CN115738486B - Ceramic blank waste recovery system - Google Patents
Ceramic blank waste recovery system Download PDFInfo
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- CN115738486B CN115738486B CN202310033453.3A CN202310033453A CN115738486B CN 115738486 B CN115738486 B CN 115738486B CN 202310033453 A CN202310033453 A CN 202310033453A CN 115738486 B CN115738486 B CN 115738486B
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Abstract
The invention relates to the field of ceramic production and processing, and provides a ceramic blank waste recovery system which is mainly used for recovering ceramic blanks and comprises a multistage sedimentation tank, wherein three filter frames which are arranged up and down are arranged in the multistage sedimentation tank, filter sheets are arranged on the filter frames, the multistage sedimentation tank is divided into a plurality of sedimentation chambers by the filter frames, the top of the multistage sedimentation tank is provided with a water inlet valve, the bottom of the multistage sedimentation tank is provided with a water outlet valve, each filter frame is respectively connected with a discharge mechanism, and the three discharge mechanisms are respectively connected with a first recovery mechanism, a second recovery mechanism and a third recovery mechanism from top to bottom in sequence. According to the invention, ceramic blanks with different sizes can be treated and recovered respectively through the first recovery mechanism, the second recovery mechanism and the third recovery mechanism, so that substances doped in the ceramic blanks can be removed, the quality of the recovered ceramic blanks is improved, and the technical problem that the secondary use of the ceramic blanks is affected due to low quality of the recovered ceramic blanks is solved.
Description
Technical Field
The invention relates to the field of ceramic production and processing, in particular to a ceramic blank waste recycling system.
Background
The ceramic body is the main body of the ceramic article, and its properties determine the properties and applications of the ceramic article. The preparation of the billets is of outstanding importance in the ceramic production process. In the ceramic production and processing process, a large amount of ceramic mud exists in the discharged wastewater, if the wastewater is not recycled, the wastewater is wasted, and the environment is easily polluted. In the existing ceramic production setting, the blanks are recycled, however, the larger solid blanks are recycled only through simple filtration, the smaller granular ceramic mud is remained in the waste water and is difficult to filter and recycle, and meanwhile, metals or other substances, even harmful substances, are easily remained in the recycled blanks, so that the secondary use of the blanks is influenced, and the recycling efficiency is low.
Chinese patent application No.: 202021763631.6 discloses a ceramic blank residue recovery device. Comprising the following steps: a case; the feeding hopper is fixedly arranged at one side of the box body; the first motor is fixedly arranged at the top of the box body; the first conical gear is fixedly arranged on an output shaft of the first motor; the screw is rotatably arranged on one side of the box body; the second bevel gear is fixedly arranged at the top end of the screw rod, and the first bevel gear is meshed with the second bevel gear; the driving arm is sleeved on the screw rod in a threaded manner, and one end of the driving arm extends into the box body; the second motor is fixedly arranged at the bottom of the driving arm. The ceramic blank recovered by the device may contain substances such as iron, zinc, lead, cadmium and the like, and the quality of the recovered ceramic blank is low.
Disclosure of Invention
Accordingly, in view of the above-mentioned problems, the present invention provides a ceramic green waste recycling system. The method solves the technical problems that the quality of the recycled ceramic blank is low and the secondary use of the ceramic blank is affected.
In order to achieve the above purpose, the present invention adopts the following technical scheme:
the utility model provides a ceramic blank waste recovery system, its mainly used is to the recovery of ceramic blank, including multistage sedimentation tank, be equipped with three filter frames that set up from top to bottom in the multistage sedimentation tank, be equipped with the filter piece on the filter frame, the filtration pore of filter piece below is less than the filtration pore of filter piece above, and the filter piece below is the filter membrane, the filter frame divide into a plurality of settling chambers with multistage sedimentation tank, multistage sedimentation tank top is equipped with the water intaking valve, multistage sedimentation tank bottom is equipped with the outlet valve, every filter frame is connected a bin outlet mechanism respectively, and first recovery mechanism, second recovery mechanism and third recovery mechanism are connected gradually from top to bottom respectively to three bin outlet mechanisms;
the first recovery mechanism comprises a first cleaning chamber, a first drying chamber, a crushing chamber, a first metal removing chamber, a first conveying chamber and a first recovery chamber which are sequentially connected;
the first cleaning chamber comprises a water spray head arranged in the first cleaning chamber and a water spray device connected with the water spray head, a first discharge valve is arranged between the first cleaning chamber and the first drying chamber, and a first drain valve is arranged in the first cleaning chamber; a drying device is arranged in the first drying chamber, and a second discharge valve is arranged between the first drying chamber and the crushing chamber;
the crushing chamber is internally provided with two crushing rollers and a crushing motor for driving the crushing rollers to rotate, the first metal removing chamber comprises at least one electromagnetic filter screen plate, the electromagnetic filter screen plate is connected with a first power supply, the first metal removing chamber is internally provided with two third discharge valves, one of the third discharge valves is connected with the first conveying chamber, and the other third discharge valve is connected with the metal collecting chamber;
the second recovery mechanism comprises a second cleaning chamber, a second drying chamber, a second metal removing chamber, a second conveying chamber and a second recovery chamber which are sequentially connected;
the third recovery mechanism comprises two reaction tanks, a third cleaning chamber, a third drying chamber, a third metal removing chamber, a third conveying chamber and a third recovery chamber which are sequentially connected;
the second cleaning chamber, the third cleaning chamber and the first cleaning chamber have the same structure, and the second drying chamber, the third drying chamber and the first drying chamber have the same structure; the second metal removing chamber and the third metal removing chamber have the same structure as the first metal removing chamber; the third conveying chamber, the second conveying chamber and the first conveying chamber have the same structure;
at least one discharging box is respectively connected to the two reaction tanks, the two reaction tanks are connected through a conveying mechanism, an exhaust valve is arranged on each reaction tank, and one reaction tank is connected with a third cleaning chamber through a second exhaust valve.
Further:
the first conveying chamber is of a cylindrical structure, auger blades are arranged in the first conveying chamber, and an auger motor for driving the auger blades to rotate is arranged in the first conveying chamber.
Still include a support body, first delivery chamber rotationally locates on the support body, be equipped with the pivoted rotating electrical machines of drive first delivery chamber on the support body, first delivery chamber inner wall is equipped with the electromagnetic layer, the second power is connected to the electromagnetic layer, first delivery chamber both ends are equipped with feed inlet and discharge gate respectively, the feed inlet passes through the bellows and connects in the third relief valve, the discharge gate passes through the bellows and connects in first recovery room, be equipped with the fourth relief valve on the first delivery chamber, the fourth relief valve passes through the bellows and connects in the metal collecting chamber, there is the clearance between auger blade and the electromagnetic layer.
The stirring mechanism is arranged in the reaction tank and comprises a stirring rod rotatably arranged in the reaction tank, a plurality of stirring blades arranged on the stirring rod and a rotating motor for driving the stirring rod to rotate.
The exhaust valve is connected with the first exhaust gas treatment device.
The first drying chamber, the second drying chamber and the third drying chamber are connected with a second waste gas treatment device.
The first drain valve of the first cleaning chamber, the second cleaning chamber and the third cleaning chamber is connected with the wastewater treatment device.
The filter frame is of a conical structure, and the lower end of the filter frame is connected with a discharge mechanism.
The multistage sedimentation tank is provided with a circulating mechanism, and the circulating mechanism comprises circulating valves arranged at the top and the bottom of the multistage sedimentation tank, a circulating pipe connected with the circulating valves and a circulating pump arranged on the circulating pipe.
The discharging mechanism is a suction pump.
By adopting the technical scheme, the invention has the beneficial effects that:
the multistage sedimentation tank can filter blocky ceramic blanks, sandy ceramic blanks and mud-shaped ceramic blanks from top to bottom, and then the ceramic blanks are respectively discharged into a first recovery mechanism, a second recovery mechanism and a third recovery mechanism through a discharge mechanism for treatment, the first cleaning chamber has the cleaning function, the ceramic blanks are cleaned to remove ions or other substances adhered to the ceramic blanks, the first drying chamber is used for drying the ceramic blanks, the larger ceramic blanks are crushed into small blocks or particles after being dried, an electromagnetic filter screen is electrified to adsorb metal substances mixed in the ceramic blanks, the metal substances in the ceramic blanks are removed, and after entering into a first conveying chamber from one third discharge valve, the metal substances enter into a metal collecting chamber from the other third discharge valve; the ceramic blanks conveyed to the second recovery mechanism are sandy ceramic blanks, so that a crusher is not required to be arranged for crushing, and the sandy ceramic blanks are recovered by adopting the method; the ceramic blank conveyed to the third recovery mechanism is mud-shaped and contains other small-particle substances, the substances left on the ceramic blank need to be reacted through the reaction tanks, two reaction tanks are adopted, the ceramic blank is discharged into one of the reaction tanks for reaction after being reacted, the reacted substances are dissolved in water or form gas to be discharged, the ceramic blank is alternately and repeatedly conveyed in the two reaction tanks, the substances of the ceramic blank can be respectively treated, more reaction tanks are not needed, the equipment space is saved, the equipment cost is reduced, and meanwhile, the efficiency is also provided; the ceramic blanks with different sizes can be recovered from the first recovery mechanism, the second recovery mechanism and the third recovery mechanism, other substances on the ceramic blanks can be cleaned, the quality of the recovered ceramic blanks is high, and the secondary use of the ceramic blanks is improved; further, the first conveying chamber adopts auger blades, so that ceramic blanks can be stirred; further, after the electromagnetic layer on the inner wall of the first conveying chamber is electrified, part of a small amount of metal is possibly mixed in the ceramic blank and is not adsorbed by the first metal removing chamber, the electromagnetic layer can adsorb and fix the ceramic blank under the stirring and conveying of the auger blade, when the ceramic blank is conveyed to the first recycling chamber, the rotating motor drives the first conveying chamber to rotate, so that the first conveying chamber is obliquely arranged, the second power supply is powered off, the fourth discharge valve is opened, and the metal adsorbed by the electromagnetic layer falls into the metal collecting chamber from the fourth discharge valve under the action of gravity; furthermore, the stirring mechanism can improve the reaction speed; furthermore, the first waste gas treatment device can treat the gas generated by the reaction, in particular to recycle the gas such as methane; furthermore, the filter frame is conical, so that the filter area is increased; further, circulation mechanism can filter waste water many times, because less particulate matter or clay embryo material is likely to mix the clay embryo material of top, with sewage multiple times circulation, can separate the clay embryo material of equidimension not and other substances to corresponding settling chamber, prevent that little granular other substances from leaving in the settling chamber of top for little granular other substances are all on the filter frame of below, make all little granular other substances can be handled through the reaction chamber, improve the recovery quality of clay.
Drawings
Fig. 1 is a schematic diagram of the structure of the present invention.
Fig. 2 is a schematic structural view of a multistage sedimentation tank.
Fig. 3 is a schematic view of the first recovery mechanism.
Fig. 4 is a schematic structural view of the first transfer chamber.
Fig. 5 is a schematic structural view of another state of the first conveyance chamber.
Fig. 6 is a schematic view of the second recovery mechanism.
Fig. 7 is a schematic view of the third recovery mechanism.
FIG. 8 is a schematic structural view of the reaction cell.
FIG. 9 is a schematic view of another construction of the reaction cell.
Fig. 10 is a schematic structural view of fig. 9 reflecting another state.
Detailed Description
The invention will now be further described with reference to the drawings and detailed description.
Referring to fig. 1 to 10, the present embodiment provides a ceramic blank waste recycling system, which is mainly used for recycling ceramic blanks, and includes a multi-stage sedimentation tank 1, wherein three filter frames 11 are arranged up and down in the multi-stage sedimentation tank 1, the filter frames 11 are in a conical structure, filter discs 12 are arranged on the filter frames 11, the filter holes of the filter discs 12 below are smaller than the filter holes of the filter discs 12 above, the filter discs 12 below are water filtering films, the filter frames 11 divide the multi-stage sedimentation tank 1 into a plurality of sedimentation chambers 10, the top of the multi-stage sedimentation tank 1 is provided with a water inlet valve 13, the bottom of the multi-stage sedimentation tank 1 is provided with a water outlet valve 14, the water outlet valve 14 is connected with a wastewater treatment device 2, the lower ends of the filter frames 11 are connected with a discharge mechanism 3, and the three discharge mechanisms 3 are sequentially connected with a first recycling mechanism 4, a second recycling mechanism 5 and a third recycling mechanism 6 from top to bottom respectively; the multistage sedimentation tank 1 is provided with a circulating mechanism which comprises circulating valves 15 arranged at the top and the bottom of the multistage sedimentation tank 1, a circulating pipe 16 connected with the circulating valves 15 and a circulating pump 17 arranged on the circulating pipe 16.
The first recovery mechanism 4 includes a first cleaning chamber 41, a first drying chamber 42, a crushing chamber 43, a first metal removing chamber 44, a first conveying chamber 45, and a first recovery chamber 46, which are connected in this order.
The first cleaning chamber 41 comprises a water spray head 411 arranged in the first cleaning chamber 41 and a water spray device 412 connected with the water spray head 411, a first discharge valve 413 is arranged between the first cleaning chamber 41 and the first drying chamber 42, and a first drain valve 414 is arranged in the first cleaning chamber 41; a drying device 421 is arranged in the first drying chamber 42, and a second discharge valve 422 is arranged between the first drying chamber 42 and the crushing chamber 43.
The crushing chamber 43 is provided with two crushing rollers 431 and a crushing motor 432 for driving the crushing rollers 431 to rotate, the first metal removing chamber 44 comprises two electromagnetic filter screen plates 441, the electromagnetic filter screen plates 441 are connected with a first power source 442, the first metal removing chamber 44 is provided with two third discharge valves 443, one of the third discharge valves 443 is connected with the first conveying chamber 45, and the other third discharge valve 443 is connected with the metal collecting chamber 47.
The first conveying chamber 45 has a cylindrical structure, an auger blade 451 is provided in the first conveying chamber 45, and an auger motor 452 for driving the auger blade 451 to rotate is provided in the first conveying chamber 45. The first conveying chamber 45 is rotatably arranged on the frame 453, a rotating motor 454 for driving the first conveying chamber 45 to rotate is arranged on the frame 453, an electromagnetic layer 455 is arranged on the inner wall of the first conveying chamber 45, the electromagnetic layer 455 is connected with a second power supply 456, a feed inlet 457 and a discharge outlet 458 are respectively arranged at two ends of the first conveying chamber 45, the feed inlet 457 is connected with a third discharge valve 443 through a corrugated pipe 459, the discharge outlet 458 is connected with the first recovery chamber 46 through the corrugated pipe 459, a fourth discharge valve 450 is arranged on the first conveying chamber 45, the fourth discharge valve 450 is connected with the metal collection chamber 47 through the corrugated pipe 459, and a gap exists between the auger blade 451 and the electromagnetic layer 455.
The second recovery mechanism 5 includes a second cleaning chamber 51, a second drying chamber 52, a second metal removing chamber 53, a second conveying chamber 54, and a second recovery chamber 55, which are connected in this order.
The third recovery mechanism 6 includes two reaction tanks 61, a third cleaning chamber 62, a third drying chamber 63, a third metal removing chamber 64, a third conveying chamber 65, and a third recovery chamber 66, which are sequentially connected.
The two reaction tanks 61 are respectively connected with a plurality of discharging boxes 611, the two reaction tanks 61 are connected through a conveying mechanism 612, the two reaction tanks 61 are provided with exhaust valves 613, the exhaust valves 613 are connected with a first waste gas treatment device 614, and one reaction tank 61 is connected with a third cleaning chamber 62 through a second drain valve 615. The stirring mechanism 616 is provided in the reaction tank 61, and the stirring mechanism 616 includes a stirring rod rotatably provided in the reaction tank 61, a plurality of stirring blades provided on the stirring rod, and a rotating motor for driving the stirring rod to rotate.
The second washing chamber 51 and the third washing chamber 62 have the same structure as the first washing chamber 41, the first drain valves 414 of the first washing chamber 41, the second washing chamber 51 and the third washing chamber 62 are connected with the wastewater treatment device 2, the second drying chamber 52 and the third drying chamber 63 have the same structure as the first drying chamber 42, and the first drying chamber 42, the second drying chamber 52 and the third drying chamber 63 are connected with the second wastewater treatment device 7; the second metal removing chamber 53 and the third metal removing chamber 64 have the same structure as the first metal removing chamber 44; the third conveying chamber 65, the second conveying chamber 54, and the first conveying chamber 45 are identical in structure.
The filter 12 may be a filtering fabric, a filtering mesh or other filtering material, and the filtering film can filter water, but cannot filter ceramic mud, which is a well-known material and structure and will not be described herein.
The drying device 421 may be an electric heating rod, an electric heating tube, a fan or other drying devices, which are well known devices and will not be described herein.
The crushing roller 431 has a known structure and will not be described in detail herein.
The electromagnetic filter screen 441 may have a mesh structure, and the number of the mesh structures may be one, two or even more, or may have other structures, and the electromagnetic filter screen 441 may be powered to generate electromagnetic force to adsorb metal, which is a well-known material and will not be described herein.
The above-mentioned discharging tank 611 is capable of adding reactants into the reaction tank 61, and is of a well-known structure, and the discharging tank 611 is usually added with a liquid, and is specifically set according to circumstances.
The first, second and third conveying chambers 45, 54, 65 may be provided by a conveyor belt, a conveyor passage or other structures, as the case may be, instead of the auger blade 451.
The stirring mechanism 616 may not be provided in the reaction tank 61, and the reaction in the reaction tank 61 may be slow, and the stirring mechanism may be provided according to circumstances.
The filter frame 11 may also have a rectangular, hemispherical or other structure, as the case may be.
The circulating mechanism can also adopt other structures, and the circulating mechanism is not required to be arranged, and is particularly arranged according to the situation.
The discharging mechanism 3 and the conveying mechanism 612 may be suction pumps or other devices, which are well known devices and will not be described herein.
The first exhaust gas treatment device 614 and the second exhaust gas treatment device 7 can collect exhaust gas, and recycle the exhaust gas, which is a well-known device and will not be described herein; the first exhaust gas treatment device 614 and the second exhaust gas treatment device 7 may not be provided, and the gas may be directly discharged, as the case may be.
The above-mentioned waste water treatment device 2 is a device for treating waste water, and chinese patent application number may be adopted: 201310238692.9 discloses a waste heat gas sewage recycling treatment system in the ceramic industry, and a part of devices mentioned in the patent; chinese patent application number may also be used: 200910162302.8, other ceramic wastewater treatment devices can be adopted, which are known devices and are not described herein.
Referring to fig. 9 and 10, the top opening of the reaction tank 61 is upward, a telescopic corrugated cover 617 is provided on the top of the reaction tank 61, a telescopic mechanism 6170 for driving the corrugated cover 617 to move is provided on the reaction tank 61, the corrugated cover 617 includes a corrugated portion 6171 provided on the top of the reaction tank 61, a cover plate 6172 provided on the top of the corrugated portion 6171, four guide rods 618 are provided on the reaction tank 61, a guide sleeve 619 for sleeving the guide rods 618 is provided on the cover plate 6172, and an air pressure sensor 610 is provided in the reaction tank 61.
The air pressure sensor 610 can detect whether the air pressure in the reaction tank 61 is changed, and detect whether the air is generated in the reaction tank 61, if the air is not generated, the reaction is complete, and the discharging box 611 does not need to continuously discharge reactants, so that reactants can be saved, the reactants are prevented from polluting water, and the quality of sewage treatment is improved.
When the air pressure in the reaction tank 61 is large, the telescopic mechanism 6170 drives the cover plate 6172 to move upwards, the volume of the corrugated cover 617 is increased, so that the air pressure in the reaction tank 61 is reduced, and when the air in the reaction tank 61 needs to be discharged, the telescopic mechanism 6170 can drive the cover plate 6172 to descend, the volume of the corrugated cover 617 is reduced, and the discharge of the air is facilitated.
The telescopic mechanism 6170 can be an air cylinder, an oil cylinder, a linear motor or other linear motion mechanisms.
The working mode of the invention is as follows:
ceramic wastewater enters the multistage sedimentation tank 1 through a water inlet valve 13, is filtered by three filter plates 12, larger blocky ceramic blanks remain on the uppermost filter plate 12, sandy ceramic blanks remain on the middle filter plate 12, mud ceramic blanks remain on the lowermost filter plate 12, and are respectively discharged into the first recovery mechanism 4, the second recovery mechanism 5 and the third recovery mechanism 6 for treatment through a discharge mechanism 3; the first cleaning chamber 41 cleans the ceramic blank to remove ions or other substances adhered to the ceramic blank, the cleaned water is discharged into the waste water treatment device 2, the ceramic blank is discharged into the first drying chamber 42 for drying, in the drying process, gas is discharged into the second waste gas treatment device 7, after the drying is finished, the ceramic blank enters the crushing chamber 43, the ceramic blank is crushed into small blocks or particles, the ceramic blank enters the first metal removal chamber 44, the electromagnetic filter screen 441 is electrified and can adsorb metal substances mixed in the ceramic blank, the metal substances in the ceramic blank are removed, the ceramic blank enters the first conveying chamber 45 from one of the third discharge valves 443, the metal substances in the first metal removal chamber 44 enter the metal collecting chamber 47 from the other third discharge valve 443, a part of small amount of metal possibly is mixed in the ceramic blank, the ceramic blank is not adsorbed by the first metal removal chamber 44, the ceramic blank is conveyed under the stirring of the auger blade 451, the electromagnetic layer 455 on the inner wall of the first conveying chamber 45 is electrified, the auger blade 45 rotates to clamp the ceramic blank 45 in the first conveying chamber 45, the ceramic blank is conveyed by the electromagnetic motor 45, and the electromagnetic valve 455 is driven to rotate, and the metal substances in the fourth conveying chamber 45 are fully adsorbed by the electromagnetic valve 450, and the metal substances can be recovered by the electromagnetic valve 450 when the electromagnetic valve 45 rotates, and the metal substances in the ceramic blank is fully rotates, and the ceramic blank 45 is adsorbed in the fourth conveying chamber 45; the second recovery mechanism 5 is similar to the first recovery mechanism 4 in treatment mode, except that the sand-shaped ceramic blanks of the second recovery mechanism 5 do not need to be crushed; the third recovery mechanism 6 is similar to the first recovery mechanism 4 in treatment mode, the ceramic blank of the third recovery mechanism 6 is not required to be crushed, the ceramic blank of the third recovery mechanism 6 is mud-shaped and contains other substances in small particles, the substances left on the ceramic blank need to be reacted through the reaction tanks 61, the two reaction tanks 61 are adopted, the ceramic blank is discharged into one reaction tank 61 to react after being reacted in the other reaction tank 61, the reacted substances are dissolved in water or form gas to be discharged, the ceramic blank is alternately and repeatedly conveyed in the two reaction tanks 61, and the substances of the ceramic blank can be respectively treated.
While the invention has been particularly shown and described with reference to a preferred embodiment, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims.
Claims (6)
1. The utility model provides a ceramic embryo waste recovery system, its mainly used is retrieved ceramic embryo, its characterized in that: the device comprises a multistage sedimentation tank, wherein three filter frames which are arranged up and down are arranged in the multistage sedimentation tank, filter sheets are arranged on the filter frames, filter holes of filter sheets below are smaller than those of filter sheets above, filter sheets below are filter films, the filter frames divide the multistage sedimentation tank into a plurality of sedimentation chambers, the top of the multistage sedimentation tank is provided with a water inlet valve, the bottom of the multistage sedimentation tank is provided with a water outlet valve, each filter frame is respectively connected with a discharge mechanism, and the three discharge mechanisms are respectively connected with a first recovery mechanism, a second recovery mechanism and a third recovery mechanism from top to bottom in sequence;
the first recovery mechanism comprises a first cleaning chamber, a first drying chamber, a crushing chamber, a first metal removing chamber, a first conveying chamber and a first recovery chamber which are sequentially connected;
the first cleaning chamber comprises a water spray head arranged in the first cleaning chamber and a water spray device connected with the water spray head, a first discharge valve is arranged between the first cleaning chamber and the first drying chamber, and a first drain valve is arranged in the first cleaning chamber; a drying device is arranged in the first drying chamber, and a second discharge valve is arranged between the first drying chamber and the crushing chamber;
the crushing chamber is internally provided with two crushing rollers and a crushing motor for driving the crushing rollers to rotate, the first metal removing chamber comprises at least one electromagnetic filter screen plate, the electromagnetic filter screen plate is connected with a first power supply, the first metal removing chamber is internally provided with two third discharge valves, one of the third discharge valves is connected with the first conveying chamber, and the other third discharge valve is connected with the metal collecting chamber;
the first conveying chamber is of a cylindrical structure, auger blades are arranged in the first conveying chamber, an auger motor for driving the auger blades to rotate is arranged in the first conveying chamber, the first conveying chamber is further arranged on the frame in a rotatable mode, a rotating motor for driving the first conveying chamber to rotate is arranged on the frame, an electromagnetic layer is arranged on the inner wall of the first conveying chamber, the electromagnetic layer is connected with a second power supply, a feeding port and a discharging port are respectively arranged at two ends of the first conveying chamber, the feeding port is connected with a third discharge valve through a corrugated pipe, the discharging port is connected with a first recovery chamber through a corrugated pipe, a fourth discharge valve is arranged on the first conveying chamber and is connected with a metal collection chamber through a corrugated pipe, and a gap exists between the auger blades and the electromagnetic layer;
the second recovery mechanism comprises a second cleaning chamber, a second drying chamber, a second metal removing chamber, a second conveying chamber and a second recovery chamber which are sequentially connected;
the third recovery mechanism comprises two reaction tanks, a third cleaning chamber, a third drying chamber, a third metal removing chamber, a third conveying chamber and a third recovery chamber which are sequentially connected;
the second cleaning chamber, the third cleaning chamber and the first cleaning chamber have the same structure, and the second drying chamber, the third drying chamber and the first drying chamber have the same structure; the second metal removing chamber and the third metal removing chamber have the same structure as the first metal removing chamber; the third conveying chamber, the second conveying chamber and the first conveying chamber have the same structure;
the two reaction tanks are respectively connected with at least one blanking box, the two reaction tanks are connected through a conveying mechanism, the two reaction tanks are provided with exhaust valves, one reaction tank is connected with a third cleaning chamber through a second exhaust valve, the top opening of the reaction tank is upward, the top of the reaction tank is provided with a telescopic corrugated cover, the reaction tank is provided with a telescopic mechanism for driving the corrugated cover to move, the corrugated cover comprises a corrugated part arranged at the top of the reaction tank and a cover plate arranged at the top of the corrugated part, four guide rods are arranged on the reaction tank, the cover plate is provided with a guide sleeve for sleeving the guide rods, the reaction tank is internally provided with an air pressure sensor, the air pressure sensor can detect whether the air pressure in the reaction tank is changed or not, if the air pressure in the reaction tank is not generated, the reaction is completely described, the blanking box does not need to continuously lower reactants, when the air pressure in the reaction tank is large, the telescopic mechanism drives the cover plate to move upward, the air pressure in the reaction tank is reduced, when the air in the reaction tank needs to be discharged, the telescopic mechanism can drive the cover plate to descend, the air pressure in the reaction tank is reduced, and the air is favorable for discharging of the air.
2. A ceramic green waste recycling system according to claim 1, wherein: the stirring mechanism is arranged in the reaction tank and comprises a stirring rod rotatably arranged in the reaction tank, a plurality of stirring blades arranged on the stirring rod and a rotating motor for driving the stirring rod to rotate.
3. A ceramic green waste recycling system according to claim 1, wherein: the exhaust valve is connected with the first exhaust gas treatment device.
4. A ceramic green waste recycling system according to claim 1, wherein: the filter frame is of a conical structure, and the lower end of the filter frame is connected with a discharge mechanism.
5. A ceramic green waste recycling system according to claim 1, wherein: the multistage sedimentation tank is provided with a circulating mechanism, and the circulating mechanism comprises circulating valves arranged at the top and the bottom of the multistage sedimentation tank, a circulating pipe connected with the circulating valves and a circulating pump arranged on the circulating pipe.
6. A ceramic green waste recycling system according to claim 1, wherein: the discharging mechanism is a suction pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310033453.3A CN115738486B (en) | 2023-01-10 | 2023-01-10 | Ceramic blank waste recovery system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310033453.3A CN115738486B (en) | 2023-01-10 | 2023-01-10 | Ceramic blank waste recovery system |
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| CN115738486A CN115738486A (en) | 2023-03-07 |
| CN115738486B true CN115738486B (en) | 2023-05-02 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2005034822A (en) * | 2003-07-17 | 2005-02-10 | Koji Sakaguchi | Metal separation/recovery technique from solution by oxidation reduction process |
| CN101942562A (en) * | 2010-04-26 | 2011-01-12 | 张夫道 | Harmless treatment technology of main metal tailings |
| CN207103162U (en) * | 2017-04-28 | 2018-03-16 | 贵州欧玛陶瓷有限责任公司 | Ceramic waste residue is classified retracting device and ceramic waste residue classification recovery system |
| CN107932742B (en) * | 2017-11-17 | 2020-07-14 | 广东恒业水泥制品有限公司 | Concrete manufacturing equipment and using method thereof |
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