluidalnego.The invention relates to a method of roasting ore particles comprising carbon and / or sulfur, in which particles are introduced into a reactor (11) for roasting. In addition, oxygen-containing gas is introduced, the particles being calcined in a fluidized bed at a temperature of 500 to 1000 ° C for at least 10 seconds, and the calcined particles are removed from the reactor. These particles have a water content of max. 2 wt. and are pneumatically injected into the fluidized bed.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102015110772.4 | 2015-07-03 | ||
DE102015110772.4A DE102015110772A1 (en) | 2015-07-03 | 2015-07-03 | Method and plant for roasting dry ore particles in a fluidized bed |
PCT/EP2016/064589 WO2017005501A1 (en) | 2015-07-03 | 2016-06-23 | Process and plant for roasting of dry ore particles in a fluidized bed |
Publications (2)
Publication Number | Publication Date |
---|---|
PL424587A1 true PL424587A1 (en) | 2018-06-04 |
PL233905B1 PL233905B1 (en) | 2019-12-31 |
Family
ID=56263684
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PL424587A PL233905B1 (en) | 2015-07-03 | 2016-06-23 | Method of and the device for roasting dry ore particles in a fluidized-bed layer |
Country Status (5)
Country | Link |
---|---|
AU (1) | AU2016289602B2 (en) |
CL (1) | CL2017003360A1 (en) |
DE (1) | DE102015110772A1 (en) |
PL (1) | PL233905B1 (en) |
WO (1) | WO2017005501A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10717061B1 (en) * | 2019-06-26 | 2020-07-21 | X Energy, Llc | Fluidized bed reactor system allowing particle sampling during an ongoing reaction |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2483485A (en) * | 1947-12-31 | 1949-10-04 | Standard Oil Dev Co | High velocity fluid solids technique |
GB702620A (en) | 1951-10-26 | 1954-01-20 | Standard Telephones Cables Ltd | Improvements in or relating to dry contact rectifiers |
DE907417C (en) | 1950-09-09 | 1954-03-25 | Standard Oil Dev Co | Process for reducing Fe O in lean ores to Fe O |
DE976145C (en) | 1951-03-23 | 1963-03-28 | Metallgesellschaft Ag | Device for roasting sulfidic ores |
DE1091339B (en) * | 1959-06-18 | 1960-10-20 | Basf Ag | Process for the automatic control of the gradual roasting of roastable sulfur-containing materials |
YU34545B (en) * | 1970-05-29 | 1979-09-10 | Ammi Spa | Process for preparing antimony axide |
JPS5140541B1 (en) | 1971-05-26 | 1976-11-04 | ||
US3941867A (en) * | 1974-09-04 | 1976-03-02 | Canadian Patents And Development Limited | Production of molybdenum trioxide from molybdenite in a fluidized bed |
DE2624302C2 (en) * | 1976-05-31 | 1987-04-23 | Metallgesellschaft Ag, 6000 Frankfurt | Methods for carrying out exothermic processes |
CA1200074A (en) | 1982-01-25 | 1986-02-04 | James E. Hoffmann | Process for production of metal calcines of low sulfur content |
DE3534419C1 (en) | 1985-09-27 | 1987-05-27 | Rheinische Braunkohlenw Ag | Method of feeding fine-grained lignite into a gas-producing reactor |
US5320815A (en) * | 1987-07-13 | 1994-06-14 | E. I. Du Pont De Nemours And Company | Fluidized bed process |
AU596758B2 (en) * | 1987-11-13 | 1990-05-10 | Jp Steel Plantech Co. | Metal-making apparatus involving the smelting reduction of metallic oxides |
DE19609284A1 (en) * | 1996-03-09 | 1997-09-11 | Metallgesellschaft Ag | Treating granular sulphidic ores containing gold and/or silver |
KR100276339B1 (en) * | 1996-12-23 | 2000-12-15 | 이구택 | Three-stage Fluidized Bed Reduction Apparatus for Ferrous Iron Ore with X-shaped Circulation Tube |
DE202005021660U1 (en) | 2005-10-04 | 2009-03-05 | Siemens Aktiengesellschaft | Apparatus for the controlled supply of combustible dust in an air flow gasifier |
-
2015
- 2015-07-03 DE DE102015110772.4A patent/DE102015110772A1/en not_active Withdrawn
-
2016
- 2016-06-23 PL PL424587A patent/PL233905B1/en unknown
- 2016-06-23 WO PCT/EP2016/064589 patent/WO2017005501A1/en active Application Filing
- 2016-06-23 AU AU2016289602A patent/AU2016289602B2/en not_active Ceased
-
2017
- 2017-12-26 CL CL2017003360A patent/CL2017003360A1/en unknown
Also Published As
Publication number | Publication date |
---|---|
PL233905B1 (en) | 2019-12-31 |
WO2017005501A1 (en) | 2017-01-12 |
CL2017003360A1 (en) | 2018-05-11 |
DE102015110772A1 (en) | 2017-01-05 |
AU2016289602B2 (en) | 2019-04-04 |
AU2016289602A1 (en) | 2018-02-01 |
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