CN201050937Y - Ceramic tunnel kiln preheating belt modified structure - Google Patents
Ceramic tunnel kiln preheating belt modified structure Download PDFInfo
- Publication number
- CN201050937Y CN201050937Y CNU2007201534459U CN200720153445U CN201050937Y CN 201050937 Y CN201050937 Y CN 201050937Y CN U2007201534459 U CNU2007201534459 U CN U2007201534459U CN 200720153445 U CN200720153445 U CN 200720153445U CN 201050937 Y CN201050937 Y CN 201050937Y
- Authority
- CN
- China
- Prior art keywords
- kiln
- temperature
- preheating zone
- preheating belt
- tunnel 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.)
- Expired - Fee Related
Links
- 239000000919 ceramic Substances 0.000 title claims abstract description 14
- 239000007921 spray Substances 0.000 claims description 14
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 9
- 239000003546 flue gas Substances 0.000 claims description 9
- 239000002918 waste heat Substances 0.000 claims description 6
- 239000000779 smoke Substances 0.000 claims description 3
- 238000003756 stirring Methods 0.000 abstract description 4
- 238000002347 injection Methods 0.000 abstract description 3
- 239000007924 injection Substances 0.000 abstract description 3
- 230000001105 regulatory effect Effects 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 230000031877 prophase Effects 0.000 abstract 1
- 238000010304 firing Methods 0.000 description 4
- 241000264877 Hippospongia communis Species 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000013517 stratification Methods 0.000 description 2
- 208000035126 Facies Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
Images
Landscapes
- Furnace Details (AREA)
Abstract
The utility model relates to an improved structure of a ceramic tunnel kiln preheating belt, which has the design keys that a group of stirring air curtains are arranged on kiln crowns whose interval is 2 meters in a first temperature zone 80-350 DEG C of the tunnel kiln preheating belt, simultaneously, and four sets of hot blast injection pipes 9 are crossly arranged on the upper and the lower of the segment of the kiln. Three sets of high speed regulating temperature nozzles 6 are crossly arranged on the lower portion of a kiln wall whose interval is 2 meter in a second temperature zone of 350-650 DEG C of the tunnel kiln preheating belt, and the hot blast injection pipes 9 whose number is corresponding are correspondingly arranged on a same section which is face to the upper portion of the square kiln. The improved structure is capable of leading the temperature difference of the upper and the lower of the tunnel kiln preheating belt to reduce to 30-50 DEG C, because the upper and lower temperature difference in the kiln is reduced, productions in the kiln are equably heated. The utility model is particularly suitable to be sintered from honeycomb ceramics and ceramic products which have high requirements for the prophase temperature uniformity of the preheating belt.
Description
Technical field
The utility model belongs to the ceramic kiln technical field, is specifically related to the improvement structure of a kind of ceramic roller kiln preheating zone, is mainly used in ceramic honey comb and other preheating zone ceramic product that temperature homogeneity is had relatively high expectations early stage is burnt till.
Background technology
Tunnel cave is the horizontal flame formula kiln that a kind of air-flow is bottom horizontal flow sheet.Though advantage is a lot, the problem that its preheating zone ubiquity is that the cross section upper and lower temperature difference is big, and the inhomogeneities of section temperature causes goods stress bigger thus, causes the goods cracking easily, and has prolonged firing time, has reduced furnace output.Producing the interior big main cause of upper and lower temperature difference of kiln is stratification of hot gas, because of this band is in negative-pressure operation, from the imprecision of kiln, as the bent envelope of kiln inlet, kiln car wadding and kiln wall, a large amount of cold wind that bleed such as the joint between the kiln car, cold wind density is big, sinks to the kiln bottom.Because kiln has certain altitude, under the effect of how much pressure heads, force the little hot flue gas of most of density upwards to flow, cause the air-flow layering, improved upper temp, reduced temperature of lower.Add the heat of kiln car absorption bottom flue gas, temperature of lower is reduced, aggravated the upper and lower temperature difference of preheating zone more.
Domestic common way at this band is at kiln hood the sealing air curtain to be set at present, with high-pressure blast one barrier of aperture high speed ejection formation from kiln hood air curtain airduct, stop extraneous cold wind to bleed in the kiln, simultaneously on Yao Qiang top, preheating zone many cold wind injection apparatus are set, high velocity air forces flue gas to flow downward.Above-mentioned way has been dwindled the temperature difference in the kiln to a certain extent, but, the cold wind that only depends on top to spray into dwindles upper and lower temperature difference because reducing kiln internal upper part temperature, and can not organize effective hot-air flow circulation, especially do not establish high velocity temperature adjusting burner in the Yao Qiang bottom, make temperature of lower low, the temperature difference in the kiln is more than 150-200 ℃, do not satisfy ceramic honey comb and other ceramic product that temperature homogeneity is had relatively high expectations burns till.
Summary of the invention
The utility model purpose is big at the existing ceramic roller kiln preheating zone temperature difference, and the technical measures that overcome the temperature difference are not enough, and propose a kind ofly can effectively reduce the improvement structure that efficient is burnt till in the tunnel cave preheating zone temperature difference and raising.
The technical scheme that the utility model adopted is: in the first humidity province 80-350 ℃ scope of tunnel cave preheating zone, arranged that every 2 meters kiln top is stirred an air curtain, the waste heat wind and the reverse high speed of flue gas that come from salband spray in the kiln, simultaneously in the kiln of this section up and down interlaced arrangement 4 cover spray hot wind pipes; In the second humidity province 350-650 ℃ scope of tunnel cave preheating zone, every 2 meters Yao Qiang bottom interlaced arrangement 3 cover high speed temperature adjustment nozzles, the spray hot wind pipe on same cross section over against the corresponding layout respective amount in square kiln top.
In first humidity province, owing to stir the air curtain stirring or stop flue gas in the kiln, force it to flow downward, to overcome stratification of hot gas, the waste heat wind that comes from salband sprays at a high speed in the kiln through the spray hot wind pipe, causes the air-flow even heating product of agitation cycle tempestuously; In second humidity province, the auxiliary air amount of high speed temperature adjustment nozzle by mixing, can in 80-1800 ℃ temperature range, regulate arbitrarily, reach the temperature requirement of desired area, the high speed hot blast of the high speed flue gas of ejection and playpipe ejection, on the kiln lateral cross section, produce the strong agitation circulation, make in the kiln about, internal and external temperature is very even.This improvement structure can make the upper and lower temperature difference of tunnel cave preheating zone narrow down to 30-50 ℃ owing to reduced upper and lower temperature difference in the kiln, make that product is heated evenly in the kiln, and accelerated go-cart speed, thereby improved product burn till quality and output.
Description of drawings
Fig. 1 is the kiln body vertical structure schematic diagram of the utility model first humidity province;
Fig. 2 is the kiln body vertical structure schematic diagram of the utility model second humidity province;
Fig. 3 is the kiln body section structural representation of the utility model first humidity province;
Fig. 4 is the kiln body section structural representation of the utility model second humidity province;
The specific embodiment
Concrete structure of the present utility model and content are described in detail as follows in conjunction with the accompanying drawings:
The utility model comprises firing chamber 1, kiln wall 2, kiln top 3, kiln car 4, playpipe 5, high speed temperature adjustment nozzle 6, exhaust smoke hole 7, waste heat airduct 8 etc., and its concrete embodiment is:
1, sends into first temperature province (80-350 ℃) by salband waste heat wind, spray hot wind is all adopted in this zone, and mix a certain amount of cold wind according to kiln temperature, spray in the kiln with the reverse high speed of flue gas by the playpipe 5 that is arranged on kiln top 3, form and stir air curtain, spray in the firing chamber 1 at a high speed in horizontal direction by Yao Qiang top and the bottom interlaced arrangement playpipe 9 simultaneously, to form the air-flow forced circulation.
2, send into second temperature province (350-650 ℃) by salband waste heat wind, take spray hot wind and the combining form of high combustion rate burner temperature adjustment wind facies in this zone, spray in the kiln by kiln top playpipe 5 and the reverse high speed of flue gas, be injected in horizontal direction in the firing chamber 1 by kiln wall 2 top playpipes 9, be provided with high velocity temperature adjusting burner 6 at kiln wall playpipe over against square bottom, the auxiliary air amount of high velocity temperature adjusting burner by mixing can be regulated temperature of lower arbitrarily, and causes air-flow acutely to circulate to dwindle the temperature difference in the kiln.On the kiln wall of first warm area and second warm area, be provided with exhaust smoke hole 7, air-flow is played regulating action.
Claims (2)
1. the improvement structure of a ceramic roller kiln preheating zone, it is characterized in that in the first humidity province 80-350 ℃ scope of tunnel cave preheating zone, arranged that every 2 meters kiln top is stirred an air curtain, the waste heat wind and the reverse high speed of flue gas that come from salband spray in the kiln, simultaneously in the kiln of this section up and down interlaced arrangement 4 cover spray hot wind pipes (9); In the second humidity province 350-650 ℃ scope of tunnel cave preheating zone, every 2 meters Yao Qiang bottom interlaced arrangement 3 the cover high speed temperature adjustment nozzles (6), the spray hot wind pipe (9) on same cross section over against the corresponding layout respective amount in square kiln top.
2. the improvement structure of ceramic roller kiln according to claim 1 preheating zone is characterized in that being provided with exhaust smoke hole (7) on the kiln wall of first warm area and second warm area.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201534459U CN201050937Y (en) | 2007-06-06 | 2007-06-06 | Ceramic tunnel kiln preheating belt modified structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201534459U CN201050937Y (en) | 2007-06-06 | 2007-06-06 | Ceramic tunnel kiln preheating belt modified structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201050937Y true CN201050937Y (en) | 2008-04-23 |
Family
ID=39337427
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201534459U Expired - Fee Related CN201050937Y (en) | 2007-06-06 | 2007-06-06 | Ceramic tunnel kiln preheating belt modified structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201050937Y (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102322684A (en) * | 2011-09-21 | 2012-01-18 | 广东中窑窑业股份有限公司 | Heating pipe for drying air hose |
| CN101629784B (en) * | 2008-07-15 | 2012-04-25 | 广东萨米特陶瓷有限公司 | Wide roller kiln for firing porcelain tile |
| CN101809399B (en) * | 2007-08-31 | 2012-10-03 | 康宁股份有限公司 | Method for firing ceramic honeycomb bodies in a kiln |
| CN103320564A (en) * | 2013-03-11 | 2013-09-25 | 王云龙 | Circular tunnel-type rotary hearth furnace and ironmaking method |
| CN103411421A (en) * | 2013-03-28 | 2013-11-27 | 济南大学 | Novel preheating belt for tunnel kiln |
| CN104011466A (en) * | 2011-12-27 | 2014-08-27 | 日本碍子株式会社 | Combustion apparatus, and heating furnace using same |
| CN107677120A (en) * | 2017-10-31 | 2018-02-09 | 广西南山瓷器有限公司 | Energy-saving environment-friendly ceramic kiln |
| CN111380357A (en) * | 2018-12-29 | 2020-07-07 | 洛阳利尔中晶光伏材料有限公司 | Tunnel kiln |
-
2007
- 2007-06-06 CN CNU2007201534459U patent/CN201050937Y/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101809399B (en) * | 2007-08-31 | 2012-10-03 | 康宁股份有限公司 | Method for firing ceramic honeycomb bodies in a kiln |
| CN101629784B (en) * | 2008-07-15 | 2012-04-25 | 广东萨米特陶瓷有限公司 | Wide roller kiln for firing porcelain tile |
| CN102322684A (en) * | 2011-09-21 | 2012-01-18 | 广东中窑窑业股份有限公司 | Heating pipe for drying air hose |
| CN104011466A (en) * | 2011-12-27 | 2014-08-27 | 日本碍子株式会社 | Combustion apparatus, and heating furnace using same |
| CN104011466B (en) * | 2011-12-27 | 2016-08-17 | 日本碍子株式会社 | Burner and use its heating furnace |
| CN103320564A (en) * | 2013-03-11 | 2013-09-25 | 王云龙 | Circular tunnel-type rotary hearth furnace and ironmaking method |
| CN103320564B (en) * | 2013-03-11 | 2015-07-29 | 王云龙 | A kind of Circular tunnel-type rotary hearth furnace and iron smelting method |
| CN103411421A (en) * | 2013-03-28 | 2013-11-27 | 济南大学 | Novel preheating belt for tunnel kiln |
| CN103411421B (en) * | 2013-03-28 | 2015-10-14 | 济南大学 | A kind of Novel tunnel furnace preheating zone |
| CN107677120A (en) * | 2017-10-31 | 2018-02-09 | 广西南山瓷器有限公司 | Energy-saving environment-friendly ceramic kiln |
| CN111380357A (en) * | 2018-12-29 | 2020-07-07 | 洛阳利尔中晶光伏材料有限公司 | Tunnel kiln |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201050937Y (en) | Ceramic tunnel kiln preheating belt modified structure | |
| CN106196056B (en) | The burner of smoke backflow indole energy low with the temperature control of Staged Premixed Combustion | |
| CN101863627B (en) | Double-beam lime kiln | |
| TW201037069A (en) | Carbonization plant with waste gas recirculation | |
| CN103742911B (en) | Fully premixed gas burner | |
| CN205447747U (en) | Ultralow NOx combustor of hot flue gas self -loopa type | |
| CN202119244U (en) | Tunnel kiln for firing ceramic heat accumulator | |
| CN203432300U (en) | Hot air circulation device of tunnel kiln | |
| CN105570890A (en) | Hot flue gas self-circulation type ultra-low NOx combustor | |
| CN101776277A (en) | Method and device for improving heat efficiency of combustion furnace by oxygen-rich partial oxygen-enriched jet flow combustion supporting | |
| CN203432302U (en) | Novel pushed slab kiln sintered by direct flame | |
| CN104098114B (en) | A kind of production method of potassium sulfate | |
| CN203947018U (en) | Indirect cooled glass liquid supply channel | |
| CN207527571U (en) | A kind of natural gas boiler low nitrogen burning system | |
| CN202813341U (en) | Biomass briquette fuel burner | |
| CN103333978B (en) | Top-burning hot-blast stove with cone-column composite vault structure | |
| CN201501894U (en) | Top combustion stove with jet nozzles which are in staggered arrangement for rotary jetting and precombustion chamber | |
| CN204042897U (en) | Lead flame tube burner | |
| CN201007484Y (en) | A ceramic burner with an annular arrangement of vertically upward nozzles | |
| CN101092292A (en) | Stepped active lime shaft kiln and calcining process thereof | |
| CN110107888A (en) | A kind of uniform distribution biomass fuel combustion equipment and its combustion method | |
| CN205372531U (en) | Biomass gasification combustor | |
| CN214528830U (en) | A supplementary heating structure for coke oven carbonization chamber | |
| CN204460689U (en) | A kind of biomass thermal wind furnace | |
| CN1215307C (en) | Reduced atmosphere firing method and device for ceramic muffle kiln |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080423 Termination date: 20120606 |