CN101880896B - Method for drying carbon anode roasting furnace - Google Patents
Method for drying carbon anode roasting furnace Download PDFInfo
- Publication number
- CN101880896B CN101880896B CN2010102020938A CN201010202093A CN101880896B CN 101880896 B CN101880896 B CN 101880896B CN 2010102020938 A CN2010102020938 A CN 2010102020938A CN 201010202093 A CN201010202093 A CN 201010202093A CN 101880896 B CN101880896 B CN 101880896B
- Authority
- CN
- China
- Prior art keywords
- furnace
- hours
- drying
- furnace chamber
- roasting
- 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.)
- Active
Links
Landscapes
- Furnace Details (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a method for drying an annular open roasting furnace, which is characterized in that: (1), a 240-hour heating curve and a 240-hour cooling curve are adopted in a roasting process; and (2), combustion racks are placed in observation holes 2 and 4 of a No.2 furnace chamber and a No.22 furnace chamber, smoke exhaust racks are placed in a No.4 furnace chamber and a No.23 furnace chamber, ignition is started from the observation holes 2 in the No.2 furnace chamber and the No.22 furnace chamber, a fourth furnace chamber is added by moving the smoke exhaust racks after three flame travel periods, ignition in the observation hole 4 is determined according to the following condition of the temperature rise to the temperature curve of the drying furnace, and after each flame travel period, the smoke exhaust rack is continuously moved and a combustion rack is added till each system has three combustion racks and forms 8-chamber operation, wherein a system travel period is 30 hours. In the method for drying the carbon anode roasting furnace, the carbon anode roasting furnace is a 38-chamber annular open roasting furnace, the technical parameters are optimized effectively, the furnace drying time is shortened, the process for converting a roasting drying furnace curve into a normal roasting production curve after the furnace drying is finished is simplified, and the furnace drying cost is reduced.
Description
Technical field
A kind of method of drying carbon anode roasting furnace relates to a kind of method of aluminum electrolysis carbon anode stoving oven baker.
Background technology
Use the carbon anode production process at aluminium, stoving oven is a very important equipment.The stoving oven baker all adopts 360 hours drying out curve of six Room operation at present, and moving period of system is 60 hours, and baker has been obtained reasonable effect after finishing.But also there is certain problem in this furnace drying method, and promptly furnace drying time is long, and it is cumbersome to convert normal baked for producing curve into from the roasting drying out curve after the baker end, and ton anode Sweet natural gas unit cost is high.
Summary of the invention
In view of this, the purpose of this invention is to provide a kind of furnace drying method of annular open roasting furnace, it is long that this method can solve furnace drying time, and baker end back converts the cumbersome problem of normal baked for producing curve into from the roasting drying out curve.
Above-mentioned purpose realizes through following proposal:
A kind of method of drying carbon anode roasting furnace is characterized in that its carbon anode roasting furnace is Room 38 annular open roasting furnaces;
(1) adopt 240 hours heating curves to be:
Fs is the temperature rise period, and 8 hours TRTs, temperature range is 60-120 ℃;
Subordinate phase is a holding-zone, and soaking time is 28 hours;
Phase III is the temperature rise period, and the TRT is 32 hours, and temperature range is 120-300 ℃;
Stage is a holding-zone, and soaking time is 23 hours;
Five-stage is the temperature rise period, and the TRT is 46 hours, and temperature range is 300-600 ℃;
The 6th stage was the temperature rise period, and the TRT is 27 hours, and temperature range is 600-800 ℃;
The 7th stage was the temperature rise period, and the TRT is 36 hours, and temperature range is 800-1150 ℃;
The 8th stage was a holding-zone, and soaking time is 40 hours;
(2) adopt 240 hours cooling curves to be:
Fs lowers the temperature naturally, and the time length is 210 hours, and temperature range is 1150-600 ℃;
Subordinate phase is for forcing cooling, and the time length is 30 hours, and temperature range is 600 a ℃-tapping temperature;
(3) burning rack is put 2# and 22# furnace chamber 2,4 vision slits, and the smoke evacuation frame is placed on 4# and 23# furnace chamber, begins igniting from 2# and 22# furnace chamber 2 vision slits; Through all after dates of 3 flame movement, moving the smoke evacuation frame increases the 4th furnace chamber, confirms the igniting of 4 vision slits if intensification does not catch up with heating curve; Every through a flame movement cycle, continue to move the smoke evacuation frame, increase burning rack; Until each system fills it up with 3 burning racks, form Room 8 running, moving period of system is 30 hours.
The method of a kind of drying carbon anode roasting furnace of the present invention; Its carbon anode roasting furnace is Room 38 annular open roasting furnaces; Optimized processing parameter effectively; Furnace drying time is short, has simplified to convert normal baked for producing curve process into from the roasting drying out curve after baker finishes, and has reduced the baker cost.
Embodiment
A kind of method of drying carbon anode roasting furnace, roasting furnace chamber are Room 38 annular open roasting furnaces, are fuel with the Sweet natural gas, and baker adopts two flame systems.
The concrete shove charge of stoving oven baker requires: 1# and 21# furnace chamber dress are given birth to piece sealing furnace chamber, and the useless piece of giving birth to of 2# and 22# furnace chamber dress is adorned qualified living piece later on from 3# and 23# furnace chamber.Furnace chamber assurance one goes out, a dress, is equipped with.Burning rack is put 2# and 22# furnace chamber 2,4 vision slits, and the smoke evacuation frame is placed on 4# and 23# furnace chamber.Begin igniting from 2# and 22# furnace chamber 2 vision slits, through 3 flame movement week after date, moving the smoke evacuation frame increases the 4th furnace chamber, whether can catch up with oven drying temperature curve the 2nd row's nozzle of confirming whether to light a fire according to heating up.Every through a flame movement cycle, continue to move the smoke evacuation frame, increase burning rack, until each system fills it up with 3 burning racks, form Room 8 running.After 8 flame movement cycle heating, first heated 2# and 21# furnace chamber begin to get into colling stages.Colling stages is divided into naturally cooling and forces cooling.The flame movement direction is a CW, from Room 1 to Room 38.
The stoving oven baker adopts and rose curve, 30 hours moving periods in 240 hours.Cooling curve 240 hours is as shown in table 1.
240 hours drying out curve of table 1
The cooling curve of baker shown in the table 2.After 1150 ℃ of insulation end of top temperature, naturally cooling 180 hours begins to force cooling 60 hours then, guarantees and can come out of the stove.
Table 2 baker cooling curve
Remarks: take off the cooling of quirk lid nature from C5 the 3rd hole, C8 forces cooling, and C9 comes out of the stove, and (C5 wherein, C8, C9 represent respectively and cool off the 5th furnace chamber of furnace chamber, the 8th furnace chamber, the 9th furnace chamber.)。
The control of baker process requires:
The scene can be implemented elastic curve according to practical situation and heated up in temperature-rise period, and the quirk top temperature is 1150 ℃ between drying-out period.The quirk cold zone temperature difference is different to be ± 20 ℃, and the quirk high-temperature zone temperature difference is different to be ± 5 ℃.Also must be noted that following operation rules and regulations:
For being ambient conditions and when causing intensification can't catch up with the baker heating curve, must guarantee the balance of each fire path temperature really.
Cause temperature to descend for mishap, when heating up again, must implement elastic curve according to practical situation and carry out the curve adjustment.
Total negative pressure is divided the negative pressure using priciple with each quirk: the benchmark negative pressure, from high to low, the reddish tone balance.
The fuel quantity at each furnace chamber upper reaches of strict control does not allow quirk that the dazzling phenomenon of turning white is arranged.
Low thermophase and middle thermophase (in 800 ℃) adopt the manual regulation gas discharge to control temperature-rise period, are main with control zero-pressure frame negative pressure.
Hot stage adopts the automatic gas discharge of regulating to control temperature-rise period, is main with control smoke evacuation frame negative pressure.
Claims (1)
1. the method for a drying carbon anode roasting furnace is characterized in that its carbon anode roasting furnace is Room 38 annular open roasting furnaces;
(1) adopt 240 hours heating curves to be:
Fs is the temperature rise period, and 8 hours TRTs, temperature range is 60-120 ℃;
Subordinate phase is a holding-zone, and soaking time is 28 hours;
Phase III is the temperature rise period, and the TRT is 32 hours, and temperature range is 120-300 ℃;
Stage is a holding-zone, and soaking time is 23 hours;
Five-stage is the temperature rise period, and the TRT is 46 hours, and temperature range is 300-600 ℃;
The 6th stage was the temperature rise period, and the TRT is 27 hours, and temperature range is 600-800 ℃;
The 7th stage was the temperature rise period, and the TRT is 36 hours, and temperature range is 800-1150 ℃;
The 8th stage was a holding-zone, and soaking time is 40 hours;
(2) adopt 240 hours cooling curves to be:
Fs lowers the temperature naturally, and the time length is 210 hours, and temperature range is 1150-600 ℃;
Subordinate phase is for forcing cooling, and the time length is 30 hours, and temperature range is 600 a ℃-tapping temperature;
(3) burning rack is put 2# and 22# furnace chamber 2,4 vision slits, and the smoke evacuation frame is placed on 4# and 23# furnace chamber, begins igniting from 2# and 22# furnace chamber 2 vision slits; Through all after dates of 3 flame movement, moving the smoke evacuation frame increases the 4th furnace chamber, confirms the igniting of 4 vision slits if intensification does not catch up with heating curve; Every through a flame movement cycle, continue to move the smoke evacuation frame, increase burning rack; Until each system fills it up with 3 burning racks, form Room 8 running, moving period of system is 30 hours.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010102020938A CN101880896B (en) | 2010-06-10 | 2010-06-10 | Method for drying carbon anode roasting furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010102020938A CN101880896B (en) | 2010-06-10 | 2010-06-10 | Method for drying carbon anode roasting furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101880896A CN101880896A (en) | 2010-11-10 |
CN101880896B true CN101880896B (en) | 2012-08-29 |
Family
ID=43053031
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2010102020938A Active CN101880896B (en) | 2010-06-10 | 2010-06-10 | Method for drying carbon anode roasting furnace |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101880896B (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102564109B (en) * | 2010-12-08 | 2014-02-05 | 沈阳铝镁设计研究院有限公司 | Irregular furnace moving operation and warming method for turning furnace chambers of roasting furnace |
CN103123224B (en) * | 2011-11-21 | 2014-12-17 | 沈阳铝镁设计研究院有限公司 | Open-type roasting furnace heating curve and furnace moving operational method |
CN102494538B (en) * | 2011-11-24 | 2013-07-17 | 中国铝业股份有限公司 | Process for overhauling of calcining furnace and starting of baking oven |
CN104879774B (en) * | 2015-04-21 | 2017-05-31 | 泉州格罗特机电设备有限公司 | The furnace drying method of tilting furnace |
CN111662078B (en) * | 2020-06-01 | 2022-07-08 | 国家电投集团黄河上游水电开发有限责任公司 | High-temperature flue gate plate sintering method |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101255564A (en) * | 2007-12-17 | 2008-09-03 | 中国铝业股份有限公司 | Drying method for ring-form calcining furnace |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5855582A (en) * | 1981-09-29 | 1983-04-01 | Sumitomo Alum Smelt Co Ltd | Hard pitch for aluminum electrolytic electrode |
-
2010
- 2010-06-10 CN CN2010102020938A patent/CN101880896B/en active Active
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101255564A (en) * | 2007-12-17 | 2008-09-03 | 中国铝业股份有限公司 | Drying method for ring-form calcining furnace |
Non-Patent Citations (3)
Title |
---|
JP昭58-55582A 1983.04.01 |
刘君.改进焙烧炉烘炉工艺 降低燃料消耗.《有色冶金节能》.2003,第20卷(第1期),43-45. * |
刘君.焙烧炉烘炉新工艺.《轻金属》.2003,(第6期),45-47. * |
Also Published As
Publication number | Publication date |
---|---|
CN101880896A (en) | 2010-11-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101880896B (en) | Method for drying carbon anode roasting furnace | |
CN105222581B (en) | Method adopting walking beam type heating furnace for heating low temperature billets | |
CN103466617B (en) | A kind of preparation method of High-temperature crystallite bamboo charcoal | |
CN202581322U (en) | Ultrahigh-energy high-turndown ratio combustor | |
CN103123224B (en) | Open-type roasting furnace heating curve and furnace moving operational method | |
CN107033927B (en) | A kind of coke oven combustion chamber flue structure of segmentally heating | |
CN201711490U (en) | Small-sized three-stage push rod continuous forging heating furnace | |
CN206514685U (en) | A kind of electrically mixing kiln | |
CN101353579A (en) | 7.63m coke oven negative pressure in-furnace furnace drying method | |
CN202216560U (en) | Multi-chain type crucible furnace | |
CN104374192B (en) | Multifunctional ceramic firing kiln and manufacturing method of porcelain thereof | |
CN102344133A (en) | Method for preparing fine particles high-density graphite product and open type circular calcinator | |
CN103206857B (en) | Method for operating environment-friendly energy-saving de-waxing kiln | |
CN101314471B (en) | Ring type roasting furnace temperature elevation method | |
CN208382878U (en) | One kind producing heat-resisting closed kiln for ceramic high temperature molding | |
CN103884026B (en) | Underground flue warming stove | |
CN104776434A (en) | Nozzle for blast furnace gas oven | |
CN204554816U (en) | Blast furnace gas baker burner | |
CN205137891U (en) | It generates stove to keep off flame structure flue gas with adjustable | |
CN207486852U (en) | A kind of side filling biomass stove of gravity-flow ventilation | |
CN101314859A (en) | Setting method for temperature elevation curve of pre-baked anode in torrefaction heating period | |
CN203501786U (en) | Firebrick for open ring-type roaster | |
CN203914605U (en) | Fire-resistant charcoal brazier | |
CN208282617U (en) | A kind of gas kiln for firing ceramics | |
CN204084473U (en) | A kind of energy-saving stove cast iron burner hearth |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |