ZA200201890B - Device for thermally treating granular solid matter. - Google Patents
Device for thermally treating granular solid matter.Info
- Publication number
- ZA200201890B ZA200201890B ZA200201890A ZA200201890A ZA200201890B ZA 200201890 B ZA200201890 B ZA 200201890B ZA 200201890 A ZA200201890 A ZA 200201890A ZA 200201890 A ZA200201890 A ZA 200201890A ZA 200201890 B ZA200201890 B ZA 200201890B
- Authority
- ZA
- South Africa
- Prior art keywords
- solid matter
- reactor
- thermally treating
- granular solid
- treating granular
- Prior art date
Links
- 239000007787 solid Substances 0.000 title abstract 8
- 239000007789 gas Substances 0.000 abstract 3
- 239000000567 combustion gas Substances 0.000 abstract 2
- 239000000446 fuel Substances 0.000 abstract 2
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 238000003260 vortexing Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- 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
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/14—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moving in free vortex flow apparatus
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2405—Stationary reactors without moving elements inside provoking a turbulent flow of the reactants, such as in cyclones, or having a high Reynolds-number
-
- 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
- B01J6/00—Heat treatments such as Calcining; Fusing ; Pyrolysis
- B01J6/001—Calcining
- B01J6/004—Calcining using hot gas streams in which the material is moved
-
- 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
- B01J6/00—Heat treatments such as Calcining; Fusing ; Pyrolysis
- B01J6/008—Pyrolysis reactions
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/02—Aluminium oxide; Aluminium hydroxide; Aluminates
- C01F7/44—Dehydration of aluminium oxide or hydroxide, i.e. all conversions of one form into another involving a loss of water
- C01F7/441—Dehydration of aluminium oxide or hydroxide, i.e. all conversions of one form into another involving a loss of water by calcination
- C01F7/444—Apparatus therefor
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
- B01J2219/00112—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00159—Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/18—Details relating to the spatial orientation of the reactor
- B01J2219/182—Details relating to the spatial orientation of the reactor horizontal
Abstract
The invention relates to a device for thermally treating granular solid matter for the purpose of carrying out endothermic reactions. CO2 and/or water is removed from the solid matter in a reactor by burning fuel to generate a combustion gas in the reactor, vortexing the solid matter with the combustion gases in the reactor, using hot exhaust gas from the reactor to pre-heat the solid matter and removing the solid matter from the reactor. The reactor used is an approximately cylindrical, horizontal cyclone with an approximately horizontal axis of symmetry and vortex. Fuel, solid matter and gases are supplied in an inlet zone of the reactor while a rotation vortex is formed in said inlet zone and solid matter and hot gas are removed from an outlet zone of the reactor.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19944778A DE19944778B4 (en) | 1999-09-17 | 1999-09-17 | Process for the thermal treatment of granular solids |
Publications (1)
Publication Number | Publication Date |
---|---|
ZA200201890B true ZA200201890B (en) | 2002-12-24 |
Family
ID=7922482
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ZA200201890A ZA200201890B (en) | 1999-09-17 | 2002-03-07 | Device for thermally treating granular solid matter. |
Country Status (11)
Country | Link |
---|---|
EP (1) | EP1212260B1 (en) |
CN (1) | CN1197776C (en) |
AT (1) | ATE248771T1 (en) |
AU (1) | AU778126B2 (en) |
BR (1) | BR0014085B1 (en) |
CA (1) | CA2384957A1 (en) |
DE (2) | DE19944778B4 (en) |
EA (1) | EA004496B1 (en) |
ES (1) | ES2204657T3 (en) |
WO (1) | WO2001021530A1 (en) |
ZA (1) | ZA200201890B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100406104C (en) * | 2005-01-26 | 2008-07-30 | 中国铝业股份有限公司 | Clinker dissolving out milled dust collecting method and washing tower thereof |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3752455A (en) * | 1969-08-21 | 1973-08-14 | Prerovske Strojirny Np | Arrangement for burning of pulverulent and fine grain material |
DE2048207A1 (en) * | 1970-10-01 | 1972-04-06 | Kloeckner Humboldt Deutz Ag | Equipment for the production of alumina from alumina hydrate |
GB2019369B (en) * | 1978-04-20 | 1982-12-01 | Smidth & Co As F L | Production of anhydrous alumina |
RU1806309C (en) * | 1989-03-03 | 1993-03-30 | Научно-технический центр "Новатор" Приморского краевого совета ВОИР | Horizontal cyclone furnace |
US5616303A (en) * | 1994-10-11 | 1997-04-01 | Gas Research Institute | Centrifugal bed reactor |
DE19542309A1 (en) * | 1995-11-14 | 1997-05-15 | Metallgesellschaft Ag | Process for the production of aluminum oxide from aluminum hydroxide |
-
1999
- 1999-09-17 DE DE19944778A patent/DE19944778B4/en not_active Expired - Fee Related
-
2000
- 2000-07-03 BR BRPI0014085-6A patent/BR0014085B1/en not_active IP Right Cessation
- 2000-07-03 EA EA200200318A patent/EA004496B1/en not_active IP Right Cessation
- 2000-07-03 WO PCT/EP2000/006174 patent/WO2001021530A1/en active IP Right Grant
- 2000-07-03 CN CNB008144788A patent/CN1197776C/en not_active Expired - Fee Related
- 2000-07-03 CA CA002384957A patent/CA2384957A1/en not_active Abandoned
- 2000-07-03 AU AU61538/00A patent/AU778126B2/en not_active Ceased
- 2000-07-03 AT AT00947911T patent/ATE248771T1/en not_active IP Right Cessation
- 2000-07-03 DE DE50003573T patent/DE50003573D1/en not_active Expired - Fee Related
- 2000-07-03 EP EP00947911A patent/EP1212260B1/en not_active Expired - Lifetime
- 2000-07-03 ES ES00947911T patent/ES2204657T3/en not_active Expired - Lifetime
-
2002
- 2002-03-07 ZA ZA200201890A patent/ZA200201890B/en unknown
Also Published As
Publication number | Publication date |
---|---|
DE19944778B4 (en) | 2004-07-08 |
BR0014085B1 (en) | 2009-01-13 |
CA2384957A1 (en) | 2001-03-29 |
DE19944778A1 (en) | 2001-03-29 |
ATE248771T1 (en) | 2003-09-15 |
WO2001021530A1 (en) | 2001-03-29 |
EP1212260A1 (en) | 2002-06-12 |
AU6153800A (en) | 2001-04-24 |
EA004496B1 (en) | 2004-04-29 |
EP1212260B1 (en) | 2003-09-03 |
AU778126B2 (en) | 2004-11-18 |
CN1197776C (en) | 2005-04-20 |
CN1379734A (en) | 2002-11-13 |
ES2204657T3 (en) | 2004-05-01 |
EA200200318A1 (en) | 2002-10-31 |
BR0014085A (en) | 2002-05-21 |
DE50003573D1 (en) | 2003-10-09 |
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