CN113769841A - Sanitary ceramic slurry pulping production processing device and processing technology thereof - Google Patents
Sanitary ceramic slurry pulping production processing device and processing technology thereof Download PDFInfo
- Publication number
- CN113769841A CN113769841A CN202111136799.3A CN202111136799A CN113769841A CN 113769841 A CN113769841 A CN 113769841A CN 202111136799 A CN202111136799 A CN 202111136799A CN 113769841 A CN113769841 A CN 113769841A
- Authority
- CN
- China
- Prior art keywords
- slurry
- cone
- conveyer belt
- ceramic
- ball milling
- 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
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Crushing And Grinding (AREA)
Abstract
The production and processing device for the ceramic sanitary slurry and the processing technology thereof comprise a feeding machine, a conveying mechanism, an underground octagonal pool, a stirring machine, a sieving machine, a ball mill and a mixing kettle, wherein the raw materials are independently pulverized by a cone and then mixed with ball milling components to form ceramic slurry. The invention adopts a separate slurry process, namely a production process of forming slurry by separately slurrying the cone beating raw material and then mixing the cone beating raw material with the ball milling component, so that the original mineral structure of the cone beating material is ensured, the good cracking performance of the ceramic slurry is ensured, the cracking time is prolonged by 10-20 minutes compared with the traditional ball milling process, and the cracking problem in the drying process of the blank body is obviously reduced.
Description
Technical Field
The invention relates to the technical field of sanitary ceramic manufacturing and processing, in particular to a device and a process for producing and processing slurry of sanitary ceramic slurry.
Background
The sanitary ware refers to ceramic and hardware household equipment applied to toilets and kitchens. The sanitary ware is mainly made of ceramic, glass fiber reinforced plastic, artificial marble (agate), stainless steel and other materials. Compared with other types of sanitary ware, the ceramic sanitary ware has the advantages of white texture, soft color, compact structure, higher strength, good thermal stability and the like, and is widely used. A typical ceramic-type plumbing fixture includes: toilet, wash basin, sink, etc.
The ceramic sanitary slurry is a key process in the processing process of ceramic products, the ceramic sanitary slurry is generally prepared by a ball milling process, the traditional ball milling process is to put all raw materials including primary materials, secondary materials and cone beating materials into balls for ball milling, but the primary materials and the secondary materials need ball milling for a certain time to ensure that the raw materials are uniformly dispersed. In the ball milling process, the flaky structure of the conical ramming mineral is changed, and the cracking performance of the slurry is seriously influenced.
Disclosure of Invention
The invention provides a production and processing device and a processing technology for ceramic sanitary ware slurry, which are used for solving the problems that the cracking performance cannot be ensured because the original mineral structure of a conical ramming material is changed in the slurry processing process in the prior art.
The technical scheme adopted by the invention for solving the technical problems is as follows:
the utility model provides a sanitary ceramic thick liquids ization thick liquid production processingequipment, including the feeding machine, transport mechanism, eight aluminium ponds in underground, the mixer, the screening machine, the ball mill and mix the cauldron, transport mechanism is by the conveyer belt, transfer conveyer belt and portable conveyer belt are constituteed, the feeding machine export links to each other with the conveyer belt import, the conveyer belt export links to each other with transfer conveyer belt import, the transfer conveyer belt links to each other with eight aluminium ponds in underground through portable conveyer belt, the export in eight aluminium ponds in underground communicates with each other with the mixer import, the mixer export links to each other with the screening machine, the ball mill export and the screening machine export link to each other with mixing the cauldron import respectively.
The production and processing technology of the ceramic sanitary slurry adopts the ceramic sanitary slurry production and processing device, adopts the cone beating raw material to independently slurry, and then forms ceramic slurry after being mixed with ball milling components, and the concrete process steps are as follows:
(1) the method comprises the following steps of (1) carrying out cone beating and slurry formation, wherein cone beating raw materials are sent into a feeding machine to be crushed, weighed and sent into an underground octagonal pool through a conveying mechanism, water glass, a water reducing agent and cone beating materials are added into each underground octagonal pool, then the mixture is sent into a stirrer to be stirred and slurry is formed, and the specific gravity of cone beating slurry after the slurry is well formed is controlled between 1.760 and 1.770;
(2) ball milling, wherein the primary material and the secondary material are sequentially weighed and fed into a ball mill, and the specific gravity of the ball grinding material is controlled between 1.780 and 1.785 after the ball milling is finished;
(3) and (3) mixing, namely feeding the cone beating slurry and the ball milling material into a mixing kettle together for mixing to obtain ceramic slurry, wherein the specific gravity of the ceramic slurry is between 1.770 and 1.775 finally.
The mass of the water glass added in the cone ramming material is 0.5-1.0% of that of the cone ramming material, and the mass of the water reducing agent added in the cone ramming material is 0.02-0.2%.
The invention adopts a separate slurry process, namely a production process of forming slurry by separately slurrying the cone beating raw material and then mixing the cone beating raw material with the ball milling component, so that the original mineral structure of the cone beating material is ensured, the good cracking performance of the ceramic slurry is ensured, the cracking time is prolonged by 10-20 minutes compared with the traditional ball milling process, and the cracking problem in the drying process of the blank body is obviously reduced.
Drawings
The invention is further illustrated with reference to the following figures and examples.
FIG. 1 is a schematic process flow diagram of the apparatus of the present invention.
In the figure, a feeder 1, a conveyor belt 2, a transfer conveyor belt 3, a movable conveyor belt 4, an underground octagonal pool 5, a stirrer 6, a sieving machine 7, a ball mill 8 and a mixing kettle 9 are arranged.
Detailed Description
As shown in the figure: the utility model provides a sanitary ceramic thick liquids ization thick liquid production processingequipment, including feeder 1, transport mechanism, eight aluminium ponds in underground 5, mixer 6, screening machine 7, ball mill 8 and mixed cauldron 9, transport mechanism is by conveyer belt 2, transfer conveyer belt 3 and portable conveyer belt 4 are constituteed, the feeder export links to each other with the conveyer belt import, the conveyer belt export links to each other with the transfer conveyer belt import, the transfer conveyer belt links to each other with eight aluminium ponds in underground through portable conveyer belt, the export in eight aluminium ponds in underground communicates with each other with the mixer import, the mixer export links to each other with the screening machine, ball mill export and screening machine export link to each other with mixed cauldron import respectively.
The production and processing technology of the ceramic sanitary slurry adopts the ceramic sanitary slurry production and processing device, adopts the cone beating raw material to independently slurry, and then forms ceramic slurry after being mixed with ball milling components, and the concrete process steps are as follows:
(1) the method comprises the steps of (1) carrying out cone beating and slurry formation, feeding cone beating raw materials into a feeding machine for crushing, weighing, then feeding the crushed cone beating raw materials into underground octagonal pools through a conveying mechanism, adding 700kg of water, 30-70kg of water glass, 1-15kg of water reducing agent and 7000 kg of cone beating materials into each underground octagonal pool, then feeding the mixture into a stirring machine for stirring and slurry formation, wherein the specific gravity of the cone beating slurry is controlled between 1.760-1.770;
(2) ball milling, wherein the primary material and the secondary material are sequentially weighed and fed into a ball mill, and the specific gravity of the ball grinding material is controlled between 1.780 and 1.785 after the ball milling is finished;
(3) and (3) mixing, namely feeding the cone beating slurry and the ball milling material into a mixing kettle together for mixing to obtain ceramic slurry, wherein the specific gravity of the ceramic slurry is between 1.770 and 1.775 finally.
The mass of the water glass added in the cone ramming material is 0.5-1.0% of that of the cone ramming material, and the mass of the water reducing agent added in the cone ramming material is 0.02-0.2%.
And (3) adjusting the rotating speed of the stirrer by a frequency converter in the step (1). The control system can set the rotation direction of the stirrer, can set 6 time stages at most, and can set the frequency and the stirring time of each stage. The best slurry efficiency solution is found by the example 4.
Claims (3)
1. The utility model provides a sanitary ceramic thick liquids ization thick liquid production processingequipment, characterized by includes the feeder, transport mechanism, eight aluminium ponds in underground, the mixer, the screening machine, the ball mill and mix the cauldron, transport mechanism is by the conveyer belt, transfer conveyer belt and portable conveyer belt are constituteed, the feeder export links to each other with the conveyer belt import, the conveyer belt export links to each other with transfer conveyer belt import, the transfer conveyer belt links to each other with eight aluminium ponds in underground through portable conveyer belt, the export in eight aluminium ponds in underground communicates with each other with the mixer import, the mixer export links to each other with the screening machine, the export of ball mill and screening machine export link to each other with mixing the cauldron import respectively.
2. A production and processing technology of ceramic sanitary slurry adopts the production and processing device of ceramic sanitary slurry as claimed in claim 1, adopts a cone beating raw material to carry out slurry independently, and then forms ceramic slurry after being mixed with a ball milling component, and the concrete process steps are as follows:
(1) the method comprises the following steps of (1) carrying out cone beating and slurry formation, wherein cone beating raw materials are sent into a feeding machine to be crushed, weighed and sent into an underground octagonal pool through a conveying mechanism, water glass, a water reducing agent and cone beating materials are added into each underground octagonal pool, then the mixture is sent into a stirrer to be stirred and slurry is formed, and the specific gravity of cone beating slurry after the slurry is well formed is controlled between 1.760 and 1.770;
(2) ball milling, wherein the primary material and the secondary material are sequentially weighed and fed into a ball mill, and the specific gravity of the ball grinding material is controlled between 1.780 and 1.785 after the ball milling is finished;
(3) and (3) mixing, namely feeding the cone beating slurry and the ball milling material into a mixing kettle together for mixing to obtain ceramic slurry, wherein the specific gravity of the ceramic slurry is between 1.770 and 1.775 finally.
3. The production and processing technology of ceramic sanitary ware slurry according to claim 2, wherein the mass of the added water glass in the cone ramming material is 0.5-1.0% of that of the cone ramming material, and the mass of the added water reducing agent is 0.02-0.2% of that of the cone ramming material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202111136799.3A CN113769841A (en) | 2021-09-27 | 2021-09-27 | Sanitary ceramic slurry pulping production processing device and processing technology thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202111136799.3A CN113769841A (en) | 2021-09-27 | 2021-09-27 | Sanitary ceramic slurry pulping production processing device and processing technology thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
CN113769841A true CN113769841A (en) | 2021-12-10 |
Family
ID=78853819
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202111136799.3A Pending CN113769841A (en) | 2021-09-27 | 2021-09-27 | Sanitary ceramic slurry pulping production processing device and processing technology thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN113769841A (en) |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES473804A1 (en) * | 1977-10-13 | 1979-04-16 | Simmering Graz Pauker Ag | Method and apparatus for the preparation and activation of ceramic raw materials |
CN1693270A (en) * | 2005-05-29 | 2005-11-09 | 雷志刚 | Batching for ceramic blank and continuous powder milling material |
CN110143820A (en) * | 2019-06-11 | 2019-08-20 | 佛山市蓝之鲸科技有限公司 | Ceramic raw material wet process thin material slurrying mixture manufacturing line and its working method |
CN110202692A (en) * | 2019-05-23 | 2019-09-06 | 佛山市恒力泰机械有限公司 | Sand device is washed and starched in a kind of serialization |
CN110404657A (en) * | 2019-09-05 | 2019-11-05 | 广东鼎汇能科技股份有限公司 | A kind of ceramic raw material intelligence wet powder-making production technology |
CN112094100A (en) * | 2020-11-16 | 2020-12-18 | 佛山东鹏洁具股份有限公司 | High-efficiency ceramic slurry preparation process |
-
2021
- 2021-09-27 CN CN202111136799.3A patent/CN113769841A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES473804A1 (en) * | 1977-10-13 | 1979-04-16 | Simmering Graz Pauker Ag | Method and apparatus for the preparation and activation of ceramic raw materials |
CN1693270A (en) * | 2005-05-29 | 2005-11-09 | 雷志刚 | Batching for ceramic blank and continuous powder milling material |
CN110202692A (en) * | 2019-05-23 | 2019-09-06 | 佛山市恒力泰机械有限公司 | Sand device is washed and starched in a kind of serialization |
CN110143820A (en) * | 2019-06-11 | 2019-08-20 | 佛山市蓝之鲸科技有限公司 | Ceramic raw material wet process thin material slurrying mixture manufacturing line and its working method |
CN110404657A (en) * | 2019-09-05 | 2019-11-05 | 广东鼎汇能科技股份有限公司 | A kind of ceramic raw material intelligence wet powder-making production technology |
CN112094100A (en) * | 2020-11-16 | 2020-12-18 | 佛山东鹏洁具股份有限公司 | High-efficiency ceramic slurry preparation process |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101672035A (en) | High-strength prestressed concrete pipe-styled pile blended with ground river sands and production method thereof | |
CN202911000U (en) | Concrete high-quality raw material production system for building | |
CN106239696B (en) | Multi-functional hollow concrete segment machining production line | |
CN113213802A (en) | High-performance concrete admixture and production method thereof | |
CN107572852A (en) | A kind of production method of high-performance ground granulated blast furnace slag | |
CN101468492A (en) | Fly ash steam-pressing brisk production chain | |
CN113831142A (en) | Sanitary ceramic slurry pulping production processing device and processing technology thereof | |
CN202846704U (en) | Rear warehouse system for environment-friendly concrete enterprises | |
CN113769841A (en) | Sanitary ceramic slurry pulping production processing device and processing technology thereof | |
CN102229205B (en) | Continuous controllable dry mixed mortar stirring station | |
CN210999347U (en) | Cement production mixing arrangement | |
CN100464961C (en) | Serum pulping method and pulping equipment | |
CN209665846U (en) | A kind of ready-mixed concrete production system | |
CN211709665U (en) | Mixing mechanism for concrete mixing plant | |
CN108481555A (en) | A kind of building materials processing mixing device | |
CN211514696U (en) | Broken agitating unit of concrete raw materials | |
CN107297818A (en) | A kind of portable rapidly and efficiently mixer | |
CN103771898A (en) | Production system and production process for producing bricks by utilizing paper pulp sludge | |
CN206418028U (en) | A kind of ceramic glaze production system | |
CN107352895B (en) | Regenerated plastering mortar and preparation method thereof | |
CN115532357B (en) | Method for manufacturing silicate magnesium slag cement by using magnesium slag | |
CN212578884U (en) | A concrete ready-mixed device for mixing plant | |
CN211814181U (en) | Wet sand making double-frequency secondary dewatering device | |
CN109352813A (en) | A kind of integrated wallboard automatic production line | |
CN213556507U (en) | Homogenization device for calcium carbonate production |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20211210 |