CN202725128U - Granulation part structure of coal ash ceramsite production line - Google Patents
Granulation part structure of coal ash ceramsite production line Download PDFInfo
- Publication number
- CN202725128U CN202725128U CN201220463335.3U CN201220463335U CN202725128U CN 202725128 U CN202725128 U CN 202725128U CN 201220463335 U CN201220463335 U CN 201220463335U CN 202725128 U CN202725128 U CN 202725128U
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- China
- Prior art keywords
- belt conveyor
- granulation
- coal ash
- production line
- part structure
- 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 - Lifetime
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- 238000005469 granulation Methods 0.000 title claims abstract description 32
- 230000003179 granulation Effects 0.000 title claims abstract description 32
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 31
- 239000010883 coal ash Substances 0.000 title abstract description 29
- 239000000463 material Substances 0.000 claims abstract description 37
- 238000007599 discharging Methods 0.000 claims abstract description 17
- 239000000203 mixture Substances 0.000 claims abstract description 9
- 239000010881 fly ash Substances 0.000 claims description 17
- 238000002156 mixing Methods 0.000 claims description 7
- 238000005303 weighing Methods 0.000 description 17
- 239000000654 additive Substances 0.000 description 12
- 230000000996 additive effect Effects 0.000 description 12
- 150000001875 compounds Chemical class 0.000 description 12
- 238000009736 wetting Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 5
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 4
- 229910052698 phosphorus Inorganic materials 0.000 description 4
- 239000011574 phosphorus Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000012467 final product Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 239000002671 adjuvant Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 239000000049 pigment Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000004566 building material Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 238000003032 molecular docking Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000004382 potting Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
Images
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
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/60—Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes
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- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a granulation part structure of a coal ash ceramsite production line. The granulation part structure is characterized by comprising a mixture belt conveyor which is obliquely arranged, wherein the lower end of the mixture belt conveyor is provided with a feeding port and is correspondingly formed below a discharging port of a humidification agitator, a distribution skirt mechanism is arranged below the discharging port in the upper end of the mixture belt conveyor and comprises a feeding barrel and two discharging barrels, the feeding barrel is vertically arranged, the upper end of the feeding barrel is positioned below the discharging port in the upper end of the mixture belt conveyor, the lower end of the feeding barrel is connected with the two discharging barrels so as to form a Y-shaped material channel, and the lower ends of the two discharging barrels are respectively and correspondingly provided with a disc-type granulator. The granulation part structure adopts the disc-type granulator for automatically granulating, is reasonable in structure and has the characteristics of high granulation efficiency, long service life and the like.
Description
Technical field
The utility model relates to flyash pollution control field and building material field, especially relates to a kind of granulation part-structure of the lytag production line for construction material.
Background technology
Flyash is one of trade waste of China's annual emissions and accumulative total volume of cargo in storage maximum, about 1.8 hundred million tons of every annual emissions, and the flyash of accumulation brings serious environmental problem.In the prior art, there is a kind of technology of flyash being fired again the haydite of using for building, the haydite of firing can be used in building structure insulation, industrial equipment insulation, bridge structure etc., also can be used for concrete aggregate, substitute natural sandstone and reach the effect that high-strength light is saved natural resources.
The for example disclosed a kind of lytag of CN1821161N and production method, its lytag, be comprised of flyash and the aqueous solution, it is characterized in that selecting the flyash of phosphorus content 25-35% and the flyash of phosphorus content 59% to be mixed, respectively accounting for percentage is 15-20% and 70-80%; The aqueous solution contains NaOH, gelling resin, pigment, bath of glass and water, and it respectively accounts for percentage and is (NaOH60%+ gelling resin 5%+ pigment 5%+ bath of glass 30%) 1%, water 99%; Lytag contains: the fine coal 70-80% of flyash 15-20%, the phosphorus content 5-9% of phosphorus content 25-35%, aqueous solution 0.15-04%.
The disclosed a kind of method of making lytag of CN101439964A for example again, this invention relates to the method for making lytag, include material and proportioning and the technological process of production, material mixture ratio is that flyash 85-95%, coal dust 1-10% and clay 0-10% compound concentration are the combustion adjuvant solution 1%-2% of 0.5%-0.05%, technological process is for stirring first mixture processed, spraying combustion adjuvant solution, rolling potting grain ball base, sieve, advance kiln roasting 1.0-1.5 hour to mixture, kiln discharge after being cooled to below 600 ℃ cools off to get the lytag finished product naturally.The method can make interior all the contained inflammable constituents of haydite ball base be fully burned, except being conducive to improve efficiency of combustion, reducing cost, outside shortening roasting time, enhancing productivity, also overcome the situation that the lytag color and luster differs in the prior art, hardness differs, for lytag is used for the building and ornament materials assurance that provides the foundation.
Above-mentioned these prior aries all disclose proportioning raw material or the sintering process of lytag, but do not have the production equipment of open concrete preparation.In the prior art, in preparation during lytag, the preparation before sintering particularly, often only be directly to pour nodulizer into after adopting simply manual weighing's raw material also to mix to carry out granulation, its production scale is less, limited by manpower, is difficult to realize large-scale production.
In current condition, the trade waste of flyash for piling up, the long-term accumulation causes industrial pollution serious, affected environment for human survival.So the applicant considers, if can design a kind of can the large batch of lytag production line of rapidly flyash being processed, then not only can play the raising haydite and prepare production efficiency, can also play the effect of administering the flyash environmental pollution faster and betterly.Simultaneously, when the granulation part-structure of this lytag production line of design, just need to consider how to improve the problems such as granulation efficiency, extension device life-span.
The utility model content
For above-mentioned deficiency, technical problem to be solved in the utility model is how to provide a kind of granulation efficiency high, the lytag production line granulation part-structure that equipment life is long.
In order to solve the problems of the technologies described above, adopted following technical scheme in the utility model:
A kind of lytag production line granulation part-structure, its characteristics are, described granulation part-structure comprises the compound belt conveyor that is obliquely installed, described compound belt conveyor lower end is feed end and the corresponding discharging opening below that is arranged on described wetting stirrer, below, discharging opening place, compound belt conveyor upper end is provided with sub-material skirt mechanism, described sub-material skirt mechanism comprises a feeding cylinder and two discharge barrels, feeding cylinder vertically arranges and the upper end is positioned at below, discharging opening place, compound belt conveyor upper end, the feeding cylinder lower end connects two discharge barrels and is formed into the material channel of Y-shaped, and two discharge barrel lower ends separately correspondence are provided with a dribbling balling machine.
In the utility model, consider that dribbling balling machine has certain altitude, so adopted the compound belt conveyor to promote conveying, then designed sub-material skirt mechanism and material is assigned to carried out simultaneously the granulation balling-up in two dribbling balling machines; So both can improve granulation speed doublely, greatly improve production efficiency.
As optimization, two discharge barrel tip positions are fixedly installed a receiver in the described sub-material skirt mechanism.After optimizing like this, material is introduced into receiver after feeding cylinder is fallen into, slide into the discharge barrel on both sides after receiver is taken advantage of and expired again, and can improve the uniformity that two discharge barrel materials distribute, avoid simultaneously material directly to impact angle, two discharge barrel tops and caused wearing and tearing, improved service life of equipment.
In sum, the utility model adopts dribbling balling machine to realize the automation granulation, and simultaneously its setting rational in infrastructure makes it possess granulation efficiency height, the characteristics such as long service life.The lytag production line with pipeline system granulation function in enormous quantities can be designed based on the utility model, the processing speed to trade waste flyash can be greatly improved; So solving industrial pollution, there is huge meaning in the aspects such as raising environmental protection.
Description of drawings
Fig. 1 is a kind of structural representation that has adopted the lytag production line of the utility model structure.
Fig. 2 is independent sub-material skirt mechanism and dribbling balling machine side view partly among Fig. 1.
The specific embodiment
The utility model is described in further detail below in conjunction with a kind of lytag production line that has adopted the utility model structure.
During implementation, as depicted in figs. 1 and 2, a kind of lytag production line that adopts the utility model structure comprises batch mixing part and granulation part;
Described batch mixing part-structure comprises coal ash storehouse 1, coal ash feed screw 2, coal ash weighing screw machine 3, additive weigh belt machine 4, bucket elevator 5 and wetting stirrer 6, wherein, described coal ash storehouse 1 is supported in ground by bracing frame, 1 lower end, coal ash storehouse is that cone-shaped and the bottom that diameter reduces gradually is the coal ash bin discharge port external, the coal ash bin discharge port external docks with described coal ash feed screw 2 feeding cylinders, and coal ash bin discharge port external place also is provided with the butterfly valve 7 for the control load; Coal ash feed screw 2 is supported in ground and setting that discharge barrel at one end is inclined upwardly, and coal ash feed screw discharge barrel docks with coal ash weighing screw machine 3 charging ports downwards; The discharging port of coal ash weighing screw machine 3 arranges over against the lifting feed hopper 8 of bucket elevator 5 lower ends downwards; The feed end of described additive weigh belt machine 4 is provided with the additive feed hopper, and the discharge end of additive weigh belt machine 4 is communicated with the lifting feed hopper 8 of bucket elevator 5; Described bucket elevator 5 vertically is installed in the mounting groove that is lower than ground, bucket elevator 5 lower ends are feed end and are provided with described lifting feed hopper 8, and the upper end of described bucket elevator 5 is above ground level and be provided with the chute 9 that tilts to the outer lower side in upper end discharging place docking; Chute 9 below correspondences are arranged on the feed hopper top of described wetting stirrer 6;
Described granulation part-structure comprises the compound belt conveyor 10 that is obliquely installed, described compound belt conveyor 10 lower ends are feed end and the corresponding discharging opening below that is arranged on described wetting stirrer 6, below, discharging opening place, compound belt conveyor 10 upper end is provided with sub-material skirt mechanism 11, described sub-material skirt mechanism 11 comprises a feeding cylinder and two discharge barrels, feeding cylinder vertically arranges and the upper end is positioned at below, discharging opening place, compound belt conveyor upper end, the feeding cylinder lower end connects two discharge barrels and is formed into the material channel of Y-shaped, and two discharge barrel lower ends separately correspondence are provided with a dribbling balling machine 12.Wherein, two discharge barrel tip positions are fixedly installed a receiver in the described sub-material skirt mechanism 11.
During above-mentioned lytag production line implementation, the equipment such as described coal ash feed screw, coal ash weighing screw machine, additive weigh belt machine, bucket elevator, wetting stirrer and dribbling balling machine separately, all are ripe existing equipments, can directly buy installation.Wherein, when referring to possess the material weighing function, adopt described coal ash weighing screw machine spiral way to advance the equipment of material, it can carry out weighing to the material of larger flow, adopt belt to carry out the equipment of mass transport when described additive weigh belt machine refers to have the weighing function, be applicable to the material weighing than low discharge.Its concrete structure is not at this detailed description.
Above-mentioned lytag production line is the production equipment that is used for the granulation part for lytag production, wherein, because coal ash is main material in the proportioning material, be in great demand, deposit in advance in it for coal ash so designed the coal ash storehouse, additive gets final product so directly add because materials are less.When this production line uses, coal ash enters into the coal ash feed screw from lower end, coal ash storehouse discharging opening, send into the lifting feed hopper that coal ash weighing screw machine carries out entering after the weighing bucket elevator by the coal ash feed screw again, additive enters from the additive feed hopper simultaneously, enters the lifting feed hopper of bucket elevator after additive weigh belt machine carries out weighing; Then promote through bucket elevator and send in the wetting stirrer by chute.Humidification and mixing in wetting stirrer.Deliver to finally by the compound belt conveyor and to carry out the granulation balling-up in the dribbling balling machine.Directly inputting agglomerating plant after the granulation carries out sintering and gets final product again.So just realized the streamline production of granulation.
In the above-mentioned lytag production line, in the batch mixing part-structure, adopt to coal ash and additive respectively the mode of Weighting and Controlling charging guarantee its proportion relation.Wherein coal ash is larger because of materials, so adopt coal ash weighing screw machine to carry out weighing, additive is less because of materials, gets final product so adopt the weigh belt machine to carry out weighing.Adopt bucket elevator to rise to after the weighing and carry out separately humidification and stirring in the wetting stirrer, guarantee mixed effect.Simultaneously, also considered the installation site of each equipment in the batch mixing part-structure, made the compacter and saving space of its overall structure.In the granulation part-structure, consider that dribbling balling machine has certain altitude, so adopted the compound belt conveyor to promote conveying, then adopt sub-material skirt mechanism that material is assigned to and carry out simultaneously the granulation balling-up in two dribbling balling machines; Can improve granulation speed doublely.
In the above-mentioned lytag production line, two discharge barrel tip positions are fixedly installed a receiver in the described sub-material skirt mechanism.Material is introduced into receiver after feeding cylinder is fallen into like this, after taking advantage of and expire, receiver slides into again the discharge barrel on both sides, can improve the uniformity that two discharge barrel materials distribute, avoid simultaneously material directly to impact angle, two discharge barrel tops and caused wearing and tearing, improve service life of equipment.
In sum, above-mentioned lytag production has realized first the purpose of flyash pipeline system granulation in enormous quantities, has the automaticity height, and topology layout is compact, and production efficiency is high, saves the advantages such as space.Simultaneously, this equipment has greatly improved the processing speed to trade waste flyash; So solving industrial pollution, there is huge meaning in the aspects such as raising environmental protection.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220463335.3U CN202725128U (en) | 2012-09-12 | 2012-09-12 | Granulation part structure of coal ash ceramsite production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220463335.3U CN202725128U (en) | 2012-09-12 | 2012-09-12 | Granulation part structure of coal ash ceramsite production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202725128U true CN202725128U (en) | 2013-02-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220463335.3U Expired - Lifetime CN202725128U (en) | 2012-09-12 | 2012-09-12 | Granulation part structure of coal ash ceramsite production line |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202725128U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103570341A (en) * | 2013-11-14 | 2014-02-12 | 山东恒远利废技术发展有限公司 | Complete equipment for molding ceramsite |
| CN109821476A (en) * | 2019-03-18 | 2019-05-31 | 杭州国电机械设计研究院有限公司 | A kind of flyash in great mixed amount balling-up granulating system and balling-up prilling process |
-
2012
- 2012-09-12 CN CN201220463335.3U patent/CN202725128U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103570341A (en) * | 2013-11-14 | 2014-02-12 | 山东恒远利废技术发展有限公司 | Complete equipment for molding ceramsite |
| CN103570341B (en) * | 2013-11-14 | 2015-04-15 | 山东恒远利废技术发展有限公司 | Complete equipment for molding ceramsite |
| CN109821476A (en) * | 2019-03-18 | 2019-05-31 | 杭州国电机械设计研究院有限公司 | A kind of flyash in great mixed amount balling-up granulating system and balling-up prilling process |
| CN109821476B (en) * | 2019-03-18 | 2024-02-02 | 杭州国电机械设计研究院有限公司 | High-dosage fly ash balling and granulating system and balling and granulating method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: CHONGQING HAOPAN ENERGY SAVING TECHNOOGY CO., LTD. Free format text: FORMER NAME: CHONGQING HAOPAN ENERGY SAVING TECHNOOGY LTD. |
|
| CP03 | Change of name, title or address |
Address after: 400039 Chongqing Jiulongpo Shiqiaopu Yuzhou Road 27 No. 18-13 Patentee after: CHONGQING HAOPAN ENERGY SAVING TECHNOLOGY CO.,LTD. Address before: 400039 Chongqing Jiulongpo Shiqiaopu Yuzhou Road No. 17 Hua Yu capital 27 Building No. 18-13 Patentee before: CHONGQING HAOPAN ENERGY-SAVING SCIENCE & TECHNOLOGY Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 400039 Chongqing Jiulongpo Shiqiaopu Yuzhou Road 27 No. 18-13 Patentee after: CHONGQING HAOPAN ENERGY-SAVING SCIENCE & TECHNOLOGY Co.,Ltd. Address before: 400039 Chongqing Jiulongpo Shiqiaopu Yuzhou Road 27 No. 18-13 Patentee before: CHONGQING HAOPAN ENERGY SAVING TECHNOLOGY CO.,LTD. |
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| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130213 |