CN206654865U - The dry and wet fuel pulverizing plant of ceramic dry-pressed - Google Patents
The dry and wet fuel pulverizing plant of ceramic dry-pressed Download PDFInfo
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- CN206654865U CN206654865U CN201720293687.1U CN201720293687U CN206654865U CN 206654865 U CN206654865 U CN 206654865U CN 201720293687 U CN201720293687 U CN 201720293687U CN 206654865 U CN206654865 U CN 206654865U
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Abstract
A kind of dry and wet fuel pulverizing plant of ceramic dry-pressed is the utility model is related to, belongs to ceramic production device technical field.The dry and wet fuel pulverizing plant includes the wet granulation feed bin and non-slurry pelletizing feed bin being arranged side by side, the bottom connection micro-formula metering units of wet granulation feed bin, the output end connection batch mixer of micro-formula metering units；Powder meter is provided with the outlet at bottom of non-slurry pelletizing feed bin, the lower section of powder meter is provided with can be by the powder conveyer belt of powder carry to batch mixer, the outlet connection elevator of batch mixer, the output end connection blending bunker of elevator, the outlet at bottom connection press of blending bunker.The utility model ensure that the proportioning accuracy of burden process, reduce handling time, with dispensing efficiency high, labour cost is low the characteristics of, and for the intensive powder processed of ceramics, an economic transition scheme is provided for powder, improve product quality, the thermal efficiency, with significant economic benefit, the intensive manufacture of raw material is advantageously implemented.
Description
Technical field
A kind of dry and wet fuel pulverizing plant of ceramic dry-pressed is the utility model is related to, belongs to ceramic production device technology neck
Domain.
Background technology
The flouring technology of ceramic dry-pressed mainly has following two：First, ceramic raw material is through wet ball grinding, spray drying
The processes for wet granulation of granulation, the powder that the method is obtained are in hollow ball-shape, the good fluidity of powder, base substrate uniformity compared with
It is good, but the consistency of base substrate is not high, however it remains the problem of deformation of products, as glazed tile ripple and ink-jet ooze colored polished bricks decorative pattern
The defects of uneven, the process are commonly used in existing ceramic tile factory；Second, ceramic raw material is milled through dry method successively, dry method
Balling-up granulation, the dry granulation methods for drying (or natural drying) again, the method are to solve wet milling water height (to reach first
34% or so) the shortcomings that, later stage energy consumption for drying is big, next to that non-slurry pelletizing is medicine ball, the density of molding blank is big, follow-up
Dry, burn till and shrink small, the defects of deformation of products can be reduced.
At present, dry method flouring technology method is in popularization period in the production of ceramic tile, is not widely accepted also, a side
Abandon wet powder-making if face is existing factory and change dry method powder, stop production transformation, fund etc. are problematic in that；On the other hand energy-conservation subtracts
The policy guidance of row requires that china industry must develop to intensive manufacture direction, and will consume energy workshop section's concentrative operation high, that discharge is big,
Such as producing region centralized system powder, for powder, for the Arid Area in the north, clay moisture is few, is relatively adapted to dry method powder, but powder exists
Easily it is micronized during transport etc., causes molding blank lamination defect.
Utility model content
Deficiency of the prior art, the technical problems to be solved in the utility model are more than：It is dry to provide a kind of ceramics
Molded dry and wet fuel pulverizing plant, original wet powder-making device can be made full use of, at the same it is also intensive for china industry
Powder processed, for powder an economic transition scheme is provided, there is the characteristics of simple to operate, equipment interoperability is strong, dispensing is stable.
The dry and wet fuel pulverizing plant of ceramic dry-pressed described in the utility model, including the wet granulation feed bin being arranged side by side
With non-slurry pelletizing feed bin, the bottom connection micro-formula metering units of wet granulation feed bin, the output of micro-formula metering units
End connection batch mixer；Powder meter is provided with the outlet at bottom of non-slurry pelletizing feed bin, the lower section of powder meter is provided with can
By the powder conveyer belt of powder carry to batch mixer, the outlet connection elevator of batch mixer, the output end connection mixing of elevator
Feed bin, the outlet at bottom connection press of blending bunker.
Wherein：
Described micro-formula weigher unit includes built-in weighing sensor, roller bearing and dispensing cartridge arranged in parallel,
Dispensing cartridge travels forward by the drive of roller bearing, and weighing sensor electrically connects with PLC.
Described powder meter is any one in weight metering scale, volume metering scale.
Beneficial effect is possessed by the utility model：
The utility model ensure that the proportioning accuracy of burden process, reduce handling time, have dispensing efficiency high,
The characteristics of labour cost is low, wet granulation powder can be reduced with the powder preparation method that non-slurry pelletizing powder mixes by a certain percentage
Product occurs deforming and the problem of lamination defect, while can make full use of original wet powder-making device, and intensive for ceramics
Change powder processed, provide an economic transition scheme for powder, improve product quality, the thermal efficiency, there is significant economic benefit, have
Beneficial to the intensive manufacture for realizing raw material.
Brief description of the drawings
Fig. 1 is process chart of the present utility model；
In figure：1st, wet granulation feed bin；2nd, non-slurry pelletizing feed bin；3rd, powder meter；4th, powder conveyer belt；5th, batch mixing
Machine；6th, weighing sensor；7th, dispensing cartridge；8th, roller bearing；9th, elevator；10th, blending bunker；11st, press.
Embodiment
Embodiment of the present utility model is described further below in conjunction with the accompanying drawings：
As shown in figure 1, the dry and wet fuel pulverizing plant of ceramic dry-pressed includes wet granulation feed bin 1 and the dry method being arranged side by side
Feed bin 2, the bottom connection micro-formula metering units of wet granulation feed bin 1 are granulated, the output end of micro-formula metering units connects
Batch mixer 5 is connect, powder meter 3 is provided with the outlet at bottom of non-slurry pelletizing feed bin 2, the lower section of powder meter 3 is provided with can
By the powder conveyer belt 4 of powder carry to batch mixer 5, the outlet connection elevator 9 of batch mixer 5, the output end connection of elevator 9
Blending bunker 10, the outlet at bottom connection press 11 of blending bunker 10.Wherein, micro-formula weigher unit includes built-in title
Sensor 6, roller bearing 8 and dispensing cartridge 7 arranged in parallel are retransmitted, dispensing cartridge 7 travels forward by the drive of roller bearing 8, weighing sensor
Electrically connected with PLC；Powder meter 3 is any one in weight metering scale, volume metering scale.
Operating process is as follows：Powder in wet granulation feed bin 1 is by micro-formula metering units, via PLC
The weighing sensor 6 of control is added in dispensing cartridge 7 after measuring, the band trend that the powder in dispensing cartridge 7 then is passed through into roller bearing 8
It is preceding to move and be sent into batch mixer 5；Powder in non-slurry pelletizing feed bin 2 delivers to powder transmission belt 4 after the metering of powder meter 3
On, subsequently into batch mixer, two kinds of powders of dry and wet are mixed in the ratio of setting in batch mixer 5, mixed powder
Expect that boosted machine 9 is sent into blending bunker 10, mixed powder is compressing through press 11, forms base substrate, through subsequent decorations, burn till,
After cutting, turn into required product.
The automatization level of the utility model technology is high, realizes the continuous automatic work of burden process, improves production
Efficiency.
Claims (3)
1. a kind of dry and wet fuel pulverizing plant of ceramic dry-pressed, including the wet granulation feed bin (1) being arranged side by side and non-slurry pelletizing
Feed bin (2), it is characterised in that：The bottom connection micro-formula metering units of wet granulation feed bin (1), micro-formula metering units
Output end connection batch mixer (5)；Powder meter (3), powder meter are provided with the outlet at bottom of non-slurry pelletizing feed bin (2)
(3) lower section is provided with can be by the powder conveyer belt (4) of powder carry to batch mixer (5), the outlet connection lifting of batch mixer (5)
Machine (9), the output end connection blending bunker (10) of elevator (9), the outlet at bottom connection press (11) of blending bunker (10).
2. the dry and wet fuel pulverizing plant of ceramic dry-pressed according to claim 1, it is characterised in that：Micro-formula metering is single
Member includes built-in weighing sensor (6), roller bearing arranged in parallel (8) and dispensing cartridge (7), and dispensing cartridge (7) is by roller bearing (8)
Drive travels forward, and weighing sensor (6) electrically connects with PLC.
3. the dry and wet fuel pulverizing plant of ceramic dry-pressed according to claim 1, it is characterised in that：Powder meter (3)
For any one in weight metering scale, volume metering scale.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720293687.1U CN206654865U (en) | 2017-03-23 | 2017-03-23 | The dry and wet fuel pulverizing plant of ceramic dry-pressed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720293687.1U CN206654865U (en) | 2017-03-23 | 2017-03-23 | The dry and wet fuel pulverizing plant of ceramic dry-pressed |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206654865U true CN206654865U (en) | 2017-11-21 |
Family
ID=60316016
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720293687.1U Expired - Fee Related CN206654865U (en) | 2017-03-23 | 2017-03-23 | The dry and wet fuel pulverizing plant of ceramic dry-pressed |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206654865U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN111645168A (en) * | 2020-06-13 | 2020-09-11 | 哈尔滨农撷科技有限公司 | Automatic change 5G basic station ceramic filter production system |
-
2017
- 2017-03-23 CN CN201720293687.1U patent/CN206654865U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN111645168A (en) * | 2020-06-13 | 2020-09-11 | 哈尔滨农撷科技有限公司 | Automatic change 5G basic station ceramic filter production system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171121 |
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| CF01 | Termination of patent right due to non-payment of annual fee |