CN203668247U - Ceramic dry pressing powder processing device - Google Patents
Ceramic dry pressing powder processing device Download PDFInfo
- Publication number
- CN203668247U CN203668247U CN201320830231.6U CN201320830231U CN203668247U CN 203668247 U CN203668247 U CN 203668247U CN 201320830231 U CN201320830231 U CN 201320830231U CN 203668247 U CN203668247 U CN 203668247U
- Authority
- CN
- China
- Prior art keywords
- dry
- filler bin
- powder
- output terminal
- atomizing
- 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
Abstract
The utility model discloses a ceramic dry pressing powder processing device. The ceramic dry pressing powder processing device comprises a ball mill, a mud pit, a mud pump and an atomizing drying tower connected in sequence, wherein the mud pump in the mud pit is connected with the atomizing drying tower through a pipeline. The ceramic dry pressing powder processing device is characterized in that a powder storage device is connected with the output end of the atomizing drying tower; a dry-method pelletizing granulator is connected with the powder storage device. According to the utility model, the ceramic dry pressing powder processing device has the characteristics of simplicity in operation, high reliability, strong device universality and the like, and the prepared products can solve the problems that a ceramic tile product is dry, large in burning shrinkage, liable to deformation, large in later-period processing charges and the like.
Description
Technical field
The utility model relates to ceramic production device technical field, particularly relates to a kind of secondary granulation powder manufacturing apparatus and milling method of ceramic dry-pressed.
Background technology
The flouring technology of ceramic dry-pressed has several.The one, ceramic raw material is through wet milling, press filtration, oven dry, beats powder prilling process.Although the grinding efficiency of wet milling and raw material good evenness, beat the particle shape that powder granulation obtains round, powder poor fluidity, causes that adobe compactness is inconsistent, distortion, the defect such as easy to crack.The 2nd, wet ball grinding, atomization drying prilling process.The powder obtaining is hollow ball body, powder good fluidity, and adobe compactness improves, and distortion and cracking defect significantly reduce, but still have deformation of products, and the planar products of large specification needs edging, strikes off and polishing.The 3rd, dry method is milled, the dry method that adds water balling-up granulation, again dry method.Mainly solve the wet milling water yield high, the shortcoming that later stage energy consumption for drying is large; And because non-slurry pelletizing is solid sphere, the density of molding blank is large, follow-up being dried, burning till shunk little.But still there is the oven dry pre-treatment of one of clay raw materials, raw material mixture homogeneity is poor; Because solid particle hardness is large, between the particle of molding blank, there is the defect of minim gap; The particle of non-slurry pelletizing also needs to dry again; Adapt to personalized product is difficult, technique general applicability is poor, and the blank that is only applicable to sanitary equipment or ornamental brick uses, and is therefore never applied by large-scale popularization.
Summary of the invention
The purpose of this utility model is exactly the deficiency in order to solve prior art and the one that provides is simple to operate, and reliability is high, the powder manufacturing apparatus of the ceramic dry-pressed that equipment interoperability is strong.
The utility model is to adopt following technical solution to realize above-mentioned purpose: a kind of powder manufacturing apparatus of ceramic dry-pressed; comprise the wet method grinding machine, suction pit, slush pump and the atomizing dry tower that connect successively; the mud of suction pit; connect atomizing dry tower by the pipeline before and after slush pump; it is characterized in that; the output terminal of described atomizing dry tower is connected with powder storage device, and powder storage device is connected with dry method balling-up tablets press.
As further illustrating of such scheme, dry method balling-up tablets press is the one of rotating chop the chop tablets press and swash plate Free-rolling tablets press; The atomizing type of atomizing dry tower is one centrifugal and spraying; Wet method grinding machine is that one or both of ball mill and agitator mill share.
Described powder storage device comprises the two or more filler bins one that are arranged between atomizing dry tower and dry method balling-up tablets press, wherein the output terminal of at least one filler bin one connects dry method balling-up tablets press, and the output terminal of at least one filler bin one is connected with mixer; The output terminal of dry method balling-up tablets press is connected with at least one filler bin two; the output terminal of filler bin two connects mixer; atomization drying powder and the non-slurry pelletizing powder of part are mixed by a certain percentage; the advantage that little distortion of solid particle molding shrinkage and the easy compacting of hollow granule can be plugged the gap combines; reach the production requirement of high-quality product, tool has an unexpected effect.
The output terminal of described atomizing dry tower is connected with lift one, and lift one output terminal connects filler bin one; Between dry method balling-up tablets press and filler bin two, be connected with lift two.
The output terminal of described mixer is connected with filler bin three, between mixer and filler bin three, be connected with lift three, the discharge port below of filler bin three is provided with travelling belt one, the below of travelling belt one is provided with filler bin four, and the discharge port below of filler bin four is provided with powder is transported to the travelling belt two in press.
Described powder storage device comprises the filler bin five being arranged between atomizing dry tower and dry method balling-up tablets press; the output terminal of atomizing dry tower is connected with lift four; the output terminal of lift four connects filler bin five; the discharge port of filler bin five connects after dry method balling-up tablets press; be connected to a filler bin six by lift five outputs; the discharge port below of filler bin six is provided with travelling belt three; the below of travelling belt three is provided with filler bin seven, and the discharge port below of filler bin seven is provided with powder is transported to the travelling belt four in press.
The beneficial effect that the utility model adopts above-mentioned technical solution to reach is:
1, the utility model adopts a kind of secondary granulation powder manufacturing apparatus of ceramic dry-pressed, powder can be whole non-slurry pelletizing powder, also the atomization drying powder and the non-slurry pelletizing powder that can novels, anecdotes, etc. divide mix by a certain percentage, have simple to operate, the features such as reliability is high, and equipment interoperability is strong.
2, the powder preparation method of taking atomization drying granulation powder to mix by a certain percentage with dry method balling-up granulation powder, the advantage that little distortion of solid particle molding shrinkage and the easy compacting of hollow granule can be plugged the gap combines, solve ceramic tile product drying, burnt till and shrink greatly, volatility, the problems such as post-production expense is large, improve quality product, there is significant economic benefit.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of embodiment 2.
Description of reference numerals: 1, ball mill by wet process 2, atomizing dry tower 3, suction pit 4, slush pump 5, slurry pool 6, powder storage device 7, dry method balling-up tablets press 8, filler bin 1, mixer 10, lift 1, filler bin 2 12, lift 2 13, discharge port 14, filler bin 3 15, lift 3 16, travelling belt 1, filler bin 4 18, press 19, travelling belt 2 20, filler bin 5 21, lift 4 22, filler bin 6 23, travelling belt 3 24, filler bin 7 25, travelling belt four.
Embodiment
Below in conjunction with specific embodiment, specific embodiments of the present utility model is described in further detail.
As shown in Figure 1, the powder manufacturing apparatus of a kind of ceramic dry-pressed of the utility model, comprise the ball mill by wet process 1, the atomizing dry tower 2 that connect successively, the output terminal of ball mill by wet process 1 is connected with suction pit 3, the slush pump 4 of suction pit 3 connects atomizing dry tower 2 by pipeline, the slush pump 4 of suction pit is arranged on slurry pool 5 outsides, and pug is pumped in atomizing dry tower.The output terminal of atomizing dry tower 2 is connected with powder storage device 6, and powder storage device 6 is connected with dry method balling-up tablets press 7.Dry method balling-up tablets press 7 is for rotating the one of chop the chop tablets press and swash plate Free-rolling tablets press; The atomizing type of atomizing dry tower 2 is one centrifugal and spraying; Wet method grinding machine 1 is that one or both of ball mill and agitator mill share.Powder storage device 6 comprises the two or more filler bins 1 that are arranged between atomizing dry tower 2 and dry method balling-up tablets press 7, the present embodiment is three, wherein the output terminal of 7, one filler bins 1 of the output terminal of at least one filler bin 1 connection dry method balling-up tablets press is connected with mixer 9; The output terminal of atomizing dry tower is connected with lift 1, and lift one 10 output terminals connect filler bin 1, and the output terminal of dry method balling-up tablets press is connected with three filler bins 2 11, between dry method balling-up tablets press 7 and filler bin 2 11, is connected with lift 2 12.The output terminal of filler bin 2 11 connects mixer 9, atomization drying powder and the non-slurry pelletizing powder of part are mixed by a certain percentage, the advantage that little distortion of solid particle molding shrinkage and the easy compacting of hollow granule can be plugged the gap combines, reach the production requirement of high-quality product, tool has an unexpected effect.The output terminal of mixer 9 is connected with filler bin 3 14, between mixer 9 and filler bin 3 14, be connected with lift 3 15, discharge port 13 belows of filler bin 3 14 are provided with travelling belt 1, the below of travelling belt 1 is provided with filler bin 4 17, and the discharge port below of filler bin 4 17 is provided with powder is transported to the travelling belt 2 19 in press 18.
In preparation process; the ceramic size of suction pit; through slush pump pressurization, atomization heat drying in spray-drying tower, powder falls into filler bin one through lift one; part spray drying powder is through dry granulating machine granulation; enter filler bin two, filler bin one is mixed into filler bin three through mixer in proportion with the powder that enters filler bin two, after the transmission of travelling belt one and travelling belt two; finally extrusion forming in press, becomes base substrate.
Specific operation process is: first by ceramic raw material through batching, wet milling, delivers to atomizing dry tower drying-granulating by pump by ceramic size; Then the powder of part is again through dry method balling-up granulation, and powder carries out dry-pressing formed through press; Powder mixes by a certain percentage with atomization drying powder and non-slurry pelletizing powder.The particle diameter of powder granule prepared by described atomizing dry tower is less than the particle diameter of the powder granule of dry method balling-up preparation, the hollow granule that the molding shrinkage that dry method balling-up granulation is obtained is out of shape the easy pressure that little solid particle prepares with atomizing dry tower fully mixes, fill up the space between solid particle by hollow granule, reach the production requirement of high-quality product.
As shown in Figure 2, the difference of the present embodiment and above-mentioned embodiment is, powder storage device 6 comprises the filler bin 5 20 being arranged between atomizing dry tower 2 and dry method balling-up tablets press 7, the output terminal of atomizing dry tower 2 is connected with lift 4 21, the output terminal of lift 4 21 connects filler bin 5 20, the discharge port of filler bin 5 20 connects after dry method balling-up tablets press 7, be connected to a filler bin 6 22 by lift 5 20 outputs, the discharge port below of filler bin 6 22 is provided with travelling belt 3 23, the below of travelling belt 3 23 is provided with filler bin 7 24, the discharge port below of filler bin 7 24 is provided with powder is transported to the travelling belt 4 25 in press.
Transport tape is conveyed into ball mill by ceramic raw material and mills; ceramic size is discharged into suction pit; pressurize through slush pump; atomization heat drying in spray-drying tower; powder falls into filler bin five through lift five, then through dry granulating machine granulation, enters filler bin six, filler bin seven; finally extrusion forming in press, becomes base substrate.
Above-described is only preferred implementation of the present utility model; it should be pointed out that for the person of ordinary skill of the art, do not departing under the prerequisite of the utility model creation design; can also make some distortion and improvement, these all belong to protection domain of the present utility model.
Claims (8)
1. the powder manufacturing apparatus of a ceramic dry-pressed; comprise the ball mill, suction pit, slush pump and the atomizing dry tower that connect successively; the slush pump of suction pit connects atomizing dry tower by pipeline; it is characterized in that; the output terminal of described atomizing dry tower is connected with powder storage device, and powder storage device is connected with dry method balling-up tablets press.
2. the powder manufacturing apparatus of ceramic dry-pressed according to claim 1, it is characterized in that, described powder storage device comprises the two or more filler bins one that are arranged between atomizing dry tower and dry method balling-up tablets press, wherein the output terminal of at least one filler bin one connects dry method balling-up tablets press, and the output terminal of at least one filler bin one is connected with mixer; The output terminal of dry method balling-up tablets press is connected with at least one filler bin two, and the output terminal of filler bin two connects mixer.
3. the powder manufacturing apparatus of ceramic dry-pressed according to claim 2, is characterized in that, the output terminal of described atomizing dry tower is connected with lift one, and lift one output terminal connects filler bin one; Between dry method balling-up tablets press and filler bin two, be connected with lift two.
4. the powder manufacturing apparatus of ceramic dry-pressed according to claim 2, it is characterized in that, the output terminal of described mixer is connected with filler bin three, between mixer and filler bin three, be connected with lift three, the discharge port below of filler bin three is provided with travelling belt one, the below of travelling belt one is provided with filler bin four, and the discharge port below of filler bin four is provided with powder is transported to the travelling belt two in press.
5. the powder manufacturing apparatus of ceramic dry-pressed according to claim 1, it is characterized in that, described powder storage device comprises the filler bin five being arranged between atomizing dry tower and dry method balling-up tablets press, the output terminal of atomizing dry tower is connected with lift four, the output terminal of lift four connects filler bin five, the discharge port of filler bin five connects after dry method balling-up tablets press, be connected to a filler bin six by lift five outputs, the discharge port below of filler bin six is provided with travelling belt three, the below of travelling belt three is provided with filler bin seven, the discharge port below of filler bin seven is provided with powder is transported to the travelling belt four in press.
6. the powder manufacturing apparatus of ceramic dry-pressed according to claim 1, is characterized in that, described dry method balling-up tablets press is the one of rotating chop the chop tablets press and swash plate Free-rolling tablets press.
7. the powder manufacturing apparatus of ceramic dry-pressed according to claim 1, is characterized in that, the atomizing type of described atomizing dry tower is one centrifugal and spraying.
8. the powder manufacturing apparatus of ceramic dry-pressed according to claim 1, is characterized in that, wet method grinding machine is that one or both of ball mill and agitator mill share.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320830231.6U CN203668247U (en) | 2013-12-14 | 2013-12-14 | Ceramic dry pressing powder processing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320830231.6U CN203668247U (en) | 2013-12-14 | 2013-12-14 | Ceramic dry pressing powder processing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203668247U true CN203668247U (en) | 2014-06-25 |
Family
ID=50964563
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320830231.6U Expired - Fee Related CN203668247U (en) | 2013-12-14 | 2013-12-14 | Ceramic dry pressing powder processing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203668247U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103693964A (en) * | 2013-12-14 | 2014-04-02 | 游洪 | Ceramic dry pressing pulverizing device and method |
| CN106336222A (en) * | 2016-08-29 | 2017-01-18 | 佛山市陶泽新能源科技有限公司 | Powder making equipment with ceramic dry-pressing forming and production method |
| CN107056307A (en) * | 2017-03-23 | 2017-08-18 | 淄博峰霞陶瓷有限公司 | The dry and wet milling method and device of ceramic dry-pressed |
-
2013
- 2013-12-14 CN CN201320830231.6U patent/CN203668247U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103693964A (en) * | 2013-12-14 | 2014-04-02 | 游洪 | Ceramic dry pressing pulverizing device and method |
| CN103693964B (en) * | 2013-12-14 | 2015-12-09 | 游洪 | A kind of powder manufacturing apparatus of ceramic dry-pressed and method |
| CN106336222A (en) * | 2016-08-29 | 2017-01-18 | 佛山市陶泽新能源科技有限公司 | Powder making equipment with ceramic dry-pressing forming and production method |
| CN107056307A (en) * | 2017-03-23 | 2017-08-18 | 淄博峰霞陶瓷有限公司 | The dry and wet milling method and device of ceramic dry-pressed |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103833376B (en) | The device and method of preparation ceramic tile forming powders | |
| CN106431204B (en) | Waste slag ceramics brick and powder used, adobe body and preparation method thereof | |
| CN103693964B (en) | A kind of powder manufacturing apparatus of ceramic dry-pressed and method | |
| CN105294086B (en) | A kind of ceramic tile and preparation method | |
| CN101480813A (en) | Cleaning energy-saving processing technique of ceramic raw material dry powder prilling | |
| CN103664195B (en) | Standardized continuous treatment method of ceramic raw material and production line thereof | |
| CN102557583A (en) | Energy-saving dry powder production method for building ceramics | |
| CN203668247U (en) | Ceramic dry pressing powder processing device | |
| CN102795862A (en) | Device and method for preparing permanent magnet ferrite presintering material by dry process | |
| CN106336222A (en) | Powder making equipment with ceramic dry-pressing forming and production method | |
| CN103056959A (en) | Ceramics raw material preparation dry method and short process craft | |
| CN101786160A (en) | Special molybdenum powder used for automatic forming and preparation method thereof | |
| CN104529412A (en) | Preparation method of nano-scale hexagonal boron nitride/silicon dioxide multi-phase ceramic material | |
| CN103922679A (en) | Autoclaved sand-lime bricks manufactured by using building waste materials and crystal glass solid waste and manufacturing method thereof | |
| CN104261866A (en) | Production method for coal gangue ceramsite | |
| EP3402590A1 (en) | Process and system for the dry granulation of powdered ceramic mixture | |
| CN102060541A (en) | Production method of polished tile | |
| CN102320076B (en) | Method for producing dry granules of ceramic raw material powder | |
| CN113399093B (en) | Method for preparing spheroidic powder by mechanical crushing method and spheroidic powder | |
| CN103506053A (en) | Circular mold pelleting machine and production technology thereof | |
| CN206654865U (en) | The dry and wet fuel pulverizing plant of ceramic dry-pressed | |
| CN203558979U (en) | Standardized continuous treatment production line for ceramic raw materials | |
| CN102101322A (en) | Production technology of arge-particle ceramic tile | |
| CN101913892A (en) | Method for producing homogenized alumina | |
| CN102010181A (en) | Building ceramic dry-press power formed high-intensity body and preparation method thereof |
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: 20140625 Termination date: 20171214 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |