CN105436195A - Vertical processing treatment production line for recycling of ceramic slurry - Google Patents
Vertical processing treatment production line for recycling of ceramic slurry Download PDFInfo
- Publication number
- CN105436195A CN105436195A CN201511005401.7A CN201511005401A CN105436195A CN 105436195 A CN105436195 A CN 105436195A CN 201511005401 A CN201511005401 A CN 201511005401A CN 105436195 A CN105436195 A CN 105436195A
- Authority
- CN
- China
- Prior art keywords
- vertical
- drying device
- production line
- vertical drying
- recycles
- 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.)
- Pending
Links
- 239000000919 ceramic Substances 0.000 title claims abstract description 35
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 239000002002 slurry Substances 0.000 title abstract 5
- 238000004064 recycling Methods 0.000 title abstract 2
- 238000001035 drying Methods 0.000 claims abstract description 42
- 239000000428 dust Substances 0.000 claims abstract description 30
- 239000000843 powder Substances 0.000 claims abstract description 30
- 238000007599 discharging Methods 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 17
- 239000000463 material Substances 0.000 claims abstract description 15
- 239000010802 sludge Substances 0.000 claims description 20
- 238000012216 screening Methods 0.000 claims description 18
- 238000003860 storage Methods 0.000 claims description 14
- 239000004480 active ingredient Substances 0.000 abstract 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 238000005498 polishing Methods 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- 235000013312 flour Nutrition 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000003082 abrasive agent Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000003837 high-temperature calcination Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B2101/00—Type of solid waste
- B09B2101/02—Gases or liquids enclosed in discarded articles, e.g. aerosol cans or cooling systems of refrigerators
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Treatment Of Sludge (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a vertical processing treatment production line for recycling of ceramic slurry. The vertical processing treatment production line comprises a vertical drying device, a sorting device and a storing device which are sequentially arranged, wherein the vertical drying device is connected with a heat source device which can supply heat to the vertical drying device in the drying work as requirement. The vertical processing treatment production line further comprises a dehydrating device and a dust removing device, wherein a first conveying device for conveying a material from a discharging port of the dehydrating device to a feeding port of the vertical drying device is arranged between the dehydrating device and the vertical drying device; a second conveying device for conveying the material from the discharging port of the sorting device to the feeding port of the storing device is arranged between the sorting device and the storing device; the dust removing device is connected to the vertical drying device to remove the powder generated in the drying process. According to the vertical processing treatment production line, a complete set of device is provided to process and treat the ceramic slurry, so as to recycle the ceramic slurry; the main active ingredients in the ceramic slurry are extracted and applied to other fields; the vertical processing treatment production line is high in working efficiency, energy saving and environmentally friendly.
Description
Technical field
The present invention relates to solid ceramic Waste Disposal Technology field, particularly relate to a kind of ceramic sludge and recycle the vertical production line of processing process.
Background technology
Ceramic polished brick needs the surface to ceramic body with water and high-abrasive material to polish in process of production, forms a large amount of solid wastes, become ceramic polished mud after polishing.China is Production of Ceramics big country, and the amount of annual ceramic sludge is more than ten million ton, and the main component of ceramic sludge is silica and alundum (Al2O3), and its source accounts for toatl proportion about 70%, and sludge type is mainly semisolid waste material.By the end of the end of the year 2012, China has polished bricks production line 1081 altogether, day production capacity 1254.63 ten thousand square meter, annual capacity 41.4 hundred million square meter, the annual ceramic sludge amount produced in the whole nation is more than 2,300 ten thousand tons, these mud major parts are backfilling in soil by as backfill, because ceramic polished mud is through high-temperature calcination, itself shows as faintly acid, non-degradable in soil, produce serious pollution to environment, cause environmental disruption, therefore processing ceramic polished mud is current extremely urgent thing.
Application number be 201410690331.2 patent of invention disclose a kind of preparation method of Ceramic Tiles silica flour, specifically, the preparation process of Ceramic Tiles silica flour adopts ceramic tile polishing mud, by tower drier oven dry, sorting, then collect to obtain through finished product trap and be rich in silica and the supplementary cementitious material with hydration activity.This invention reaches certain ceramic polished sludge circulation recovering effect, but ceramic tile polishing mud just will can enter tower drier after natural air dry, causes the overlong time processed; Heat carrier does not make the easy contaminated environment of dust removal process, is therefore necessary to improve this.
Summary of the invention
In view of this, the object of the invention is to overcome the deficiencies in the prior art, provide that a kind for the treatment of effeciency is high, the ceramic sludge of environmental protection recycles the vertical production line of processing process.
In order to solve the problems of the technologies described above, the present invention adopts following scheme to realize:
A kind of ceramic sludge recycles the vertical production line of processing process, comprise the vertical drying device arranged successively, powder screening device and storage arrangement, described vertical drying device is connected with and can supplies the heat power supply device that it dries operation institute calorific requirement, also comprise dewater unit and dust arrester, first conveying arrangement that material can be transported to vertical drying device charging aperture from dewater unit discharging opening is provided with between described dewater unit and vertical drying device, second conveying arrangement that material can be transported to storage arrangement charging aperture from powder screening device discharging opening is provided with between described powder screening device and storage arrangement, described dust arrester is connected the dust produced to remove drying course with vertical drying device.
Ceramic sludge, first through dewater unit, makes the water content of ceramic sludge drop to proper level, and after entering into vertical drying device, vertical drying device more can be made to play usefulness, and dewater unit shortens the ceramic sludge pretreated time greatly.Vertical drying device provides heat to carry out material drying by heat power supply device, and in oven dry operation process, heat carrier can carry a large amount of dust, if directly discharge pollutes the environment, is therefore collected the dust in heat carrier by dust arrester.Enter powder screening device from vertical drying device material out and can collect out satisfactory particle, then be transported to storage arrangement by the second conveying arrangement to store, the undesirable particle filtered out by powder screening device reenters vertical drying device and again processes, whole polyvinyl chloride is efficient, energy-conserving and environment-protective.
Described dust arrester is cyclone dust collectors and the pulse dust collector of series connection, and the gas outlet of vertical drying device is connected with cyclone dust collectors.First use cyclone dust collectors, dirt gas classification process large for concentration, reduce resistance, after be further processed with pulse dust collector again, make treatment effect more outstanding.
Described heat power supply device comprises heat source furnace and gas generator, and heat source furnace is connected with vertical drying device respectively by pipeline with gas generator, with provide dry operation time required heat.
Described vertical drying device comprises tower drier, and described tower drier is connected with the air blast for providing air intake, and described powder screening device is that powder selects machine, and described powder selects the charging aperture of machine to be connected with the discharging opening of tower drier by pipeline.Material by the first conveying arrangement be transported to tower drier top, material is slowly downward by gravity, and the hot blast that the high wind that air blast provides and heat power supply device provide mixes mutually and carries out heat exchange with material, and powder is transferred to powder screening device by air pressure and carried out powder choosing.
Described dewater unit is filter press, and the first conveying arrangement is belt feeder, and the discharging opening of described filter press is corresponding with one end of belt feeder, and the other end of belt feeder is arranged on the top of vertical drying device, corresponding with the charging aperture of vertical drying device.
Described second conveying arrangement is bucket elevator, and the charge door of described bucket elevator is connected by the discharging opening of pipeline with powder screening device, and its discharge port is connected to storage arrangement by pipeline.
Compared with prior art, the present invention has following beneficial effect:
1. treatment effeciency of the present invention is high, environmental protection, reduces waste gas to the pollution of environment;
2. pair ceramic sludge is divided into different classes of superfines, waste resource is carried out recirculation and uses, and reduce polishing mud environmental pollution, last powder forms the products such as concrete admixture, coating additive, road surface anti-wear agent, forms social resources and is worth.
Accompanying drawing explanation
Fig. 1 is embodiment 1 structural representation;
Fig. 2 is embodiment 1 production line top view;
Wherein, wherein, 111, filter press; 331, tower drier; 332, air blast; 441, powder selects machine; 551, bucket elevator; 661, raw material cabin; 771, heat source furnace; 772, gas generator; 881, cyclone dust collectors; 882, pulse dust collector.
Detailed description of the invention
In order to allow those skilled in the art understand technical scheme of the present invention better, below in conjunction with accompanying drawing, the present invention is further elaborated.
Embodiment 1
As illustrated in fig. 1 and 2, a kind of ceramic sludge recycles the vertical production line of processing process, comprise the dewater unit arranged successively, vertical drying device, powder screening device and storage arrangement, first conveying arrangement that material can be transported to vertical drying device charging aperture from dewater unit discharging opening is provided with between described dewater unit and vertical drying device, the charging aperture of described powder screening device receives the material from vertical drying device discharging opening, second conveying arrangement that material can be transported to storage arrangement charging aperture from powder screening device discharging opening is provided with between described powder screening device and storage arrangement, also comprise heat power supply device and dust arrester, described heat power supply device is connected with vertical drying device respectively with dust arrester.Concrete, described dewater unit is filter press 111, first conveying arrangement is belt feeder, vertical drying device comprises tower drier 331, it is connected with the air blast 332 for providing air intake, the discharging opening of described filter press 111 is corresponding with one end of belt feeder, and the other end of belt feeder is arranged on the top of tower drier 331, corresponding with the charging aperture of tower drier 331.Described powder screening device is that powder selects machine 441, and described powder selects the charging aperture of machine 441 to be connected by the discharging opening of pipeline with tower drier 331.Described heat power supply device comprises heat source furnace 771 and gas generator 772, and heat source furnace 771 is connected with tower drier 331 respectively by pipeline with gas generator 772, with provide dry operation time required heat.Described dust arrester is cyclone dust collectors 881 and the pulse dust collector 882 of series connection, and the gas outlet of tower drier 331 is connected with cyclone dust collectors 881.Described second conveying arrangement is bucket elevator 551, and the charge door of described bucket elevator 551 selects the discharging opening of machine 441 to be connected by pipeline and powder, and its discharge port is connected to storage arrangement by pipeline, and described storage arrangement is raw material cabin 661.
Claims (6)
1. a ceramic sludge recycles the vertical production line of processing process, comprise the vertical drying device arranged successively, powder screening device and storage arrangement, described vertical drying device is connected with and can supplies the heat power supply device that it dries operation institute calorific requirement, it is characterized in that, also comprise dewater unit and dust arrester, first conveying arrangement that material can be transported to vertical drying device charging aperture from dewater unit discharging opening is provided with between described dewater unit and vertical drying device, second conveying arrangement that material can be transported to storage arrangement charging aperture from powder screening device discharging opening is provided with between described powder screening device and storage arrangement, described dust arrester is connected the dust produced to remove drying course with vertical drying device.
2. ceramic sludge according to claim 1 recycles the vertical production line of processing process, it is characterized in that, described dust arrester is cyclone dust collectors and the pulse dust collector of series connection, and the gas outlet of vertical drying device is connected with cyclone dust collectors.
3. ceramic sludge according to claim 1 recycles the vertical production line of processing process, it is characterized in that, described heat power supply device comprises heat source furnace and gas generator, and heat source furnace is connected with vertical drying device respectively by pipeline with gas generator, with provide dry operation time required heat.
4. ceramic sludge according to claim 1 recycles the vertical production line of processing process, it is characterized in that, described vertical drying device comprises tower drier, described tower drier is connected with the air blast for providing air intake, described powder screening device is that powder selects machine, and described powder selects the charging aperture of machine to be connected with the discharging opening of tower drier by pipeline.
5. ceramic sludge according to claim 1 recycles the vertical production line of processing process, it is characterized in that, described dewater unit is filter press, first conveying arrangement is belt feeder, the discharging opening of described filter press is corresponding with one end of belt feeder, the other end of belt feeder is arranged on the top of vertical drying device, corresponding with the charging aperture of vertical drying device.
6. ceramic sludge according to claim 1 recycles the vertical production line of processing process, it is characterized in that, described second conveying arrangement is bucket elevator, the charge door of described bucket elevator is connected by the discharging opening of pipeline with powder screening device, and its discharge port is connected to storage arrangement by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201511005401.7A CN105436195A (en) | 2015-12-29 | 2015-12-29 | Vertical processing treatment production line for recycling of ceramic slurry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201511005401.7A CN105436195A (en) | 2015-12-29 | 2015-12-29 | Vertical processing treatment production line for recycling of ceramic slurry |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105436195A true CN105436195A (en) | 2016-03-30 |
Family
ID=55547081
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201511005401.7A Pending CN105436195A (en) | 2015-12-29 | 2015-12-29 | Vertical processing treatment production line for recycling of ceramic slurry |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105436195A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106391667A (en) * | 2016-11-16 | 2017-02-15 | 重庆市鸦屿陶瓷有限公司 | Device for treatment of waste mud after rolling forming of ceramics |
| CN111066401A (en) * | 2020-01-19 | 2020-04-28 | 刘红英 | Agricultural ecology pond mud extraction element |
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| CN205253718U (en) * | 2015-12-29 | 2016-05-25 | 黄贺明 | Vertical production line of pottery silt cyclic utilization processing |
-
2015
- 2015-12-29 CN CN201511005401.7A patent/CN105436195A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002248465A (en) * | 2001-02-26 | 2002-09-03 | Japan Organo Co Ltd | Evaporation-to-dryness method for wastewater |
| CN101885610A (en) * | 2010-07-20 | 2010-11-17 | 杭州诺贝尔集团有限公司 | Recycling Method of Polished Brick Waste Slag |
| CN101898900A (en) * | 2010-07-20 | 2010-12-01 | 杭州诺贝尔集团有限公司 | Recycling method of ceramic tile polishing waste residue |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106391667A (en) * | 2016-11-16 | 2017-02-15 | 重庆市鸦屿陶瓷有限公司 | Device for treatment of waste mud after rolling forming of ceramics |
| CN106391667B (en) * | 2016-11-16 | 2017-09-19 | 重庆市鸦屿陶瓷有限公司 | A kind of useless pug processing unit after ceramic roll forming |
| CN111066401A (en) * | 2020-01-19 | 2020-04-28 | 刘红英 | Agricultural ecology pond mud extraction element |
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| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160330 |
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| RJ01 | Rejection of invention patent application after publication |