WO1991000251A1 - Feeding system for a lime reburning kiln - Google Patents

Feeding system for a lime reburning kiln Download PDF

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Publication number
WO1991000251A1
WO1991000251A1 PCT/FI1990/000172 FI9000172W WO9100251A1 WO 1991000251 A1 WO1991000251 A1 WO 1991000251A1 FI 9000172 W FI9000172 W FI 9000172W WO 9100251 A1 WO9100251 A1 WO 9100251A1
Authority
WO
WIPO (PCT)
Prior art keywords
lime
lime mud
kiln
mud
reburning kiln
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
PCT/FI1990/000172
Other languages
French (fr)
Inventor
Arto Ahvenainen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ahlstrom Corp
Original Assignee
Ahlstrom Corp
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 Ahlstrom Corp filed Critical Ahlstrom Corp
Priority to EP90909734A priority Critical patent/EP0480960B1/en
Priority to DE69017449T priority patent/DE69017449T2/en
Priority to DE1990909734 priority patent/DE480960T1/en
Publication of WO1991000251A1 publication Critical patent/WO1991000251A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2/00—Lime, magnesia or dolomite
    • C04B2/10—Preheating, burning calcining or cooling
    • 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
    • F27B7/20—Details, accessories or equipment specially adapted for rotary-drum furnaces
    • F27B7/32—Arrangement of devices for charging
    • F27B7/3205—Charging
    • 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
    • F27B7/161—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 projections jutting out from the wall
    • F27B7/162—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 projections jutting out from the wall the projections consisting of separate lifting elements, e.g. lifting shovels
    • F27B2007/163—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 projections jutting out from the wall the projections consisting of separate lifting elements, e.g. lifting shovels using only a ring of lifting elements to lift the charge
    • 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
    • F27B7/20—Details, accessories or equipment specially adapted for rotary-drum furnaces
    • F27B2007/2008—Devices for reintroducing dust in the drum

Definitions

  • the present invention relates to a method and apparatus for feeding lime mud into a rotary kiln in order to re- generate the lime mud, which has been separated in connec ⁇ tion with causticizing process and is mainly CaC0 3 , to form CaO in the rotary kiln.
  • lime mud is introduced in a dry solids content of 60 through 70 % into the top end of a rotary kiln, wherefrom it slowly moves downwards through drying, heating and reaction zones.
  • chains are employed in the drying zone where heat is transferred from flue gases to the lime mud mainly through convection. The chains come into contact with lime mud when the kiln rotates. To obtain a good result, the heat treatment of the lime mud in the kiln has to take place slowly. For this purpose, the lime reburning kiln has to be long, consequently requiring a large space.
  • the object of the present invention is to provide a simple method and apparatus for introcuding lime mud into a rotary kiln.
  • Finnish patent application 890376 discloses thickening of lime mud in a lime filter to a dryness of over 75%, whereby it is possible to introduce the lime mud directly into a
  • the lime mud coming from the filter is fed by means of a feed screw to the same channel from which the lime mud is introduced either into a pneumatic dryer or directly into the lime reburning kiln, or both, depending on the dry solids content and particle size of the lime mud.
  • the lime mud is fed into a upwrardly moving gas flow which contains an adjustable portion of the flue gases discharged from the lime reburning kiln, that at least part of the lime mud fed into the gas flow is dried in a pneumatic dryer by means of flue gases, the remaining part possibly falling into a feeding means disposed in connection with the inlet or top end of the lime reburning kiln and that the lime mud dried in the dryer is separated from the flue gas and introduced into the lime reburning kiln.
  • the arrangement according to the invention provides, for example, the following advantages:
  • the end temperature of the dryer may be adjusted by changing the ratio between the gas amounts flowing through adjacent flow channels, consequently affecting the amount of lime mud entering the pneumatic dryer;
  • Fig. 1 is a schematic illustration of an apparatus suitable for carrying out the method according to the invention
  • Fig. 2 is a vertical, sectional view of a feeding system for a lime reburning kiln in accordance with the invention.
  • Fig. 3 is an illustration of the feeding system in the direction of travel of arrow A.
  • Fig. 1 shows the principle of a dryer-kiln system operating in accordance with the method of the invention.
  • the main parts of the apparatus shown in the figure are feed screw 1, feed chamber 2, drying pipe 3, separation cyclone 4 and rotary kiln 5.
  • Lime mud is thickened in a lime filter 6.
  • a belt conveyor 7 disposed underneath the filter receives the lime mud coming from the filter and then drops it into the feed screw 1.
  • the feed chamber includes an upper section 11, which is divided by a partition wall 8 into two adjacent, vertical flow channels 9 and 10 and which communicates with the vertical section of the drying pipe 3, and a lower section 14 which encases feed vanes 13 with shovel-formed extensions 12, said feed vanes being attached to the upper section of the rotary kiln.
  • the drying pipe 3 extends vertically upwardly from the feed pipe and is thereafter bent in the horizontal direction and connected tangentially to the top end of the cyclone 4.
  • the feed screw 1 opens to one of the adjacent chambers 9 of the feed chamber and doses the lime mud discharged from the filter thereinto.
  • the upper section of the partition wall 8 of the feed chamber is provided with a control baffle 15 for controlling or defining how much of the flue gas discharged from the lime reburning kiln 5 flows through each flow channel 9, 11. Thereby, depending on the position of the control baffle, only part of the flue gas or the entire amount thereof flows through the flow channel 9. The amount may range, for example, from 30 to 100 %.
  • the coarse and wet fraction of the lime mud introduced into the feed chamber falls into the lower section of the feed chamber.
  • the shovels 12 disposed at the end of the feed vanes 13 lift it up and the vanes lead it further into the kiln.
  • the lighter fraction is entrained with the flue gas into the cyclone 4 and is dried by the heat of the flue gas.
  • the solid material is separated from the gas in the cyclone and the dried lime mud is discharged from the lower end of the cyclone.
  • a conveyor 16, disposed underneath the cyclone transfers the dried lime mud into a return pipe 17 leading to the lower section 14 of the feed chamber.
  • the flue gas is removed from the cyclone via pipe 18.
  • the lime mud is introduced into the feed chamber in the dry solids content of over 75 %, preferably of 80 %, and it dries in the drying pipe by means of flue gases to a dry solids content of about 100 %.
  • the wet "precoat” discharged from the lime filter and introduced into the feed chamber 2 falls into the lower section of the feed chamber, wherefrom it is fed by means of vanes 13 into the lime reburning kiln.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Ceramic Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • General Engineering & Computer Science (AREA)
  • Treatment Of Sludge (AREA)
  • Drying Of Solid Materials (AREA)
  • Furnace Details (AREA)
  • Processing Of Solid Wastes (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Weting (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Bipolar Transistors (AREA)

Abstract

A method and apparatus for heat treatment of lime mud comprises drying of the lime mud to be introduced into the lime reburning kiln (5) in a pneumatic dryer (3) by means of flue gases discharged from the lime reburning kiln in order to regenerate the lime content of the lime mud. From a drying filter (6), the lime mud thickened to a dry solids content of over 75 %, preferably to 80 %, is introduced into a feed chamber (2) through which an adjustable portion of the flue gas is conducted. Depending on the gas amount, 100 % or less of the lime mud is entrained with the gas into the dryer (3), the remaining portion falling into the lower section (14) of the feed chamber, wherefrom it is further transferred into the lime reburning kiln (5).

Description

Feeding system for a lime reburning kiln
The present invention relates to a method and apparatus for feeding lime mud into a rotary kiln in order to re- generate the lime mud, which has been separated in connec¬ tion with causticizing process and is mainly CaC03 , to form CaO in the rotary kiln.
In previously known apparatuses, lime mud is introduced in a dry solids content of 60 through 70 % into the top end of a rotary kiln, wherefrom it slowly moves downwards through drying, heating and reaction zones. To improve the heat transfer, chains are employed in the drying zone where heat is transferred from flue gases to the lime mud mainly through convection. The chains come into contact with lime mud when the kiln rotates. To obtain a good result, the heat treatment of the lime mud in the kiln has to take place slowly. For this purpose, the lime reburning kiln has to be long, consequently requiring a large space.
It has been possible to shorten a lime reburning kiln by drying and preheating the lime mud in pneumatic dryers with flue gas prior to introducing the lime mud into the lime reburning kiln.
Since it is difficult to handle wet lime mud obtained from the filter, it has been mixed with dried lime mud before introducing it into a pneumatic dryer. The equipment needed for the pretreatment of lime mud has been complex and it has required a complicated control and regulating system.
The object of the present invention is to provide a simple method and apparatus for introcuding lime mud into a rotary kiln.
Finnish patent application 890376 discloses thickening of lime mud in a lime filter to a dryness of over 75%, whereby it is possible to introduce the lime mud directly into a
Figure imgf000003_0001
pneumatic dryer without the necessity of using hammer mills or mixing screws for crushing the lumps. The lime mud is so dry that the dryer will remain open. Another point of feeding lime mud is, however, still needed for the lime reburning kiln. When the "precoat" of the lime mud filter is replaced, it is not desirable to feed the wet lump of lime mud into the pneumatic dryer because there is a risk of the dryer becoming clogged, but the lime mud is introduced directly into the lime reburning kiln by means of a separate feed screw.
In the feeding system according to the invention, the lime mud coming from the filter is fed by means of a feed screw to the same channel from which the lime mud is introduced either into a pneumatic dryer or directly into the lime reburning kiln, or both, depending on the dry solids content and particle size of the lime mud.
It is a main characteristic feature of the method according to the invention that the lime mud is fed into a upwrardly moving gas flow which contains an adjustable portion of the flue gases discharged from the lime reburning kiln, that at least part of the lime mud fed into the gas flow is dried in a pneumatic dryer by means of flue gases, the remaining part possibly falling into a feeding means disposed in connection with the inlet or top end of the lime reburning kiln and that the lime mud dried in the dryer is separated from the flue gas and introduced into the lime reburning kiln.
It is a characteristic feature of the apparatus according to the invention that it comprises a feed chamber with the upper section thereof being divided by a partition wall into two adjacent, substantially vertical flow channels and connected to a substantially vertical part of a drying pipe leading to a cyclone, and with the lower section thereof encasing the feeding means disposed at the top end of the lime reburning kiln, a control baffle inserted in the upper section of the partition wall, a feed screw or equiva¬ lent for dosing lime . mud into one of the feed chambers from adjacent flow channels, and means for introducing dried lime mud which has been separated in the cyclone into the lower section of the feed chamber.
The arrangement according to the invention provides, for example, the following advantages:
- simple and inexpensive construction;
- distribution of lime mud into the dryer/kiln requires no special measures to be taken;
- the end temperature of the dryer may be adjusted by changing the ratio between the gas amounts flowing through adjacent flow channels, consequently affecting the amount of lime mud entering the pneumatic dryer;
- fluctuations of the dry solids content at the lime filter do not cause alterations to the end temperature of the dryer.
The invention is described in more detail below, by way of example, with reference to the accompanying drawings, in which
Fig. 1 is a schematic illustration of an apparatus suitable for carrying out the method according to the invention;
Fig. 2 is a vertical, sectional view of a feeding system for a lime reburning kiln in accordance with the invention; and
Fig. 3 is an illustration of the feeding system in the direction of travel of arrow A.
Fig. 1 shows the principle of a dryer-kiln system operating in accordance with the method of the invention. The main parts of the apparatus shown in the figure are feed screw 1, feed chamber 2, drying pipe 3, separation cyclone 4 and rotary kiln 5. Lime mud is thickened in a lime filter 6. A belt conveyor 7 disposed underneath the filter receives the lime mud coming from the filter and then drops it into the feed screw 1.
As shown in Figs 2 and 3, the feed chamber includes an upper section 11, which is divided by a partition wall 8 into two adjacent, vertical flow channels 9 and 10 and which communicates with the vertical section of the drying pipe 3, and a lower section 14 which encases feed vanes 13 with shovel-formed extensions 12, said feed vanes being attached to the upper section of the rotary kiln.
The drying pipe 3 extends vertically upwardly from the feed pipe and is thereafter bent in the horizontal direction and connected tangentially to the top end of the cyclone 4.
The feed screw 1 opens to one of the adjacent chambers 9 of the feed chamber and doses the lime mud discharged from the filter thereinto. The upper section of the partition wall 8 of the feed chamber is provided with a control baffle 15 for controlling or defining how much of the flue gas discharged from the lime reburning kiln 5 flows through each flow channel 9, 11. Thereby, depending on the position of the control baffle, only part of the flue gas or the entire amount thereof flows through the flow channel 9. The amount may range, for example, from 30 to 100 %.
The coarse and wet fraction of the lime mud introduced into the feed chamber falls into the lower section of the feed chamber. When rotating, the shovels 12 disposed at the end of the feed vanes 13 lift it up and the vanes lead it further into the kiln. The lighter fraction is entrained with the flue gas into the cyclone 4 and is dried by the heat of the flue gas. The solid material is separated from the gas in the cyclone and the dried lime mud is discharged from the lower end of the cyclone. A conveyor 16, disposed underneath the cyclone, transfers the dried lime mud into a return pipe 17 leading to the lower section 14 of the feed chamber. The flue gas is removed from the cyclone via pipe 18.
Depending on the amount of flue gas flowing through the flow chamber 9, i.e. on the flow rate of the gas, 100 % or less, for example, 50 % of the lime mud introduced into said flue gas is entrained with the gas into the drying pipe and dries therein.
The lime mud is introduced into the feed chamber in the dry solids content of over 75 %, preferably of 80 %, and it dries in the drying pipe by means of flue gases to a dry solids content of about 100 %.
The wet "precoat" discharged from the lime filter and introduced into the feed chamber 2 falls into the lower section of the feed chamber, wherefrom it is fed by means of vanes 13 into the lime reburning kiln.
The invention is not limited to the embodiment of the example described above, but its details may vary within the inventive scope defined by the accompanying claims.
'

Claims

We claim;
1. A method of introducing lime mud into a rotary kiln, characterized in that the lime mud is fed into an upwrardly moving gas flow which contains an adjustable portion of the flue gases discharged from a lime reburning kiln, that at least part of the lime mud fed into the gas flow is dried in a penumatic dryer by means of flue gases from the lime reburning kiln, any remaining part falling into a feeding means disposed in connection with the top or inlet end of the lime reburning kiln and that the lime mud dried in the dryer is separated from the flue gas and introduced into the lime reburning kiln.
2. A method as claimed in claim 1, characterized in that the lime mud is fed into the gas flow in a dry solids content exceeding 75 %.
3. A method as claimed in claim 1 or 2, characterized in that 50 to 100 % of the lime mud fed into the gas flow is dried in a pneumatic dryer.
4. A method as claimed in claim 1, 2 or 3, characterized in that the adjustable gas flow contains 30 to 100 % of the flue gases discharged from the lime reburning kiln.
5. An apparatus for carrying out the method as claimed in any of the preceding claims, characterized in that it comprises a feed chamber (2), having upper section (11) divided by a partition wall (8) into two adjacent, substan¬ tially vertical flow channels (9, 10) and connected to a substantially vertical part of a drying pipe (3) which leads to a cyclone (4), and with the lower section (14) of said feed chamber encasing at least part of the feeding means (12, 13) disposed at the inlet or top end of the lime reburning kiln (5), a control baffle (15) disposed at an upper part of the partition wall, a feed screw (1) or equivalent feeding means for dosing lime mud into the feed chamber from adjacent flow channels ( ), and means (16, 17) for introducing the dried lime mud which has been separated in the cyclone (4) into the lower section of the feed chamber.
6. An apparatus as claimed in claim 5, characterized in that the feeding means (12, 13) are comprised of vanes (13) having scoop means or shovel-formed extensions (12) and being attached to the inlet or top end of the lime reburning kiln, which vanes, when rotating, transfer the lime mud into the lime reburning kiln.
PCT/FI1990/000172 1989-07-03 1990-06-28 Feeding system for a lime reburning kiln Ceased WO1991000251A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP90909734A EP0480960B1 (en) 1989-07-03 1990-06-28 Feeding system for a lime reburning kiln
DE69017449T DE69017449T2 (en) 1989-07-03 1990-06-28 FEEDING SYSTEM FOR LIME RECALCINATION OVENS.
DE1990909734 DE480960T1 (en) 1989-07-03 1990-06-28 FEEDING SYSTEM FOR LIME RECALCINATION OVENS.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI893224 1989-07-03
FI893224A FI87245C (en) 1989-07-03 1989-07-03 INMATNINGSSYSTEM FOER MESAUGN

Publications (1)

Publication Number Publication Date
WO1991000251A1 true WO1991000251A1 (en) 1991-01-10

Family

ID=8528703

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/FI1990/000172 Ceased WO1991000251A1 (en) 1989-07-03 1990-06-28 Feeding system for a lime reburning kiln

Country Status (9)

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EP (1) EP0480960B1 (en)
JP (1) JP2553771B2 (en)
AT (1) ATE119140T1 (en)
CA (1) CA2063390C (en)
DE (1) DE69017449T2 (en)
ES (1) ES2071100T3 (en)
FI (1) FI87245C (en)
PT (1) PT94572B (en)
WO (1) WO1991000251A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006104775A3 (en) * 2005-03-29 2006-12-21 Kadant Black Clawson Inc Method and apparatus for pneumatic drying of lime mud

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104829146B (en) * 2015-03-26 2017-03-01 中国中轻国际工程有限公司 A kind of white mud lime kiln feeding method and its drawing-in device

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2796249A (en) * 1955-04-05 1957-06-18 Western Precipitation Corp Apparatus for heating finely divided solid material
FR1238562A (en) * 1958-10-14 1960-08-12 Furnace with rotating combustion chamber
SE184846C1 (en) * 1963-01-01
US3603569A (en) * 1969-12-29 1971-09-07 Kaiser Aluminum & Chemical Kiln preheat and drying section
GB1451057A (en) * 1973-11-29 1976-09-29 Ass Portland Cement Atomised kiln feed
DE3425099A1 (en) * 1984-07-07 1986-02-06 Klöckner-Humboldt-Deutz AG, 5000 Köln Installation for the treatment of finely grained material, especially cement raw meal
EP0369650A2 (en) * 1988-11-17 1990-05-23 F.L. Smidth & Co. A/S Method and apparatus for the treatment of calcium carbonate slurry as residue from the manufacture of paper

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2483447A1 (en) * 1980-06-03 1981-12-04 Ugine Kuhlmann COMPOSITION AND METHOD FOR PROTECTING MATERIALS AGAINST SOIL

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE184846C1 (en) * 1963-01-01
US2796249A (en) * 1955-04-05 1957-06-18 Western Precipitation Corp Apparatus for heating finely divided solid material
FR1238562A (en) * 1958-10-14 1960-08-12 Furnace with rotating combustion chamber
US3603569A (en) * 1969-12-29 1971-09-07 Kaiser Aluminum & Chemical Kiln preheat and drying section
GB1451057A (en) * 1973-11-29 1976-09-29 Ass Portland Cement Atomised kiln feed
DE3425099A1 (en) * 1984-07-07 1986-02-06 Klöckner-Humboldt-Deutz AG, 5000 Köln Installation for the treatment of finely grained material, especially cement raw meal
EP0369650A2 (en) * 1988-11-17 1990-05-23 F.L. Smidth & Co. A/S Method and apparatus for the treatment of calcium carbonate slurry as residue from the manufacture of paper

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006104775A3 (en) * 2005-03-29 2006-12-21 Kadant Black Clawson Inc Method and apparatus for pneumatic drying of lime mud

Also Published As

Publication number Publication date
PT94572B (en) 1997-05-28
DE69017449T2 (en) 1995-08-10
FI893224L (en) 1991-01-04
FI893224A0 (en) 1989-07-03
FI87245C (en) 1992-12-10
FI87245B (en) 1992-08-31
CA2063390C (en) 1995-08-08
ES2071100T3 (en) 1995-06-16
EP0480960B1 (en) 1995-03-01
JPH04504163A (en) 1992-07-23
JP2553771B2 (en) 1996-11-13
PT94572A (en) 1992-06-30
DE69017449D1 (en) 1995-04-06
CA2063390A1 (en) 1991-01-04
ATE119140T1 (en) 1995-03-15
EP0480960A1 (en) 1992-04-22

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