CN201864651U - Granular material kiln-feeding system and plurality of screw-conveying granular material heating machines thereof - Google Patents
Granular material kiln-feeding system and plurality of screw-conveying granular material heating machines thereof Download PDFInfo
- Publication number
- CN201864651U CN201864651U CN2010205455195U CN201020545519U CN201864651U CN 201864651 U CN201864651 U CN 201864651U CN 2010205455195 U CN2010205455195 U CN 2010205455195U CN 201020545519 U CN201020545519 U CN 201020545519U CN 201864651 U CN201864651 U CN 201864651U
- Authority
- CN
- China
- Prior art keywords
- pellet
- kiln
- heater
- head spiral
- screw
- 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
Images
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a granular material kiln-feeding system and a plurality of screw-conveying granular material heating machines thereof. The disclosed plurality of screw-conveying granular material heating machines comprise at least two rows of screw conveyers arranged in a high temperature airflow channel, and granular materials are conveyed by the screw conveyers. In the conveying process, the granular materials are heated in the high temperature screw channel, so that the temperature of the granular materials before kiln-feeding is improved, which saves the fuel use amount in a glass melting kiln, achieves the aim of energy conservation and simultaneously increases the economical benefits of an enterprise; and through the adoption of a plurality of screw conveyers, the amount of the granular materials being heated is remarkably increased, and the heating efficiency of the granular materials is improved.
Description
Technical field
The utility model relates to the feedstock production field of glass manufacturing concern, particularly relates to a kind of multi-head spiral conveying pellet heater that pellet is gone into kiln system that is used for.In addition, the utility model also relates to and a kind ofly comprises that above-mentioned multi-head spiral carries the pellet of pellet heater to go into kiln system.
Background technology
Glass work is one of large-scale industry in the world, and along with the continuous development of society, the quantity of glassy product, quality and artistry thereof have obtained continuous development.World's glass output has reached several hundred million tons at present, and China is the first in the world glass production big country, and glass industries is a contamination type production industry, is one of reference index of weighing China's energy-saving and emission-reduction work.
In glass production enterprise, the admixtion of glass is continued to use the mode of powdery bulk cargo always and is fed in raw material in kiln, and there is following shortcoming in this feed way: the shape powder volume density of loosing is little, thermal conductivity is little, it is slow to conduct heat, and fusing is slow, wastes heat energy in kiln in the melting process; In the transportation of powder-material before going into kiln, one road dust from flying, contaminate environment, and corrosion hardware on the way; Powder-material can not corrode the kiln body before the fusing yet, stop up regenerator, the life-span of reducing kiln after going into kiln; The material side for preparing by glass ingredient, through flying upward of transportation, more expensive volatile one-tenth branch is subjected to loss in various degree, has destroyed the correct component proportions of frit, makes the degradation of glass material.Therefore, people expect powder-material is prepared into particulate material always, to overcome above-mentioned many shortcomings.
Therefore, how to make large batch of pellet not broken in course of conveying, not contaminated in heat-processed, improve the heat transfer efficiency between pellet and waste gas, to satisfy pellet production demand in enormous quantities, be the present technical issues that need to address of those skilled in the art.
The utility model content
The purpose of this utility model provides a kind of multi-head spiral conveying pellet heater that pellet is gone into kiln system that is used for, this multi-head spiral carries pellet heating function to guarantee that effectively pellet is not broken, not contaminated, improve pellet simultaneously and go into the preceding heating efficiency of kiln and go into the kiln amount, effectively improve the used heat utilization ratio.Another purpose of the present utility model provides a kind of pellet of above-mentioned multi-head spiral conveying pellet heater that comprises and goes into kiln system, and its economic benefit is improved.
For achieving the above object, the utility model provides a kind of multi-head spiral conveying pellet heater that pellet is gone into kiln system that is used for, and comprises and be located at the row of at least two in high temperature gas flow passage worm conveyor that pellet is carried through described worm conveyor.
Preferably, row's number of described worm conveyor is two to drain into eight rows, and the columns of the described worm conveyor of every row is that four row are to eight row.
Preferably, the length of described worm conveyor is greater than 6 meters.
Preferably, the gas in the described high temperature gas flow passage is the waste gas of glass melter.
Preferably, be provided with metal partion (metp) between described waste gas and the described pellet.
The utility model also provides a kind of pellet to go into kiln system, comprises pellet multiply dispenser, also comprises as above-mentioned each described multi-head spiral carrying the pellet heater, and pellet is carried the pellet heater through described pellet multiply dispenser and described multi-head spiral successively.
Multi-head spiral provided by the utility model is carried the pellet heater, is used for pellet and goes into kiln system pellet is heated.This multi-head spiral carries the pellet heater to comprise at least two row's worm conveyors, and by the above worm conveyor conveying of two rows pellet, pellet is fully heated in the high temperature gas flow passage, make the temperature of pellet before going into kiln obtain bigger raising, can save the firing rate in the glass melter, reach purpose of energy saving, also improve economic benefit of enterprises simultaneously.Worm conveyor is in the process of carrying pellet, and pellet can move on conveying belt always, can not turn over the shattering material, can effectively reduce the possibility of pellet fragmentation, guarantees the quality of pellet.And the above worm conveyor of two rows can significantly increase heated pellet quantity in the high temperature gas flow passage simultaneously, improves the heating efficiency of pellet, and that also improves pellet simultaneously goes into kiln efficient.
A kind of preferred embodiment in, the gas in the described high temperature gas flow passage is the waste gas of glass melter.Utilize the waste gas in the glass melter that pellet is heated, make full use of the waste heat of waste gas in the glass melter, the firing rate when significantly reducing the pellet heating improves economic benefit of enterprises.And if waste gas directly enters atmosphere, its higher temperature also can cause bad influence to environment, utilize waste gas that pellet is entered heating after, the temperature of waste gas reduces, and helps protecting environment, further improves the effect of energy-saving and emission-reduction.
In another preferred embodiment, be provided with metal partion (metp) between described waste gas and the described pellet.Promptly utilize metal partion (metp) that pellet and waste gas are separated, avoid the exhaust emission pellet, pyritous waste gas is with heat transferred heat conductivility good metal dividing plate, and metal partion (metp) is with the heat transferred pellet, thereby guaranteeing to have improved the temperature of pellet on the basis of pellet mass.
On the basis that provides above-mentioned multi-head spiral to carry the pellet heater, the utility model also provides a kind of pellet of above-mentioned multi-head spiral conveying pellet heater that comprises to go into kiln system; Because multi-head spiral carries the pellet heater to have above-mentioned technique effect, have this multi-head spiral and carry the pellet of pellet heater to go into kiln system also to have the corresponding techniques effect.
Description of drawings
Fig. 1 carries the structural representation of a kind of embodiment of pellet heater for multi-head spiral that the utility model provides;
Fig. 2 is that multi-head spiral shown in Figure 1 carries the A of pellet heater to view.
Embodiment
Core of the present utility model provides a kind of multi-head spiral conveying pellet heater that pellet is gone into kiln system that is used for, this multi-head spiral carries pellet heating function to guarantee that effectively pellet is not broken, not contaminated, improve pellet simultaneously and go into the preceding heating efficiency of kiln and go into the kiln amount, effectively improve the used heat utilization ratio.Another core of the present utility model provides a kind of pellet of above-mentioned multi-head spiral conveying pellet heater that comprises and goes into kiln system, and its economic benefit is improved.
The noun of locality such as forward and backward, upper and lower that this paper is related is to be that benchmark defines with the working direction of pellet in system, before the position of pellet elder generation process is, after through the position be after.The noun of locality that should be appreciated that herein to be adopted should not limit the protection domain of this patent.
In order to make those skilled in the art person understand the utility model scheme better, the utility model is described in further detail below in conjunction with the drawings and specific embodiments.
Please refer to Fig. 1 and Fig. 2, Fig. 1 carries the structural representation of a kind of embodiment of pellet heater for multi-head spiral that the utility model provides; Fig. 2 is that multi-head spiral shown in Figure 1 carries the A of pellet heater to view.
Multi-head spiral provided by the utility model is carried the pellet heater, is used for pellet and goes into kiln system pellet is heated.This multi-head spiral carries the pellet heater to comprise at least two row's worm conveyors 1, and by the above worm conveyor 1 conveying pellet 2 of two rows, pellet 2 is fully heated in high temperature gas flow passage 3, make the temperature of pellet 2 before going into kiln obtain bigger raising, can save the firing rate in the glass melter, reach purpose of energy saving, also improve economic benefit of enterprises simultaneously.Worm conveyor 1 is in the process of carrying pellet 2, and pellet 2 can move on conveying belt always, can not turn over the shattering material, can effectively reduce the possibility of pellet 2 fragmentations, guarantees the quality of pellet 2.And the above worm conveyor 1 of two rows can significantly increase heated pellet 2 quantity in high temperature gas flow passage 3 simultaneously, improves the heating efficiency of pellet 2, and that also improves pellet 2 simultaneously goes into kiln efficient.
In a kind of concrete embodiment, multi-head spiral provided by the utility model is carried and can be comprised in the pellet heater that two drain into eight row's worm conveyors 1, and every row has four to eight row worm conveyors 1, the worm conveyor battle arrays of the many rows of formation multiple rows.Go in the kiln system at pellet, multi-head spiral carries the front end of pellet heater to be provided with pellet multiply dispenser, be provided with the structure in the pellet multiply dispenser to such an extent that carry the pellet heater suitable with multi-head spiral, make an inlet of every worm conveyor just in time corresponding with an outlet of pellet multiply dispenser, pellet multiply dispenser distributes each strand pellet 2 that obtains to enter just in the worm conveyor 1, forms the matching structure of system.
Obviously, above-mentioned many rows multiple row worm conveyor battle array, the structure of its quantity can as long as distribute function effectively to cooperate with the pellet multiply, just can satisfy requirement of the present utility model according to producing the needs setting.
Particularly, can be more than 6 meters with the Design of length of worm conveyor 1, be about to worm conveyor commonly used 1 and prolong, to prolong the heat exchanger time between high temperature gas flow and the pellet, make pellet fully absorb the heat of high temperature gas flow, improve the temperature of pellet.
Need to prove that long worm conveyor 1 can not be connected to form with the worm conveyor 1 of several weak points.Simultaneously, this sentences the length direction of the working direction of pellet as worm conveyor 1.
A kind of preferred embodiment in, the gas in the high temperature gas flow passage 3 can be the waste gas of glass melter.Utilize the waste gas in the glass melter that pellet 2 is heated, make full use of the waste heat of waste gas in the glass melter, the firing rate when significantly reducing pellet 2 heating improves economic benefit of enterprises.And if waste gas directly enters atmosphere, its higher temperature also can cause bad influence to environment, utilize waste gas that pellet 2 is entered heating after, the temperature of waste gas reduces, and helps protecting environment, further improves the effect of energy-saving and emission-reduction.
Further, heat conductivility good metal dividing plate can be set between high temperature gas flow passage 3 and pellet 2, promptly utilize metal partion (metp) that pellet 2 and waste gas are separated, avoid exhaust emission pellet 2, pyritous waste gas is with heat transferred heat conductivility good metal dividing plate, metal partion (metp) is heat transferred pellet 2, thereby on the basis of guaranteeing pellet 2 quality, improved the temperature of pellet 2.Obviously, metal partion (metp) can also be other plate object with good heat conductive performance, as long as can separate waste gas and pellet 2, and the heat transferred pellet 2 of waste gas just can be able to be satisfied requirement of the present utility model.
In technical scheme further, multi-head spiral provided by the utility model is carried in the pellet heater, and the inlet M of high temperature gas flow passage 3 is located at the below of worm conveyor 1, and outlet N is located at the top of worm conveyor 1.According to the natural law, gas flow temperature has the trend that flows downward when reducing; Multi-head spiral of the present utility model is carried in the pellet heater, and behind the high temperature gas flow admission passage, with pellet 2 heat exchange, temperature reduces, and has the trend that moves downwards.Inlet is located at the below of worm conveyor 1, and the top that worm conveyor 1 is located in outlet can make air-flow carry the time sufficiently long that stops in the pellet heater with multi-head spiral, makes pellet 2 fully attract the heats of air-flows, improves the heats of pellet 2.
Except above-mentioned multi-head spiral is carried the pellet heater, the utility model also provides a kind of pellet of above-mentioned multi-head spiral conveying pellet heater that comprises to go into kiln system, and the structure that this pellet is gone into other each several parts of kiln system please refer to prior art, and this paper repeats no more.
More than pellet provided by the utility model gone into kiln system and multi-head spiral thereof carry the pellet heater to be described in detail.Used specific case herein principle of the present utility model and embodiment are set forth, the explanation of above embodiment just is used for helping to understand method of the present utility model and core concept thereof.Should be understood that; for those skilled in the art; under the prerequisite that does not break away from the utility model principle, can also carry out some improvement and modification to the utility model, these improvement and modification also fall in the protection domain of the utility model claim.
Claims (6)
1. one kind is used for the multi-head spiral conveying pellet heater that pellet is gone into kiln system, it is characterized in that, comprise and be located at the row of at least two in high temperature gas flow passage worm conveyor, pellet is carried through described worm conveyor.
2. the pellet that is used for according to claim 1 is gone into the multi-head spiral of kiln system and is carried the pellet heater, it is characterized in that, row's number of described worm conveyor is two to drain into eight rows, and the columns of the described worm conveyor of every row is that four row are to eight row.
3. the pellet that is used for according to claim 2 is gone into the multi-head spiral of kiln system and is carried the pellet heater, it is characterized in that the length of described worm conveyor is greater than 6 meters.
4. go into the multi-head spiral of kiln system and carry the pellet heater according to each described pellet that is used for of claim 1 to 3, it is characterized in that the gas in the described high temperature gas flow passage is the waste gas of glass melter.
5. the pellet that is used for according to claim 4 is gone into the multi-head spiral of kiln system and is carried the pellet heater, it is characterized in that, is provided with metal partion (metp) between described waste gas and the described pellet.
6. a pellet is gone into kiln system, comprise pellet multiply dispenser, it is characterized in that also comprise as each described multi-head spiral of claim 1 to 5 and carry the pellet heater, pellet is carried the pellet heater through described pellet multiply dispenser and described multi-head spiral successively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205455195U CN201864651U (en) | 2010-09-27 | 2010-09-27 | Granular material kiln-feeding system and plurality of screw-conveying granular material heating machines thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205455195U CN201864651U (en) | 2010-09-27 | 2010-09-27 | Granular material kiln-feeding system and plurality of screw-conveying granular material heating machines thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201864651U true CN201864651U (en) | 2011-06-15 |
Family
ID=44135813
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205455195U Expired - Fee Related CN201864651U (en) | 2010-09-27 | 2010-09-27 | Granular material kiln-feeding system and plurality of screw-conveying granular material heating machines thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201864651U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2491234C1 (en) * | 2012-01-13 | 2013-08-27 | Закрытое акционерное общество "Стромизмеритель" | Method of preparing mixture for making quenched cullet for foamed glass |
| CN104370112A (en) * | 2013-08-12 | 2015-02-25 | 苏州宏久航空防热材料科技有限公司 | Capsule material guiding equipment |
-
2010
- 2010-09-27 CN CN2010205455195U patent/CN201864651U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2491234C1 (en) * | 2012-01-13 | 2013-08-27 | Закрытое акционерное общество "Стромизмеритель" | Method of preparing mixture for making quenched cullet for foamed glass |
| CN104370112A (en) * | 2013-08-12 | 2015-02-25 | 苏州宏久航空防热材料科技有限公司 | Capsule material guiding equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102380903B (en) | Large-scale production process for paper surface gypsum boards with annual yield scale being 50 million square meters | |
| CN102320715A (en) | Presintering treatment process of glass batch and device thereof | |
| CN201864651U (en) | Granular material kiln-feeding system and plurality of screw-conveying granular material heating machines thereof | |
| CN103435276A (en) | Production apparatus of active lime | |
| CN103770363A (en) | Straw-type biomass pulverizing and forming system | |
| CN108518979A (en) | A kind of push-down aluminum-bar heating furnace | |
| CN201652325U (en) | Biomass double spiral wind cylinder type boiler | |
| CN202648130U (en) | Hot blast stove heating device | |
| CN115106284A (en) | Microwave drying pyrolysis slag treatment system and use method | |
| CN212315948U (en) | Novel high-temperature clinker cooling waste heat recycling and comprehensive utilization device for dry-process cement clinker production line | |
| CN205128141U (en) | Outfit of production tailing miropowder | |
| CN2865935Y (en) | Apparatus for producing uniform superfine metal powder body material | |
| CN203373276U (en) | Active lime production device | |
| CN208349818U (en) | A kind of push-down aluminum-bar heating furnace | |
| CN202660855U (en) | Efficient, energy-saving and environment friendly coal slime drying and processing system | |
| CN2877903Y (en) | Multiple continuous type fermentation drying device | |
| CN211400681U (en) | Coal slime drying equipment | |
| CN102506415B (en) | Energy-saving boiler system | |
| CN201834843U (en) | System for introducing particles into kiln and multi-strand particle distributor thereof | |
| CN221944809U (en) | Biomass fuel drying device | |
| CN110184103B (en) | Briquette coal | |
| CN102730707B (en) | Water glass (sodium silicate) production technique heat energy recycling system | |
| CN104109546B (en) | Multiple spot blanking upper-burning solid heat carrier retort technique | |
| CN2756588Y (en) | Hot material cab | |
| CN215559922U (en) | Water storage ceramsite production line |
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 |
Granted publication date: 20110615 Termination date: 20140927 |
|
| EXPY | Termination of patent right or utility model |