NO845133L - DEVICE FOR IMPROVING THE HEAT ECONOMY IN ROTATION OVEN - Google Patents
DEVICE FOR IMPROVING THE HEAT ECONOMY IN ROTATION OVENInfo
- Publication number
- NO845133L NO845133L NO84845133A NO845133A NO845133L NO 845133 L NO845133 L NO 845133L NO 84845133 A NO84845133 A NO 84845133A NO 845133 A NO845133 A NO 845133A NO 845133 L NO845133 L NO 845133L
- Authority
- NO
- Norway
- Prior art keywords
- screens
- oven
- mesa
- kiln
- improving
- Prior art date
Links
- 238000001035 drying Methods 0.000 claims description 9
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 11
- 239000003546 flue gas Substances 0.000 description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 8
- 239000000292 calcium oxide Substances 0.000 description 6
- 235000012255 calcium oxide Nutrition 0.000 description 6
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
Classifications
-
- 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
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
- F27B7/14—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge
- F27B7/16—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge the means being fixed relatively to the drum, e.g. composite means
- F27B7/166—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge the means being fixed relatively to the drum, e.g. composite means the means comprising chains
-
- 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
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
- F27B7/14—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge
- F27B7/16—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge the means being fixed relatively to the drum, e.g. composite means
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
- Treatment Of Sludge (AREA)
- Incineration Of Waste (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
- Constitution Of High-Frequency Heating (AREA)
- Ultra Sonic Daignosis Equipment (AREA)
- Drying Of Solid Materials (AREA)
Description
Den foreliggende oppfinnelse vedrører en anordning for forbedring av varmeøkonomien i rotasjonsovner, fortrinnsvis i slike for ombrenning av mesa. The present invention relates to a device for improving the heat economy in rotary kilns, preferably in those for reburning mesa.
Oppfinnelsen skal beskrives i forbindelse med ombrenning av mesa, men omfatter alle tilfeller av godsbehandling i rotasjonsovn som har gasstrømnings- og materialomrøringsforløp lignende dem i en mesaombrenningsovn. The invention is to be described in connection with the reburning of mesa, but includes all cases of goods treatment in a rotary kiln that has gas flow and material stirring processes similar to those in a mesa reburning furnace.
Mesaen er det kalsiumkarbonatslam som oppstår ved kaustisering av grønnlut med brent kalk i forbindelse med kjemikaliegjen-vinningen i sulfatmassefabrikkene. The mesa is the calcium carbonate sludge that results from the causticisation of green liquor with burnt lime in connection with the chemical recovery in the sulphate pulp factories.
Brent kalk som er nødvendig for kaustiseringen, fåes i over-veiende grad gjennom ombrenning av mesaen, vanligvis i rotasjonsovn. Quicklime, which is required for causticisation, is mainly obtained by re-burning the mesa, usually in a rotary kiln.
Rotasjonsovnen heller noe slik at mesaen som innføres gjennom ovnens øvre ende kommer til å bevege seg som følge av at ovnen roterer mot ovnens nedre ende og møter røkgassene fra en oljebrenner i ovnens nedre ende, hvorved den omvandles til brent kalk. Denne mates ut i ovnens nedre ende. The rotary kiln tilts slightly so that the mesa introduced through the upper end of the kiln moves as a result of the kiln rotating towards the lower end of the kiln and meets the flue gases from an oil burner at the lower end of the kiln, whereby it is converted into quicklime. This is fed out at the lower end of the oven.
Mesaen tilføres rotasjonsovnen med en tørrgehalt på 60-75%. Rotasjonsovnen inndeles vanligvis i tre soner, tørkesone, mellomsone og brennsone. The mesa is fed to the rotary kiln with a dry matter content of 60-75%. The rotary kiln is usually divided into three zones, drying zone, intermediate zone and burning zone.
Tørkesonen som normalt er ca. en fjerdedel av ovnslengden, er for en stor del forsynt med slakt hengende kjettinger som er festet med sine begge ender i ovnsveggen, i den hensikt å The drying zone, which is normally approx. a quarter of the length of the oven, is for the most part provided with slack hanging chains which are fixed at both ends in the oven wall, with the intention of
røre om mesaen slik at en hurtig og effektiv tørking av denne oppnås. stir the mesa so that a quick and efficient drying of this is achieved.
Mellomsonen som utgjør ca. halvparten av ovnslengden, er nå oftest forsynt helt eller delvis, med langsgående fra ovnsveggen utgående medbringere for omrøring av det finkornede The middle zone, which makes up approx. half of the length of the furnace, is now most often provided in whole or in part, with longitudinal conveyors emanating from the furnace wall for stirring the fine-grained
materialet, slik at varmeoverføringen blir bedre. the material, so that the heat transfer is improved.
Brennsonen der kalsineringen av kalsiumkarbonatet til kalsiumoksyd skjer ved en temperatur som overskrider 900°C, vanligvis 1000-1200°C, er kledd med høyverdig ildfast og isolerende materiale. The combustion zone where the calcination of the calcium carbonate to calcium oxide takes place at a temperature exceeding 900°C, usually 1000-1200°C, is lined with high-quality refractory and insulating material.
Røkgassene forlater rotasjonsovnen med en temperatur normalt mellom 170 og 240°C. The flue gases leave the rotary kiln at a temperature normally between 170 and 240°C.
Målinger ved konvensjonell drift av mesaombrenningsovner har vist betydelig meget høyere temperatur i den utgående røk-gassen enn på ovnsveggen. Derav kan den konklusjon trekkes at meget av røkgassen går gjennom ovnens sentrum med be-grenset varmeoverføring til mesaen. Measurements during conventional operation of mesa reburning furnaces have shown a significantly higher temperature in the outgoing flue gas than on the furnace wall. From this, the conclusion can be drawn that much of the flue gas passes through the center of the furnace with limited heat transfer to the mesa.
Ifølge oppfinnelsen kan varmeoverføringen fra røkgassen til mesaen forbedres, og derved betydelige energimengder spares ved sentralt i ovnens tørke- og mellomsoner, å henge inn skjermer hvilke tvinger røkgasstrømmen ut mot periferien. According to the invention, the heat transfer from the flue gas to the mesa can be improved, thereby saving significant amounts of energy by hanging screens in the center of the oven's drying and intermediate zones which force the flow of flue gas out towards the periphery.
Skjermene er hensiktsmessig konformede, og så store at de hver dekker 15-30% av ovnsrommets tverrsnittsareale. Skjermene festes med kjettinger i ovnsveggen, slik at deres sentrum faller sammen med ovntverrsnittets sentrum. Konens spiss rettes mot gasstrømmen (mot ovnens nedre ende). The screens are suitably conformed, and so large that they each cover 15-30% of the oven room's cross-sectional area. The screens are attached with chains to the oven wall, so that their center coincides with the center of the oven cross-section. The tip of the cone is directed towards the gas flow (towards the lower end of the oven).
Det er vanligvis tilstrekkelig med 3-5 skjermer plassert It is usually sufficient to place 3-5 screens
med jevne mellomrom i tørke- og mellomsonen. at regular intervals in the drying and intermediate zones.
Gjennom arrangementet forhindres en trekksone i Through the event, a draft zone is prevented
roterovnen og den varmere røkgassen som normalt strømmer i sentrum av ovnen, presses ut mot periferien og blandes med den kaldere røkgassen, hvorved en betydelig forbedring av varmeoverføringen til kalkmaterialet oppnås, hvilket påvirker varmeøkonomien i gunstig retning. the rotary kiln and the warmer flue gas that normally flows in the center of the kiln is pushed out towards the periphery and mixed with the colder flue gas, whereby a significant improvement in the heat transfer to the lime material is achieved, which affects the heat economy in a favorable direction.
Gjennom fremgangsmåten kan kjettingene i tørkesonen helt Through the procedure, the chains in the drying zone can completely
fjernes eller forkortes til et minimum. removed or shortened to a minimum.
Oppfinnelsen beskrives i det etterfølgende med et eksempel The invention is described below with an example
fra praktisk tilpasning med henvisning til tegningens fig.1 from practical adaptation with reference to the drawing's fig.1
og 2 . and 2 .
I fig. 1 betegner 1 rotasjonsovnen, 2 ovnens nedre ende med oljebrenner 3, 4 skrue for innmating av mesaen, 5 utløpet for røkgassene, 6 utløpet for den brente kalk, 7,8 og 9 skjermer ifølge oppfinnelsen. In fig. 1 denotes 1 the rotary kiln, 2 the lower end of the kiln with oil burner 3, 4 screw for feeding the mesa, 5 the outlet for the flue gases, 6 the outlet for the burnt lime, 7,8 and 9 screens according to the invention.
Fig. 2 viser en skjerm 10 opphengt med kjettinger 11 i ovnsveggen 1 2. Fig. 2 shows a screen 10 suspended by chains 11 in the oven wall 1 2.
I en rotasjonsovn 1 ble det plassert tre skjermer 7,8,9 Three screens 7,8,9 were placed in a rotary kiln 1
ifølge oppfinnelsen på 15 m (7),25 m(8)og 35 m (9) fra ovnens øvre ende der innmatingsskruen 4 for mesaen sitter. according to the invention at 15 m (7), 25 m (8) and 35 m (9) from the upper end of the furnace where the feed screw 4 for the mesa is located.
Skjermene 7,8,9 dekket hver 15% av ovnsrommets tverrsnittsareal . Screens 7,8,9 each covered 15% of the furnace room's cross-sectional area.
Rotasjonsovnens 1 lengde var 87 m og innerdiameter 3,15 m. The length of the rotary kiln 1 was 87 m and the inner diameter 3.15 m.
Den var helt uten kjettinger i tørkesonen. It was completely without chains in the drying zone.
Gjennom denne endring ifølge oppfinnelsen sank temperaturen Through this change according to the invention, the temperature decreased
på den utgående røkgass med 40°C, dvs. ved normal kalk-produksjon fra 170-180°C før endringen til 130-140°C etter endringen. Senkningen av røkgasstemperaturen tilsvarer en oljebesparing på ca. 7 liter pr. tonn produkt (90% CaO). on the outgoing flue gas by 40°C, i.e. with normal lime production from 170-180°C before the change to 130-140°C after the change. The lowering of the flue gas temperature corresponds to an oil saving of approx. 7 liters per tonnes of product (90% CaO).
Claims (5)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE8400578A SE8400578L (en) | 1984-02-06 | 1984-02-06 | DEVICE FOR IMPROVING HEATING ECONOMY IN ROOT OVEN |
Publications (1)
Publication Number | Publication Date |
---|---|
NO845133L true NO845133L (en) | 1985-08-05 |
Family
ID=20354603
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO84845133A NO845133L (en) | 1984-02-06 | 1984-12-20 | DEVICE FOR IMPROVING THE HEAT ECONOMY IN ROTATION OVEN |
Country Status (5)
Country | Link |
---|---|
ES (1) | ES8602241A1 (en) |
FI (2) | FI75884C (en) |
FR (1) | FR2559246A1 (en) |
NO (1) | NO845133L (en) |
SE (1) | SE8400578L (en) |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR414845A (en) * | 1910-04-15 | 1910-09-12 | Jean Albert Paul Lavocat | Improvements in cement kilns |
FR609023A (en) * | 1925-01-07 | 1926-08-06 | Rotary drum for cooling or processing materials using an air stream | |
FR820464A (en) * | 1936-04-14 | 1937-11-12 | Improvements to rotary kilns | |
FR1220585A (en) * | 1958-05-21 | 1960-05-25 | Fellner & Ziegler Gmbh | Rotary oven for firing cements, magnesite, lime, plaster or similar products |
-
1984
- 1984-02-06 SE SE8400578A patent/SE8400578L/en unknown
- 1984-06-08 FI FI842335A patent/FI75884C/en not_active IP Right Cessation
- 1984-12-03 FR FR8418387A patent/FR2559246A1/en active Pending
- 1984-12-20 NO NO84845133A patent/NO845133L/en unknown
-
1985
- 1985-01-15 ES ES85539584A patent/ES8602241A1/en not_active Expired
- 1985-01-21 FI FI850260A patent/FI850260L/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
FR2559246A1 (en) | 1985-08-09 |
FI75884B (en) | 1988-04-29 |
ES539584A0 (en) | 1985-11-16 |
FI842335A (en) | 1985-08-07 |
FI75884C (en) | 1988-08-08 |
SE8400578D0 (en) | 1984-02-06 |
FI842335A0 (en) | 1984-06-08 |
FI850260L (en) | 1985-08-07 |
SE8400578L (en) | 1985-08-07 |
ES8602241A1 (en) | 1985-11-16 |
FI850260A0 (en) | 1985-01-21 |
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