CN111730741A - Ceramic raw material preparation system - Google Patents
Ceramic raw material preparation system Download PDFInfo
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- CN111730741A CN111730741A CN202010686771.6A CN202010686771A CN111730741A CN 111730741 A CN111730741 A CN 111730741A CN 202010686771 A CN202010686771 A CN 202010686771A CN 111730741 A CN111730741 A CN 111730741A
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- raw material
- homogenizing
- drying tower
- spray drying
- tank
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C1/00—Apparatus or methods for obtaining or processing clay
- B28C1/003—Plant; Methods
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C1/00—Apparatus or methods for obtaining or processing clay
- B28C1/02—Apparatus or methods for obtaining or processing clay for producing or processing clay suspensions, e.g. slip
- B28C1/06—Processing suspensions, i.e. after mixing
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C1/00—Apparatus or methods for obtaining or processing clay
- B28C1/02—Apparatus or methods for obtaining or processing clay for producing or processing clay suspensions, e.g. slip
- B28C1/06—Processing suspensions, i.e. after mixing
- B28C1/08—Separating suspensions, e.g. for obtaining clay, for removing stones; Cleaning clay slurries
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C1/00—Apparatus or methods for obtaining or processing clay
- B28C1/10—Apparatus or methods for obtaining or processing clay for processing clay-containing substances in non-fluid condition ; Plants
- B28C1/12—Storing and conditioning in storage; Specially adapted storage spaces or devices for their filling or emptying; Tower structures for the storage of clay
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C1/00—Apparatus or methods for obtaining or processing clay
- B28C1/10—Apparatus or methods for obtaining or processing clay for processing clay-containing substances in non-fluid condition ; Plants
- B28C1/14—Apparatus or methods for obtaining or processing clay for processing clay-containing substances in non-fluid condition ; Plants specially adapted for homogenising, comminuting or conditioning clay in non-fluid condition or for separating undesired admixtures therefrom
- B28C1/18—Apparatus or methods for obtaining or processing clay for processing clay-containing substances in non-fluid condition ; Plants specially adapted for homogenising, comminuting or conditioning clay in non-fluid condition or for separating undesired admixtures therefrom for comminuting clay lumps
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C1/00—Apparatus or methods for obtaining or processing clay
- B28C1/10—Apparatus or methods for obtaining or processing clay for processing clay-containing substances in non-fluid condition ; Plants
- B28C1/14—Apparatus or methods for obtaining or processing clay for processing clay-containing substances in non-fluid condition ; Plants specially adapted for homogenising, comminuting or conditioning clay in non-fluid condition or for separating undesired admixtures therefrom
- B28C1/20—Apparatus or methods for obtaining or processing clay for processing clay-containing substances in non-fluid condition ; Plants specially adapted for homogenising, comminuting or conditioning clay in non-fluid condition or for separating undesired admixtures therefrom for separating undesired admixed bodies, e.g. stones
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G37/00—Combinations of mechanical conveyors of the same kind, or of different kinds, of interest apart from their application in particular machines or use in particular manufacturing processes
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- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Compositions Of Oxide Ceramics (AREA)
Abstract
A ceramic raw material preparation system relates to the technical field of ceramic green brick production and comprises a feeding machine, a ball mill, a slurry tank, an iron removing sieve, a homogenizing tank, a transfer homogenizing tank, a spray drying tower, a powder bin and a raw material conveying mechanism; the unloading end of feeding machine is connected to the ball mill, the discharge end of ball mill is connected to thick liquid pond, thick liquid pond is equipped with first plunger pump, the discharge gate of first plunger pump is connected to except that the iron sieve, the discharge end that removes the iron sieve is connected to the homogenization pond, the homogenization pond feeds through to the homogenization pond of transfer, the spray gun of spray drying tower is linked to in the homogenization pond of transfer, the raw materials exit linkage to powder storehouse of spray drying tower, the discharge gate of powder storehouse is connected to raw materials transport mechanism, raw materials transport mechanism is used for transporting the adobe raw materials to the suppression workshop of adobe and suppresses. By integrating and planning all the procedures, the automation of production, storage and conveying of raw materials is realized, and the production efficiency of the raw materials of the ceramic adobe is effectively improved.
Description
Technical Field
The invention relates to the technical field of ceramic adobe production, in particular to a ceramic raw material preparation system.
Background
Generally, the ceramic production process comprises 3 basic stages of green brick raw material preparation, green body forming, porcelain sintering and the like. The preparation of raw materials of the green bricks is the first link and the most basic link in the production of ceramics, and comprises three main processes of ball milling, slurry forming and drying. The existing ceramic factory is unreasonable in planning, so that the three processes can be completed in a plurality of workshops, manual transfer is needed among the processes, automatic production is difficult to realize, and the production efficiency of raw materials of green bricks is seriously influenced.
Disclosure of Invention
In view of the above-mentioned drawbacks, the present invention provides a ceramic raw material preparation system, which integrates and plans various processes to realize automation of raw material production, storage and transportation, thereby effectively improving the production efficiency of raw materials for ceramic bricks.
In order to achieve the purpose, the invention adopts the following technical scheme: a ceramic raw material preparation system comprises a feeding machine, a ball mill, a slurry tank, an iron removing sieve, a homogenizing tank, a transfer homogenizing tank, a spray drying tower, a powder bin and a raw material conveying mechanism;
the discharging end of the feeding machine is connected to the ball mill, the discharging end of the ball mill is connected to the slurry tank, the slurry tank is provided with a first plunger pump, the discharging port of the first plunger pump is connected to the de-ironing screen, the discharging end of the de-ironing screen is connected to the homogenizing tank, the homogenizing tank is communicated to the transit homogenizing tank, the transit homogenizing tank is communicated to the spray gun of the spray drying tower, the raw material outlet of the spray drying tower is connected to the powder bin, the discharging port of the powder bin is connected to the raw material transporting mechanism, and the raw material transporting mechanism is used for transporting raw brick materials to a raw brick pressing workshop for pressing.
Further, the transfer homogenizing pool is arranged above the homogenizing pool, the bottom of the transfer homogenizing pool is higher than the top of the spray drying tower, the homogenizing pool is provided with a second plunger pump, a discharge port of the second plunger pump is connected to the transfer homogenizing pool, and the bottom of the transfer homogenizing pool is communicated to the spray gun.
Further, the spray drying tower is provided with a raw material conveying pipe, the raw material conveying pipe comprises a first conveying section and a second conveying section, the first conveying section is arranged on the outer wall of the spray drying tower in a surrounding mode, the plurality of spray guns are distributed on the first conveying section, the first conveying section is communicated with one end of the second conveying section, and the other end of the second conveying section is communicated with the bottom of the transfer homogenizing pool.
Furthermore, the spray drying tower is provided with two material conveying pipes, and the plurality of spray guns are respectively distributed and arranged on the first conveying sections of the two material conveying pipes.
Further, raw materials transport mechanism includes flow control subassembly and transportation belt, flow control subassembly includes hopper and variable speed belt, the pan feeding mouth of hopper with the discharge gate of powder storehouse is connected, the discharge gate of hopper is located the top of variable speed belt, the terminal of variable speed belt with the transportation belt meets.
Further, the conveyor belt is provided with a plurality of carrier roller sets, and each carrier roller set is V-shaped.
Further, still include the tails and retrieve the mechanism, the spray drying tower still is equipped with the tails export, the tails is retrieved the mechanism and is included shale shaker and deironing subassembly, the deironing subassembly includes slip table and magnetic rod, the pan feeding mouth of shale shaker with the tails export meets, the top of slip table with the discharge gate of shale shaker meets, the bottom of slip table is connected to the powder storehouse, a plurality of the magnetic rod sets up the surface of slip table.
Further, the pulp tank, the homogenizing tank and the transit homogenizing tank are respectively provided with a stirrer.
The invention provides a ceramic raw material preparation system, which comprises the steps of firstly putting different types of minerals into a feeding machine in proportion, sending the minerals into a ball mill for ball milling to obtain original green brick powder, putting the green brick powder into a slurry tank for ageing, and optimizing the plasticity and viscosity of the green brick powder to obtain green brick mud. And then the first plunger pump is utilized to send the adobe pug aged in the slurry tank into the de-ironing screen for de-ironing, so that the influence of iron powder on the color and performance of adobes is avoided. And then the adobe pug after iron removal is sequentially sent into the homogenizing tank and the transit homogenizing tank for homogenization treatment, so that the components in the adobe pug are uniformly mixed, and the adobe pug is homogenized for a plurality of times, thereby improving the stability of adobe slurry. And then, feeding the adobe pug into the spray drying tower, spraying the adobe pug into powder by using a spray gun of the spray drying tower, and drying and settling in the spray drying tower to obtain an adobe raw material. And finally, conveying the produced green brick raw materials to the powder bin for storage. When the powder bin is required to be used, the powder bin is opened, the green brick raw materials are discharged on the raw material conveying mechanism, and the green brick raw materials are conveyed to a green brick pressing workshop by the raw material conveying mechanism to be pressed. By integrating and planning all the procedures, the automation of production, storage and conveying of raw materials is realized, and the production efficiency of the raw materials of the ceramic adobe is effectively improved.
Drawings
FIG. 1 is a system diagram of one embodiment of the present invention;
FIG. 2 is a system schematic of another embodiment of the present invention;
FIG. 3 is a schematic diagram of the structure of a material transport tube in an embodiment of the present invention;
FIG. 4 is a schematic structural view of a material transport mechanism in an embodiment of the present invention;
FIG. 5 is a schematic diagram of the tail recovery mechanism in one embodiment of the present invention;
FIG. 6 is a schematic structural view of an iron removal assembly in an embodiment of the present invention;
fig. 7 is a schematic diagram of the structure of a spray drying tower in an embodiment of the present invention.
Wherein: the device comprises a feeding machine 1, a ball mill 2, a slurry tank 3, an iron removing screen 4, a homogenizing tank 5, a transit homogenizing tank 6, a spray drying tower 7, a spray gun 71, a raw material conveying pipe 72, a first conveying section 721, a second conveying section 722, a powder bin 8, a raw material conveying mechanism 9, a flow control assembly 91, a hopper 911, a variable speed belt 912, a conveying belt 92, a carrier roller group 921, a tailing recycling mechanism 10, a vibrating screen 101, an iron removing assembly 102, a sliding table 1021 and a magnetic rod 1022.
Detailed Description
The technical scheme of the invention is further explained by the specific implementation mode in combination with the attached drawings.
Referring to fig. 1-7, a ceramic raw material preparation system comprises a feeder 1, a ball mill 2, a slurry tank 3, an iron removal sieve 4, a homogenizing tank 5, a transit homogenizing tank 6, a spray drying tower 7, a powder bin 8 and a raw material transportation mechanism 9;
the discharging end of the feeding machine 1 is connected to the ball mill 2, the discharging end of the ball mill 2 is connected to the slurry tank 3, the slurry tank 3 is provided with a first plunger pump, the discharging port of the first plunger pump is connected to the de-ironing screen 4, the discharging end of the de-ironing screen 4 is connected to the homogenizing tank 5, the homogenizing tank 5 is communicated to the transfer homogenizing tank 6, the transfer homogenizing tank 6 is communicated to the spray gun 71 of the spray drying tower 7, the raw material outlet of the spray drying tower 7 is connected to the powder bin 8, the discharging port of the powder bin 8 is connected to the raw material conveying mechanism 9, and the raw material conveying mechanism 9 is used for conveying raw brick materials to a green brick pressing workshop for pressing.
The invention provides a ceramic raw material preparation system, which comprises the steps of firstly putting different types of minerals into a feeding machine 1 in proportion, sending the minerals into a ball mill 2 for ball milling to obtain original green brick powder, putting the green brick powder into a slurry tank 3 for ageing, and optimizing the plasticity and viscosity of the green brick powder to obtain green brick mud. And then the adobe pug aged in the slurry tank 3 is sent into the de-ironing screen 4 by the first plunger pump to carry out de-ironing process, so that the influence of iron powder on the color and performance of adobes is avoided. And then the adobe pug after iron removal is sequentially sent into the homogenizing tank 5 and the transfer homogenizing tank 6 for homogenization treatment, so that the components in the adobe pug are uniformly mixed, and the adobe pug is homogenized for a plurality of times, thereby improving the stability of adobe slurry. And then, feeding the adobe pug into the spray drying tower 7, spraying the adobe pug into powder by using a spray gun 71 of the spray drying tower 7, and drying and settling in the spray drying tower 7 to obtain an adobe raw material. And finally, conveying the produced green brick raw materials to the powder bin 8 for storage. When the powder bin 8 needs to be used, the powder bin is opened, the green brick raw materials are discharged on the raw material conveying mechanism 9, and the green brick raw materials are conveyed to a green brick pressing workshop by the raw material conveying mechanism 9 to be pressed. By integrating and planning all the procedures, the automation of production, storage and conveying of raw materials is realized, and the production efficiency of the raw materials of the ceramic adobe is effectively improved.
Further, the transit homogenizing pool 6 is arranged above the homogenizing pool 5, the bottom of the transit homogenizing pool 6 is higher than the top of the spray drying tower 7, the homogenizing pool 5 is provided with a second plunger pump, a discharge port of the second plunger pump is connected to the transit homogenizing pool 6, and the bottom of the transit homogenizing pool 6 is communicated to the spray gun 71. Specifically, the transfer homogenizing pool 6 is arranged above the homogenizing pool 5, and the bottom of the transfer homogenizing pool 6 is higher than the top of the spray drying tower 7, so that a height difference exists between the transfer homogenizing pool 6 and a spray gun 71 of the spray drying tower 7, and the spray gun 71 is ensured to have enough pressure to spray adobe pugs, thereby being beneficial to spraying adobe raw materials with consistent particle sizes. Wherein the transfer homogenizing tank 6 for conveying the adobe pug from a low position to a high position is realized by arranging the second plunger pump in the homogenizing tank 5.
Further, as shown in fig. 3 and 7, the spray drying tower 7 is provided with a material conveying pipe 72, the material conveying pipe 72 includes a first conveying section 721 and a second conveying section 722, the first conveying section 721 is circumferentially arranged on the outer wall of the spray drying tower 7, a plurality of the spray guns 71 are distributed on the first conveying section 721, the first conveying section 721 is communicated with one end of the second conveying section 722, and the other end of the second conveying section 722 is communicated with the bottom of the intermediate homogenizing pool 6. Specifically, the green brick slurry is delivered to the first delivery section 721 through the second delivery section 722, and the first delivery section 721 distributes the green brick slurry to be sprayed out by each of the spray guns 71. By arranging the first conveying section 721 around the outer wall of the spray drying tower 7 and distributing a plurality of the spray guns 71 on the first conveying drive, a plurality of the spray guns 71 are annularly distributed on the spray drying tower 7, and green brick raw materials sprayed by the spray guns 71 are effectively prevented from colliding and bonding with each other.
Further, the spray drying tower 7 is provided with two material conveying pipes 72, and a plurality of the spray guns 71 are respectively distributed on the first conveying sections 721 of the two material conveying pipes 72. Specifically, the two raw material conveying pipes 72 are adopted to convey the green brick pug, so that the pressure fluctuation of the raw material conveying pipes is reduced, the pressure of the raw material conveying pipes 72 is kept unchanged, and the green brick raw materials with consistent grain sizes are further favorably sprayed.
Further, as shown in fig. 4, the raw material transportation mechanism 9 includes a flow control assembly 91 and a transportation belt 92, the flow control assembly 91 includes a hopper 911 and a variable speed belt 912, a feeding port of the hopper 911 is connected with a discharging port of the powder bin 8, the discharging port of the hopper 911 is located above the variable speed belt 912, and a terminal of the variable speed belt 912 is connected with the transportation belt 92. Specifically, the variable speed belt 912 is driven by a speed regulating motor or a servo motor, so that the transportation speed of the variable speed belt 912 can be adjusted. Because the bore of the discharge gate of hopper 911 is unchangeable, and the adobe raw materials are followed the volume that the material storehouse flows is certain, and the adobe raw materials fall to every second promptly the volume of variable speed belt 912 is certain, just the transportation speed of conveyer belt 92 also keeps unchangeable, consequently through changing the speed of variable speed belt 912 transportation speed, can realize that control adobe raw materials sends to the volume of conveyer belt 92, work as the transportation speed of variable speed belt 912 is on the high side, then transport to the volume of the adobe raw materials of conveyer belt 92 increases, work as the transportation speed of variable speed belt 912 is on the low side, then transport to the volume of the adobe raw materials of conveyer belt 92 reduces, conveniently adjusts the volume that the adobe raw materials sent to the adobe suppression workshop, does benefit to the ceramic adobe of preparing different specifications.
Further, the transport belt 92 has a plurality of idler sets 921, and each of the idler sets 921 is V-shaped. Specifically, the carrier belt 92 and the material weight are supported by providing the carrier roller group 921. Further, bearing roller group 921 is by the bearing roller group 921 that two slopes set up, through with bearing roller group 921 designs into the V type, the transportation terminal surface of transportation belt 92 is followed bearing roller group 921 forms the V type, makes in the adobe raw materials transportation, and the adobe raw materials is concentrated on transportation belt 92's middle part effectively avoids the adobe raw materials to fall out from transportation belt 92's both sides.
Further, as shown in fig. 5 and 6, the drying system further comprises a tailing recycling mechanism 10, and the spray drying tower 7 is further provided with a tailing outlet, wherein during the production of the ceramic tile blank raw material, a part of powder, commonly referred to as tailing in the industry, is attached to the inner wall of the spray drying tower 7, and when the spray drying tower 7 is cleaned, the raw material outlet of the spray drying tower 7 is closed, and the tailing outlet of the spray drying tower 7 is opened, so that the tailing is discharged from the tailing outlet. Mechanism 10 is retrieved to tails includes shale shaker 101 and deironing subassembly 102, deironing subassembly 102 includes slip table 1021 and magnetic rod 1022, the pan feeding mouth of shale shaker 101 with the tails export meets, the top of slip table 1021 with the discharge gate of shale shaker 101 meets, the bottom of slip table 1021 is connected to powder storehouse 8, a plurality of magnetic rod 1022 sets up the surface of slip table 1021. Specifically, as shown in fig. 5-6, the ceramic tailings discharged from the tailings outlet are firstly screened by the vibrating screen 101, agglomerated powder lumps are vibrated and waste materials with excessively large particle sizes are screened, and when the screened ceramic tailings slide on the sliding table 1021, the screened ceramic tailings pass through the magnetic rod 1022, and the scrap iron mixed in the tailings is attracted by the magnetism of the magnetic rod 1022, so that the purity of the recycled powder is improved, and the quality of the ceramic tile is prevented from being reduced due to the scrap iron mixed in the recycled powder. Wherein, the magnetic rod can be a rod body with a magnet embedded on the surface.
Further, the pulp tank 3, the homogenizing tank 5 and the transit homogenizing tank 6 are respectively provided with a stirrer. Specifically, the slurry tank 3, the homogenizing tank 5 and the transfer homogenizing tank 6 are respectively provided with a stirrer, so that powder can be uniformly mixed, and the powder mixing efficiency can be improved.
The technical principle of the present invention is described above in connection with specific embodiments. The description is made for the purpose of illustrating the principles of the invention and should not be construed in any way as limiting the scope of the invention. Based on the explanations herein, those skilled in the art will be able to conceive of other embodiments of the present invention without inventive effort, which would fall within the scope of the present invention.
Claims (8)
1. A ceramic raw material preparation system is characterized in that: comprises a feeding machine, a ball mill, a slurry tank, an iron removing sieve, a homogenizing tank, a transfer homogenizing tank, a spray drying tower, a powder bin and a raw material conveying mechanism;
the discharging end of the feeding machine is connected to the ball mill, the discharging end of the ball mill is connected to the slurry tank, the slurry tank is provided with a first plunger pump, the discharging port of the first plunger pump is connected to the de-ironing screen, the discharging end of the de-ironing screen is connected to the homogenizing tank, the homogenizing tank is communicated to the transit homogenizing tank, the transit homogenizing tank is communicated to the spray gun of the spray drying tower, the raw material outlet of the spray drying tower is connected to the powder bin, the discharging port of the powder bin is connected to the raw material transporting mechanism, and the raw material transporting mechanism is used for transporting raw brick materials to a raw brick pressing workshop for pressing.
2. The ceramic raw material preparation system according to claim 1, characterized in that: the transfer homogenizing pool is arranged above the homogenizing pool, the bottom of the transfer homogenizing pool is higher than the top of the spray drying tower, the homogenizing pool is provided with a second plunger pump, a discharge port of the second plunger pump is connected to the transfer homogenizing pool, and the bottom of the transfer homogenizing pool is communicated to the spray gun.
3. The ceramic raw material preparation system according to claim 2, characterized in that: the spray drying tower is provided with a raw material conveying pipe, the raw material conveying pipe comprises a first conveying section and a second conveying section, the first conveying section is arranged on the outer wall of the spray drying tower in a surrounding mode, a plurality of spray guns are distributed on the first conveying section, the first conveying section is communicated with one end of the second conveying section, and the other end of the second conveying section is communicated with the bottom of the transit homogenizing pool.
4. A ceramic raw material preparation system according to claim 3, characterized in that: the spray drying tower is provided with two material conveying pipes, and the plurality of spray guns are respectively distributed and arranged at the first conveying sections of the two material conveying pipes.
5. The ceramic raw material preparation system according to claim 1, characterized in that: raw materials transport mechanism includes flow control subassembly and transportation belt, flow control subassembly includes hopper and variable speed belt, the pan feeding mouth of hopper with the discharge gate of powder storehouse is connected, the discharge gate of hopper is located the top of variable speed belt, the terminal of variable speed belt with the transportation belt meets.
6. The ceramic raw material preparation system according to claim 5, characterized in that: the conveying belt is provided with a plurality of carrier roller sets, and each carrier roller set is V-shaped.
7. The ceramic raw material preparation system according to claim 1, characterized in that: still retrieve the mechanism including the tails, the spray drying tower still is equipped with the tails export, the tails is retrieved the mechanism and is included shale shaker and deironing subassembly, the deironing subassembly includes slip table and magnetic rod, the pan feeding mouth of shale shaker with the tails export meets, the top of slip table with the discharge gate of shale shaker meets, the bottom of slip table is connected to powder storehouse, a plurality of the magnetic rod sets up the surface of slip table.
8. The ceramic raw material preparation system according to claim 1, characterized in that: the pulp tank, the homogenizing tank and the transit homogenizing tank are respectively provided with a stirrer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010686771.6A CN111730741A (en) | 2020-07-16 | 2020-07-16 | Ceramic raw material preparation system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010686771.6A CN111730741A (en) | 2020-07-16 | 2020-07-16 | Ceramic raw material preparation system |
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| CN111730741A true CN111730741A (en) | 2020-10-02 |
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| CN202010686771.6A Pending CN111730741A (en) | 2020-07-16 | 2020-07-16 | Ceramic raw material preparation system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113119293A (en) * | 2021-03-03 | 2021-07-16 | 福建省漳州建华陶瓷有限公司 | Anti-cracking wear-resistant tile drying system and preparation method thereof |
-
2020
- 2020-07-16 CN CN202010686771.6A patent/CN111730741A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113119293A (en) * | 2021-03-03 | 2021-07-16 | 福建省漳州建华陶瓷有限公司 | Anti-cracking wear-resistant tile drying system and preparation method thereof |
| CN113119293B (en) * | 2021-03-03 | 2022-08-16 | 福建省漳州建华陶瓷有限公司 | Anti-cracking wear-resistant tile drying system and preparation method thereof |
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