[go: up one dir, main page]

NO845133L - DEVICE FOR IMPROVING THE HEAT ECONOMY IN ROTATION OVEN - Google Patents

DEVICE FOR IMPROVING THE HEAT ECONOMY IN ROTATION OVEN

Info

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
Application number
NO84845133A
Other languages
Norwegian (no)
Inventor
Bertil Pettersson
Original Assignee
Termorak Oy
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Termorak Oy filed Critical Termorak Oy
Publication of NO845133L publication Critical patent/NO845133L/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B7/00Rotary-drum furnaces, i.e. horizontal or slightly inclined
    • F27B7/14Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge
    • F27B7/16Rotary-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
    • F27B7/166Rotary-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B7/00Rotary-drum furnaces, i.e. horizontal or slightly inclined
    • F27B7/14Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge
    • F27B7/16Rotary-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)

1. Anordning for vesentlig forbedring av varmeøkonomien ved drift av rotasjonsovner, spesielt mesaombrenningsovner,karakterisert vedat det sentralt i ovnens (1) tørke- og mellomsoner er hengt inn skjermer (7,8,9) hvilke hver opptar 15-30% av ovnsrommets tverrsnittsareal.1. Device for significantly improving the heat economy when operating rotary kilns, especially mesa reburning kilns, characterized in that screens (7,8,9) are hung centrally in the drying and intermediate zones of the kiln (1), each of which occupies 15-30% of the cross-sectional area of the kiln chamber . 2. Anordning ifølge krav 1,karakterisert vedat antall skjermer (7,8,9) er 3-5.2. Device according to claim 1, characterized in that the number of screens (7,8,9) is 3-5. 3. Anordning ifølge krav 1,karakterisert vedat skjermene (7,8,9) er plassert med jevne mellom i tørke-og mellomsonene.3. Device according to claim 1, characterized in that the screens (7,8,9) are placed at regular intervals in the drying and intermediate zones. 4. Anordning ifølge krav 1,karakterisert vedat skjermene er koniske og at deres spiss er rettet mot ovnens nedre ende (2).4. Device according to claim 1, characterized in that the screens are conical and that their tip is directed towards the lower end of the oven (2). 5. Anordning ifølge krav 1,karakterisert vedat skjermene (10) er festet med kjeder (11) i ovnsveggen (12).5. Device according to claim 1, characterized in that the screens (10) are fixed with chains (11) in the oven wall (12).
NO84845133A 1984-02-06 1984-12-20 DEVICE FOR IMPROVING THE HEAT ECONOMY IN ROTATION OVEN NO845133L (en)

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)

* Cited by examiner, † Cited by third party
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

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

Similar Documents

Publication Publication Date Title
DK170368B1 (en) Process for incinerating waste in a cement kiln plant, as well as plant for carrying out the process
CA1042663A (en) Method of burning pulverous raw material and rotary kiln plant therefor
JPS6158406B2 (en)
SU631088A3 (en) Method of heat treatment of fine grainy material
RU2181866C1 (en) Roasting plant and process for making cement
DK172100B1 (en) Process for heat treatment of lime sludge, as well as systems for carrying out the process
US4952147A (en) Lime sludge kiln
US4915623A (en) Calcination apparatus
NO123731B (en)
NO845133L (en) DEVICE FOR IMPROVING THE HEAT ECONOMY IN ROTATION OVEN
CA1159647A (en) Calcining furnace with gas-permeable wall structure
US2603476A (en) Circular open hearth melting furnace
US2225199A (en) Multiple hearth calcining furnace
AU689188B2 (en) Improved kiln
US2373749A (en) Apparatus for the manufacture of magnesium oxide
CN2199205Y (en) Indirect heating calciner for active lime
NO166252B (en) ARRANGEMENTS FOR IMPROVING THE HEAT ECONOMY OF OPERATION AVROTATION OVEN, SPECIAL MESA BURNT Ovens.
CN218665796U (en) Large-treatment-capacity double-hearth lime kiln
SU476427A1 (en) Shaft furnace
CN2876087Y (en) Environmental protection energy saving lime calcining furnace
SU1315478A1 (en) Method for roasting sideritic ores and shaft furnace for effecting same
RU2175310C2 (en) Device for production of cement clinker
US307924A (en) Furnace for the calcination of ores
RU2063594C1 (en) Method of roasting carbonate raw material and regenerative shaft furnace for roasting carbonate raw material
US3321559A (en) Kiln operation