CN202705042U - Tank type carbon calcining furnace - Google Patents
Tank type carbon calcining furnace Download PDFInfo
- Publication number
- CN202705042U CN202705042U CN2012203820418U CN201220382041U CN202705042U CN 202705042 U CN202705042 U CN 202705042U CN 2012203820418 U CN2012203820418 U CN 2012203820418U CN 201220382041 U CN201220382041 U CN 201220382041U CN 202705042 U CN202705042 U CN 202705042U
- Authority
- CN
- China
- Prior art keywords
- calcining
- furnace
- tank
- discharge
- combustion chamber
- 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.)
- Expired - Fee Related
Links
- 238000001354 calcination Methods 0.000 title claims abstract description 50
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 12
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 12
- 238000002485 combustion reaction Methods 0.000 claims abstract description 32
- 238000010438 heat treatment Methods 0.000 claims abstract description 12
- 239000011229 interlayer Substances 0.000 claims abstract description 8
- 239000010410 layer Substances 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 claims description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound 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O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 7
- 239000003345 natural gas Substances 0.000 claims description 7
- 239000011449 brick Substances 0.000 claims description 6
- 239000002918 waste heat Substances 0.000 claims description 5
- 239000000377 silicon dioxide Substances 0.000 claims description 4
- 239000003517 fume Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 3
- 241000005139 Lycium andersonii Species 0.000 abstract description 3
- 239000000498 cooling water Substances 0.000 abstract 2
- 230000002457 bidirectional Effects 0.000 abstract 1
- 239000000779 smoke Substances 0.000 abstract 1
- 239000000470 constituent Substances 0.000 description 6
- 239000011329 calcined coke Substances 0.000 description 3
- 239000003575 carbonaceous material Substances 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 206010022000 Influenza Diseases 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000003139 buffering Effects 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Abstract
The utility model discloses a tank type carbon calcining furnace, belonging to calcining furnaces for producing carbon, wherein every four calcining tanks and a furnace wall with a heating flame path at two sides of the tank body form a combustion chamber; an expansion joint and a collection smoke flue are between every two combustion chambers; the furnace wall with the heating flame path is provided with 8-10 layers of flame paths; the flame paths are communicated with a pre-heated air path; a calcining tank body is connected to a discharge tank; an interlayer cooling water jacket is arranged on the periphery of the discharge tank; the tank type carbon calcining furnace is characterized in that the whole calcining furnace is composed of 18 combustion chambers arranged in a row and 72 calcining tanks; a large furnace-protecting cutter frame is arranged outside the front wall of the calcining furnace; a furnace-protecting frame is arranged outside the rear wall of the calcining furnace; the bottoms of the combustion chambers are supported by support columns at the bottom of the calcining furnace; a charging hole is arranged on the top of the calcining tank body; the bottom of the calcining tank body is connected to the discharge tank; the interlayer cooling water jacket is arranged on the periphery of the discharge tank; a discharge machine is arranged at the lower end of the discharge tank; and a small storage bin is between the discharge machine and a discharge valve. According to the utility model, bidirectional utilization of volatile matters and full-automatic closed type continuous discharge are realized; and the tank type carbon calcining furnace has good economic benefits and environmental benefits.
Description
Technical field
The utility model belongs to a kind of calcining kiln, particularly the can-type calcine furnace of charcoal element production usefulness.
Background technology
Can-type calcine furnace is that the charcoal element is produced calciner commonly used, material secluding air in tank body carries out indirect heating and calcines the volatile component of removing in the carbon material, this calcining furnace can take full advantage of a large amount of volatile matters that carbon materials overflows in calcining the combustion heat reduces energy consumption, the shortcomings such as but existing can-type calcine furnace existence group number is few, air supply is not enough cause that UTILIZATION OF VESIDUAL HEAT IN is insufficient, the deficiency such as calcination efficiency and quality are low.
The utility model content
In order to overcome the low deficiency of the insufficient thermo-efficiency of existing calcining furnace UTILIZATION OF VESIDUAL HEAT IN, the utility model provides a kind of tank type carbon calciner.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of tank type carbon calciner, per four calcining tanks consist of a combustion chamber with the furnace wall of the band heating quirk that is positioned at the tank body both sides, the expansion joint is arranged between each combustion chamber and compile flue, there are at least 8 layers of quirk the furnace wall of band heating quirk, quirk communicates with the preheated air road, the calcining tank body is connecting blow-down drum, blow-down drum is with the interlayer watercooling jacket outward, it is characterized in that: totally 72 the calcining tanks in 18 combustion chambers that whole calcining furnace is arranged by yi word pattern form, the calcining furnace front wall is provided with the furnace retaining carriage outward, rear wall is provided with the furnace retaining frame outward, and the bottom, combustion chamber is supported by bottom prop, and calcining tank body top is provided with charging opening, the bottom is connecting blow-down drum, blow-down drum is with the interlayer watercooling jacket outward, and material discharging machine is equipped with in the blow-down drum lower end, is small feed bin between material discharging machine and the blow-off valve.
Be provided with the combustion of natural gas mouth that communicates with natural gas line in the front wall of described combustion chamber, the furnace wall of band heating quirk is for building the fire-resistant silica brick wall that quirk is arranged, be provided with the volatile matter passage with the bottom, combustion chamber within the walls behind the combustion chamber, the horizontal volatile matter passage that is positioned at combustion chamber bottom links to each other with the waste heat boiler flue through compiling flue, and communicates with external flue towards chimney in the flue vertical shaft that the gas fume of combustion chamber outlet is connected.
The long 2180mm of described calcining tank, wide 360mm, high 5576mm.
The disclosed can-type calcine furnace of the utility model is increased to 18 group of 72 tank with 7 group of 28 tank of traditional calcining furnace, increases to 8 layers of quirk around the calcining tank, and the tank body size changes long 2180mm into, wide 360mm, high 5576mm; The calcining furnace discharge system adopts the Full automatic closed continuous discharge device of counterflow; The direct discharge of the blow-down drum of prior art is improved to the blow-down drum mouth continuous pulp discharge machine is installed, the material of discharge is introduced into and is sent to next procedure by the blow-off valve discharge by feed belt again after small feed bin is detained buffering.Realized the two-way utilization of fugitive constituent in the can-type calcine furnace, except satisfying calcining furnace burning itself, unnecessary fugitive constituent enters waste heat boiler by designated lane, is used for generating; Because above improvement, the utility model has been obtained good effect:
1. increased output, discharge by 90 kilograms/tank/hour be increased to 150-160 kilogram/tank/hour.
2. the saving energy when normally producing, utilizes the fugitive constituent burning of raw material, fully without postcombustion.
3. unnecessary fugitive constituent is used for cogeneration, has both reduced the carbon emission amount, has effectively protected environment, meets again the Development patterns of recycling economy, for enterprise has created benefit.
4. Full automatic closed continuous discharge device of counterflow, level of automation is high, has reduced workman's labour intensity; Can make product uniform motion in calcining furnace, fugitive constituent evenly overflows, thereby so that the temperature-stable in the burner hearth guarantees constant product quality, homogeneous.According to detecting the calcined coke true density at 2.08g/cm
3More than, powder remains on below the 410 μ Ω .m than resistance.
In addition, because product is kept in motion, solved the problem of burner hearth coking, prevent scaffold and blow out phenomenon, and closed discharge has prevented effectively that then dust from overflowing, and has both reduced waste, has greatly improved again workman's work situation.
5. calcined coke cushions through small feed bin, can guarantee that calcined coke fully lowers the temperature, and effectively stops extraneous air to enter the calcining tank body, prevents that raw material from secondary oxidation and tank body occurring and blowing out phenomenon.
Description of drawings
Fig. 1 is the structure sectional view at the utility model tank body position,
Fig. 2 is the structure sectional view at the utility model flue wall position,
Among the figure, 1. charging opening is 2. calcined tank, 3. quirk, 4. compile flue, 5. fire-resistant silica brick wall, 6. flue vertical shaft, 7. external flue, 8. waste heat boiler, 9. water jacket, 10. material discharging machine, 11. small feed bins, 12. blow-off valve, 13. rotary conveyors, top, 14. combustion chambers, 15. furnace retaining carriage 16. furnace retaining framves, 17. bottom props, 18. front walls, 19. natural gas line, 20. common brick walls, 21. fugitive constituent passages.
Embodiment
Embodiment of the present utility model is, as shown in the figure:
Embodiment 1, a kind of tank type carbon calciner, per four calcining tanks 2 consist of a combustion chamber with the furnace wall of the band heating quirk that is positioned at the tank body both sides, the expansion joint is arranged between each combustion chamber and compile flue 4, there is 8-10 layer quirk 3 furnace wall of band heating quirk, quirk communicates with the preheated air road, the calcining tank body is connecting blow-down drum, blow-down drum is with interlayer watercooling jacket 9 outward, it is characterized in that: totally 72 the calcining tanks in 18 combustion chambers that whole calcining furnace is arranged by yi word pattern form, the long 2180mm of calcining tank, wide 360mm, high 5576mm.The calcining furnace front wall is provided with furnace retaining carriage 15 outward, rear wall is provided with furnace retaining frame 16 outward, the bottom, combustion chamber is supported by bottom prop 17, calcining tank body top is provided with charging opening 1, the bottom is connecting blow-down drum, blow-down drum is with interlayer watercooling jacket 9 outward, and material discharging machine 10 is equipped with in the blow-down drum lower end, is small feed bin 11 between material discharging machine and the blow-off valve 12.
Be provided with the combustion of natural gas mouth that communicates with natural gas line 19 in the described calcining furnace front wall 18, the furnace wall of band heating quirk is for building the fire-resistant silica brick wall 5 that quirk is arranged, the outer wall of calcining furnace is the common brick wall, be provided with volatile matter passage 21 with the bottom, combustion chamber within the walls behind the calcining furnace, the horizontal volatile matter passage that is positioned at the bottom, combustion chamber links to each other with waste heat boiler 8 flues through compiling flue, and the flue vertical shaft 6 that is connected with the gas fume of combustion chamber outlet communicates with the external flue 7 that leads to chimney.
Claims (2)
1. tank type carbon calciner, per four calcining tanks consist of a combustion chamber with the furnace wall of the band heating quirk that is positioned at the tank body both sides, the expansion joint is arranged between each combustion chamber and compile flue, there is 8-10 layer quirk the furnace wall of band heating quirk, quirk communicates with the preheated air road, the calcining tank body is connecting blow-down drum, blow-down drum is with the interlayer watercooling jacket outward, it is characterized in that: totally 72 the calcining tanks in 18 combustion chambers that whole calcining furnace is arranged by yi word pattern form, the calcining furnace front wall is provided with the furnace retaining carriage outward, rear wall is provided with the furnace retaining frame outward, and the bottom, combustion chamber is supported by bottom prop, and calcining tank body top is provided with charging opening, the bottom is connecting blow-down drum, blow-down drum is with the interlayer watercooling jacket outward, and material discharging machine is equipped with in the blow-down drum lower end, is small feed bin between material discharging machine and the blow-off valve.
2. tank type carbon calciner according to claim 1, it is characterized in that: be provided with the combustion of natural gas mouth that communicates with natural gas line in the described calcining furnace front wall, the furnace wall of band heating quirk is for building the fire-resistant silica brick wall that quirk is arranged, be provided with the volatile matter passage with the bottom, combustion chamber within the walls behind the calcining furnace, the horizontal volatile matter passage that is positioned at the bottom, combustion chamber links to each other with the waste heat boiler flue through compiling flue, and the flue vertical shaft that is connected with the gas fume of combustion chamber outlet communicates with the external flue that leads to chimney.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012203820418U CN202705042U (en) | 2012-08-02 | 2012-08-02 | Tank type carbon calcining furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012203820418U CN202705042U (en) | 2012-08-02 | 2012-08-02 | Tank type carbon calcining furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202705042U true CN202705042U (en) | 2013-01-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012203820418U Expired - Fee Related CN202705042U (en) | 2012-08-02 | 2012-08-02 | Tank type carbon calcining furnace |
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| Country | Link |
|---|---|
| CN (1) | CN202705042U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102745671A (en) * | 2012-08-02 | 2012-10-24 | 济南澳海炭素有限公司 | Pot-type carbon calciner |
| CN104132542A (en) * | 2014-05-29 | 2014-11-05 | 山东宇佳新材料有限公司 | Petroleum coke calcinator |
-
2012
- 2012-08-02 CN CN2012203820418U patent/CN202705042U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102745671A (en) * | 2012-08-02 | 2012-10-24 | 济南澳海炭素有限公司 | Pot-type carbon calciner |
| CN102745671B (en) * | 2012-08-02 | 2014-05-14 | 济南澳海炭素有限公司 | Pot-type carbon calciner |
| CN104132542A (en) * | 2014-05-29 | 2014-11-05 | 山东宇佳新材料有限公司 | Petroleum coke calcinator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130130 Termination date: 20200802 |