A solid-liquid separation device for ternary precursor production
By using a filter pressing reinforcement mechanism and scraping and scraping technology combined with an annular electromagnet and a pumping negative pressure tube in the production equipment of ternary precursors, the problem of insufficient solid-liquid separation efficiency and material contact uniformity in existing equipment is solved. It achieves efficient solid-liquid separation and drying effects.
Patent Information
- Application Number
- CN202411324570.6
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2024-09-23
- Publication Date
- 2024-12-13
- Estimated Expiration
- 2044-09-23
AI Technical Summary
The existing solid-liquid separation equipment for the production of ternary precursors relies on a separate pressurization method in the filter press to achieve limited solid-liquid separation efficiency, and the contact uniformity between materials and heating disks in the disc dryer is insufficient, which affects solid-liquid separation. Effect and efficiency.
A device including a filter press and a disc dryer is designed. The filter press adopts a filter press reinforcement mechanism combining an annular electromagnet and a pumping negative pressure tube to reduce the filter cloth spacing and pump the negative pressure to accelerate the discharge of liquid. The disc dryer breaks the material through the scraper mechanism and magnet plate drives the scraper to improve the contact uniformity between the material and the heating plate.
It significantly improves the solid-liquid separation efficiency and material drying effect, improves the discharge efficiency of liquid materials through the dual methods of extrusion and extraction of negative pressure, and improves the heating uniformity by breaking the materials, enhancing the overall performance of solid-liquid separation equipment .
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Figure CN118846607B_ABST
Abstract
Description
Technical Field
[0001] The invention relates to the technical field of solid-liquid separation equipment for ternary precursor production, and in particular to solid-liquid separation equipment for ternary precursor production. Background Art
[0002] The production process of ternary precursors requires solid-liquid separation treatment. Existing solid-liquid separation equipment for ternary precursor production generally includes filter presses and disc dryers.
[0003] The liquid material in the material is filtered out by a filter press, and then the material after the initial solid-liquid separation is dried by a disc dryer to further remove the liquid material in the material. The filter press and disc dryer used in the existing solid-liquid separation equipment for ternary precursor production are both existing traditional equipment. Among them, the filter press basically relies on a single pressurization method to squeeze the filter cake, resulting in a limited effect on improving its solid-liquid separation efficiency; while the disc dryer has the problem of insufficient contact uniformity between the material and the heating plate, which affects the solid-liquid separation effect and solid-liquid separation efficiency of the material.
[0004] Therefore, the research purpose of the present invention is to design a solid-liquid separation equipment for ternary precursor production that can not only effectively improve the filtration effect and filtration efficiency of the material, but also improve the uniformity of contact between the material and the heating plate during drying, thereby effectively improving the solid-liquid separation effect and solid-liquid separation efficiency of the material. Summary of the invention
[0005] In view of the technical problems existing in the above-mentioned prior art, the present invention provides a solid-liquid separation device for the production of a ternary precursor, which can effectively solve the technical problems existing in the above-mentioned prior art.
[0006] The technical solution of the present invention is:
[0007] A solid-liquid separation device for ternary precursor production, comprising a filter press and a disc dryer, wherein the filter press comprises:
[0008] A frame, wherein a corresponding guide bracket is arranged on the upper part of the frame, and a guide hopper with a feed port facing the guide bracket is fixedly installed on the frame at the lower side of the guide bracket;
[0009] A plurality of filter plates are laterally movably mounted on the guide bracket, and corresponding accommodating cavities are respectively provided on opposite sides of two adjacent filter plates, and a material guide pipe located in the middle of the accommodating cavity is respectively penetrated through the middle of the filter plate, and a corresponding filter cloth is respectively fixedly connected to one side of the filter plate with the accommodating cavity, and the middle of the filter cloth is respectively sealed and connected to the material guide pipe;
[0010] The clamping mechanism comprises a push hydraulic cylinder fixedly mounted on one end of the guide bracket. When the piston rod of the push hydraulic cylinder is extended, the plurality of filter plates are closed and connected with each other under the pushing action of the push hydraulic cylinder. After the filter plates are closed and connected with each other, two adjacent material guide pipes are respectively arranged at intervals.
[0011] A feed pipe is fixedly mounted on the other end of the guide bracket, the feed end of the feed pipe is pumped to an external material source, and the discharge end of the feed pipe is connected to a guide pipe of a filter plate at the end, so as to pump the material into between the filter cloths of two adjacent filter plates;
[0012] The filter press strengthening mechanism comprises a plurality of annular electromagnets and a plurality of negative pressure extraction pipes, wherein the annular electromagnets are respectively sleeved on the periphery of the corresponding material guide pipes and fixedly connected to the inner side of the corresponding filter cloths, and the feed ends of the negative pressure extraction pipes are respectively connected to the filter plates on the inner side of the filter cloths for vacuumizing the accommodating chambers on the filter plates, and the plurality of negative pressure extraction pipes are connected in parallel to the corresponding negative pressure extraction mechanisms; when the material enters between the filter cloths of two adjacent filter plates, the annular electromagnets are energized, and the spacing between the filter cloths of the two adjacent filter plates is reduced under the action of the adsorption force, so as to squeeze and filter out the liquid material in the filter cake, and at the same time, the negative pressure extraction mechanism starts to extract negative pressure to accelerate the extraction and discharge of the liquid material in the filter cake;
[0013] The feed end of the disc dryer is connected to the discharge end of the guide hopper of the filter press through a corresponding material transmission mechanism, so as to heat and dry the material after the filter press.
[0014] The disc dryer comprises:
[0015] A fixed tank body, wherein a corresponding feed hopper is arranged on the top of the fixed tank body, and a discharge pipe is arranged on the bottom of the fixed tank body; a first heating plate and a second heating plate are arranged alternately in height in the fixed tank body, and corresponding guide holes are arranged in the middle of the first heating plate and the second heating plate respectively, and the periphery of the second heating plate is extended to the outside of the first heating plate, and the guide hole diameter of the first heating plate is smaller than the guide hole diameter of the second heating plate;
[0016] A scraper drive mechanism, comprising a drive shaft installed through the guide holes of the first heating plate and the second heating plate, wherein the drive shaft is driven by a corresponding drive motor;
[0017] The first scraping mechanism comprises first fixed rods fixed to the driving shaft on the upper side of the first heating disk in an annular array, a plurality of corresponding first fixed shafts are fixedly connected side by side downward to the first fixed rods, first scrapers for scraping the material on the first heating disk outward are rotatably mounted on the first fixed shafts, and the first scrapers and the first fixed shafts are limited by corresponding first limit springs;
[0018] The second scraping mechanism comprises a second fixed rod member fixed to the driving shaft on the upper side of the second heating disk in an annular array, a plurality of corresponding second fixed shaft members are fixedly connected side by side downward to the second fixed rod member, a second scraper for scraping the material on the second heating disk inward is rotatably mounted on the second fixed shaft member, and the second scraper and the second fixed shaft member are limited by corresponding second limit springs;
[0019] The scraper driving mechanism includes a plurality of circles of magnet sheets which are fixedly connected to the upper sides of the first heating plate and the second heating plate in an annular array at intervals, and the magnet sheets are respectively arranged corresponding to the first scraper and the second scraper. When the first scraper and the second scraper rotate and pass the position where the magnet sheets are located, the first scraper and the second scraper are adsorbed, and the first limit spring and the second limit spring are compressed. When the compression force of the first limit spring and the second limit spring is greater than the adsorption force of the magnet sheet, the first scraper and the second scraper leave the position where the magnet sheet is located, and swing under the elastic force of the first limit spring and the second limit spring, so as to break up the material when scraping it.
[0020] A corresponding lower hopper is fixedly installed on the lower side of the discharge end of the guide hopper, and the top of the lower hopper is folded inward in an inverted L shape and is provided with a corresponding cover, and the discharge end of the guide hopper extends through the cover; a screening plate arranged in a ring shape is rotatably installed on the bottom side of the cover, and a number of corresponding screening holes are evenly distributed on the screening plate, and a plurality of corresponding crushing ridges are fixedly connected to the top surface of the screening plate at intervals, and the screening plate is driven by a rotating drive motor fixedly installed on the guide hopper.
[0021] A plurality of material baffle plates are arranged in the cover at intervals, and the bottoms thereof are arranged at intervals from the crushing material convex edge.
[0022] The screening plate is provided with a plurality of fixed connecting rods fixedly connected to the output shaft end of the rotary drive motor at intervals inwardly.
[0023] The negative pressure pumping mechanism comprises a negative pressure pumping container, a plurality of negative pressure pumping tubes are connected in parallel to the negative pressure pumping container, and a top pump of the negative pressure pumping container is connected to a corresponding vacuum pump.
[0024] A corresponding push plate is fixedly connected to the piston rod end of the push hydraulic cylinder. When the piston rod of the push hydraulic cylinder is extended, the push plate pushes the plurality of filter plates to form a closed connection with each other.
[0025] The side of the annular electromagnet on the filter plate at the end that is not connected to the filter cloth is respectively provided with a corresponding plug-in shaft, and the plug-in shaft can be movably plugged into the filter plate at the end.
[0026] The annular electromagnets on both sides of the filter plate located in the middle are respectively fixedly connected with a guide sleeve and a guide shaft which are movably connected to each other on one side which is not connected to the filter cloth.
[0027] The filter press also includes a washing mechanism, which includes a washing liquid distribution pipe connected between the filter cloths of two adjacent filter plates, and the washing liquid distribution pipe is connected to an external washing liquid source through a corresponding washing liquid inlet pipe pump.
[0028] Advantages of the present invention:
[0029] 1) The filter press strengthening mechanism of the present invention includes a plurality of annular electromagnets and a plurality of negative pressure pipes. The annular electromagnets are respectively sleeved on the periphery of the corresponding material guide pipe and fixedly connected to the inner side of the corresponding filter cloth. The feed ends of the negative pressure pipes are respectively connected to the filter plates on the inner side of the filter cloth, and are used to evacuate the accommodating chamber on the filter plate. After the material enters between the filter cloths of two adjacent filter plates, as the feed pressure increases, the liquid material in the material gradually enters the accommodating chamber of the filter plate through the filter cloth. When the feed pressure reaches the set value, the annular electromagnet is energized, and the distance between the filter cloths of the two adjacent filter plates is reduced under the action of the adsorption force, so as to squeeze and filter out the liquid material in the filter cake; at the same time, the negative pressure extraction mechanism starts to extract negative pressure to accelerate the extraction and discharge of the liquid material in the filter cake. Thereby, while squeezing the filter cake, it can effectively form a negative pressure on the filter cake, and discharge the liquid material in the filter cake in two directions, thereby greatly improving the solid-liquid separation efficiency.
[0030] 2) The present invention also has a lower hopper fixedly installed on the lower side of the discharge end of the guide hopper. The top of the lower hopper is folded inward in an inverted L shape and is provided with a corresponding cover. The discharge end of the guide hopper extends through the cover. When the filter cake after filtration is discharged into the guide hopper, the material is initially crushed by collision. The crushed material enters the cover of the lower hopper through the guide hopper. As the sieve plate rotates, the crushing convex edge drives the material through the baffle plate. Under the cooperation of the crushing convex and the baffle plate, the material is sheared and crushed. The crushed material is evenly screened out through the sieve holes on the sieve plate, thereby effectively and directly crushing the filter cake and outputting it, so that the material after solid-liquid separation can directly enter the corresponding drying equipment for drying processing, so as to enhance the use function of the present invention.
[0031] 3) The annular electromagnets on the filter plates at the ends of the present invention are provided with corresponding plug-in shafts on the sides that are not connected to the filter cloth, and the plug-in shafts are respectively movably plugged into the filter plates at the ends; and the annular electromagnets on both sides of the filter plates at the middle that are not connected to the filter cloth are respectively fixed with guide sleeves and guide shafts that form a movable docking with each other. The load of the annular electromagnets is transferred to the filter plates, thereby preventing the filter cloth from being overloaded due to the setting of the annular electromagnets, and ensuring the practical effect of the present invention.
[0032] 4) The present invention not only improves the structure of the first scraper mechanism and the second scraper mechanism, but also adds a scraper driving mechanism, which includes a plurality of circles of magnet sheets fixedly connected to the upper sides of the first heating disk and the second heating disk in an annular array at intervals. When the first scraper and the second scraper rotate and pass the position of the magnet sheets, the first scraper and the second scraper are adsorbed, and the first limit spring and the second limit spring are compressed. When the compression force of the first limit spring and the second limit spring is greater than the adsorption force of the magnet sheets, the first scraper and the second scraper leave the position of the magnet sheets and swing under the elastic force of the first limit spring and the second limit spring, so as to break up the materials when scraping them, thereby effectively breaking up the materials simultaneously during the process of shoveling and pushing the materials, so as to improve the contact uniformity and contact rate between the materials and the heating disk, thereby effectively improving the drying effect of the materials. BRIEF DESCRIPTION OF THE DRAWINGS
[0033] Figure 1 It is a schematic diagram of the structure of the present invention.
[0034] Figure 2 Schematic diagram of the structure of the filter press.
[0035] Figure 3 This is the front view of the filter press.
[0036] Figure 4 for Figure 2 A partial enlarged view of part A.
[0037] Figure 5 Schematic diagram of filter plate assembly.
[0038] Figure 6 It is a cross-sectional view of the filter plate at the end.
[0039] Figure 7 It is a cross-sectional view of the filter plate located in the middle.
[0040] Figure 8 It is a structural diagram of the lower hopper.
[0041] Fig. 9 This is a cross-sectional view of the lower hopper.
[0042] Fig.10 It is a structural diagram of a disc dryer.
[0043] Fig.11 A cross-sectional view of a disc dryer.
[0044] Fig.12 Schematic diagram of the structure of the disc dryer when the fixed tank is removed.
[0045] Fig.13 It is a schematic diagram of the assembly of the first heating plate and the second heating plate.
[0046] Fig.14 It is a structural schematic diagram of the first scraping mechanism.
[0047] Fig.15 It is a structural schematic diagram of the second scraping mechanism.
[0048] In the accompanying drawings: frame 1, guide bracket 2, guide hopper 3, filter plate 4, accommodating chamber 401, guide pipe 402, filter cloth 5, pressing mechanism 6, push hydraulic cylinder 601, push plate 602, feed pipe 7, annular electromagnet 801, negative pressure pipe 802, negative pressure container 901, vacuum pump 902, washing mechanism 10, washing liquid distribution pipe 1001, washing liquid inlet pipe 1002, lower hopper 11, cover 12, sieve plate 13, crushing material convex edge 14, rotating drive motor 15, baffle plate 16, fixed connecting rod 17, plug-in shaft 18, guide sleeve 19, guide shaft 20, fixed tank body 21, feed hopper 22, discharge pipe 2101, first heating plate 23, second heating plate 24, guide hole 25 , scraper drive mechanism 26, drive shaft 2601, drive motor 2602, first scraper mechanism 27, first fixed rod 2701, first fixed shaft 2702, first scraper 2703, first limit spring 2704, second scraper mechanism 28, second fixed rod 2801, second fixed shaft 2802, second scraper 2803, second limit spring 2804, scraper drive mechanism 29, material transmission mechanism 30, material guide cone 31, discharge port 32, fixed ring plate 33, annular discharge trough 34, discharge hole 35, protrusion 36, drive block 37, connecting spring 38, hot air inlet pipe 39, exhaust pipe 40, first baffle plate 41, second baffle plate 42, dehumidification pipe 43. DETAILED DESCRIPTION
[0049] In order to facilitate understanding by those skilled in the art, the structure of the present invention is further described in detail with reference to the embodiments in conjunction with the accompanying drawings:
[0050] refer to Figure 1-15 , a solid-liquid separation device for ternary precursor production, comprising a filter press and a disc dryer, wherein the filter press comprises:
[0051] A frame 1, wherein a corresponding guide bracket 2 is disposed on the upper portion of the frame 1, and a guide hopper 3 with a feed port facing the guide bracket 2 is fixedly mounted on the frame 1 below the guide bracket 2;
[0052] A plurality of filter plates 4 are laterally movably mounted on the guide bracket 2, and corresponding accommodating cavities 401 are respectively provided on opposite sides of two adjacent filter plates 4, and a material guide pipe 402 located in the middle of the accommodating cavity 401 is respectively penetrated through the middle of the filter plate 4, and a corresponding filter cloth 5 is respectively fixedly connected to one side of the filter plate 4 provided with the accommodating cavity 401, and the middle of the filter cloth 5 is respectively sealed and connected to the material guide pipe 402;
[0053] The clamping mechanism 6 comprises a push hydraulic cylinder 601 fixedly mounted on one end of the guide bracket 2. When the piston rod of the push hydraulic cylinder 601 is extended, the plurality of filter plates 4 are closed and connected with each other under the pressing action of the push hydraulic cylinder 601. After the filter plates 4 are closed and connected with each other, two adjacent guide pipes 402 are respectively arranged at intervals.
[0054] A feed pipe 7 is fixedly mounted on the other end of the guide bracket 2, the feed end of the feed pipe 7 is pumped to an external material source, and the discharge end of the feed pipe 7 is connected to a guide pipe 402 of the filter plate 4 at the end, so as to pump the material into between the filter cloths 5 of two adjacent filter plates 4;
[0055] The filter press strengthening mechanism comprises a plurality of annular electromagnets 801 and a plurality of negative pressure pipes 802. The annular electromagnets 801 are respectively sleeved on the periphery of the corresponding material guide pipes 402 and fixedly connected to the inner side of the corresponding filter cloth 5. The feed ends of the negative pressure pipes 802 are respectively connected to the filter plates 4 on the inner side of the filter cloth 5, and are used to evacuate the accommodating chamber 401 on the filter plate 4. The plurality of negative pressure pipes 802 are connected in parallel to the corresponding negative pressure mechanism. When the material enters between the filter cloths 5 of two adjacent filter plates 4, the annular electromagnets 801 are energized, and the distance between the filter cloths 5 of the two adjacent filter plates 4 is reduced under the action of the adsorption force, so as to squeeze and filter out the liquid material in the filter cake. At the same time, the negative pressure mechanism starts to pump negative pressure to accelerate the extraction of the liquid material in the filter cake.
[0056] The feed end of the disc dryer is connected to the discharge end of the guide hopper 3 of the filter press through a corresponding material transmission mechanism 30, which is used to heat and dry the material after the filter press. The material transmission mechanism 30 in this embodiment adopts a material lifting auger.
[0057] The filter press strengthening mechanism of the present invention comprises a plurality of annular electromagnets 801 and a plurality of negative pressure extraction pipes 802. The annular electromagnets 801 are respectively sleeved on the periphery of the corresponding material guide pipes 402 and fixedly connected to the inner side of the corresponding filter cloths 5. The feed ends of the negative pressure extraction pipes 802 are respectively connected to the filter plates 4 on the inner side of the filter cloths 5, and are used to vacuum the accommodating chambers 401 on the filter plates 4. After the material enters between the filter cloths 5 of two adjacent filter plates 4, as the feed pressure increases, the liquid material in the material gradually enters the accommodating chambers 401 of the filter plates 4 through the filter cloths 5. When the feed pressure reaches the set value, the annular electromagnets 801 are energized, and the spacing between the filter cloths 5 of the two adjacent filter plates 4 is reduced under the action of the adsorption force, so as to squeeze and filter out the liquid material in the filter cake; at the same time, the negative pressure extraction mechanism starts to extract the negative pressure to accelerate the extraction of the liquid material in the filter cake. In this way, the filter cake can be squeezed and negative pressure can be effectively formed on the filter cake, so that the liquid material in the filter cake can be discharged in two directions, thereby greatly improving the solid-liquid separation efficiency.
[0058] The disc dryer comprises:
[0059] A fixed tank body 21, a corresponding feed hopper 22 is arranged on the top of the fixed tank body 21, and a discharge pipe 2101 is arranged on the bottom of the fixed tank body 21; a first heating plate 23 and a second heating plate 24 are arranged alternately in height in the fixed tank body 21, and corresponding guide holes 25 are arranged in the middle of the first heating plate 23 and the second heating plate 24 respectively, and the periphery of the second heating plate 24 is extended to the outside of the first heating plate 23, and the guide hole diameter of the first heating plate 23 is smaller than the guide hole diameter of the second heating plate 24;
[0060] The scraper driving mechanism 26 comprises a driving shaft 2601 which penetrates through the guide hole 25 of the first heating plate 23 and the second heating plate 24, and the driving shaft 2601 is driven by a corresponding driving motor 2602;
[0061] The first scraper mechanism 27 comprises a first fixed rod 2701 fixed to the driving shaft 2601 on the upper side of the first heating disk 23 in an annular array, a plurality of corresponding first fixed shafts 2702 are fixedly connected side by side downward to the first fixed rod 2701, and first scrapers 2703 for scraping the material on the first heating disk 23 outward are rotatably mounted on the first fixed shafts 2702, and the first scrapers 2703 and the first fixed shafts 2702 are limited by corresponding first limit springs 2704;
[0062] The second scraper mechanism 28 comprises a second fixed rod 2801 fixed to the driving shaft 2601 on the upper side of the second heating disk 24 in an annular array, a plurality of corresponding second fixed shafts 2802 are fixedly connected side by side downward to the second fixed rod 2801, and second scrapers 2803 for scraping the material on the second heating disk 24 inwardly are rotatably mounted on the second fixed shafts 2802, and the second scrapers 2803 and the second fixed shafts 2802 are limited by corresponding second limit springs 2804;
[0063] The scraper driving mechanism 29 includes a plurality of circles of magnet sheets which are fixedly connected to the upper sides of the first heating disk 23 and the second heating disk 24 in an annular array at intervals. The magnet sheets are respectively arranged corresponding to the first scraper 2703 and the second scraper 2803. When the first scraper 2703 and the second scraper 2803 rotate and pass through the position where the magnet sheets are located, the first scraper 2703 and the second scraper 2803 are adsorbed, and the first limit spring 2704 and the second limit spring 2804 are compressed. When the compression force of the first limit spring 2704 and the second limit spring 2804 is greater than the adsorption force of the magnet sheets, the first scraper 2703 and the second scraper 2803 leave the position where the magnet sheets are located, and swing under the elastic force of the first limit spring 2704 and the second limit spring 2804, so as to break up the material when scraping it.
[0064] The present invention improves the structure of the first scraper mechanism 27 and the second scraper mechanism 28, and adds a scraper driving mechanism 29, which includes a plurality of magnet sheets fixedly connected to the upper sides of the first heating plate 23 and the second heating plate 24 in an annular array at intervals. When the first scraper 2703 and the second scraper 2803 rotate and pass the position where the magnet sheets are located, the first scraper 2703 and the second scraper 2803 are adsorbed, and the first limit spring 2704 and the second limit spring 2804 are compressed. When the first limit spring 2704 When the compression force of the second limit spring 2804 is greater than the adsorption force of the magnet sheet, the first scraper 2703 and the second scraper 2803 leave the position of the magnet sheet and swing under the elastic force of the first limit spring 2704 and the second limit spring 2804, so as to break up the material when scraping it. In this way, the material can be effectively broken up simultaneously during the process of shoveling and pushing the material, so as to improve the contact uniformity and contact rate between the material and the heating plate, thereby effectively improving the drying effect of the material.
[0065] A corresponding lower hopper 11 is fixedly installed at the lower side of the discharge end of the guide hopper 3. The top of the lower hopper 11 is folded inward in an inverted L shape and provided with a corresponding cover 12. The discharge end of the guide hopper 3 extends through the cover 12. A sieve plate 13 arranged in a ring shape is rotatably installed at the bottom side of the cover 12. A plurality of corresponding sieve holes are evenly distributed on the sieve plate 13, and a plurality of corresponding crushing material ridges 14 are fixedly connected to the top surface of the sieve plate 13 at intervals. The sieve plate 13 is driven by a rotary drive motor 15 fixedly installed on the guide hopper 3. The feed hopper 22 is connected to the discharge end of the lower hopper 11 through the lifting auger. Several baffle plates 16 are arranged at intervals in the cover 12, and the bottoms are arranged at intervals with the crushing material ridges 14. The sieve plate 13 is provided with a plurality of fixed connecting rods 17 fixedly connected to the output shaft end of the rotary drive motor 15 at intervals.
[0066] In the process of the filter cake after filtration being discharged into the guide hopper 3, the material is initially crushed by collision, and the crushed material enters the cover of the lower hopper 11 through the guide hopper 3. As the sieve plate 13 rotates, the crushing convex edge 14 drives the material to pass through the baffle plate 16. Under the cooperation of the crushing convex edge 14 and the baffle plate 16, the material is sheared and crushed, and the crushed material is evenly screened out through the sieve holes on the sieve plate 13, so that the filter cake is effectively and directly crushed and output, so that the material after solid-liquid separation can directly enter the corresponding drying equipment for drying processing, so as to enhance the use function of the present invention.
[0067] The negative pressure extraction mechanism comprises a negative pressure extraction container 901 , a plurality of negative pressure extraction tubes 802 are connected in parallel to the negative pressure extraction container 901 , and the top pump of the negative pressure extraction container 901 is connected to a corresponding vacuum pump 902 .
[0068] A corresponding push plate 602 is fixedly connected to the piston rod end of the push hydraulic cylinder 601. When the piston rod of the push hydraulic cylinder 601 is extended, the push plate 602 pushes the plurality of filter plates 4 to form a closed connection with each other.
[0069] The side of the annular electromagnet 801 on the filter plate 4 at the end that is not connected to the filter cloth 5 is respectively provided with a corresponding plug-in shaft 18, and the plug-in shaft 18 can be movably plugged into the filter plate 4 at the end. The side of the annular electromagnet 801 on both sides of the filter plate 4 at the middle that is not connected to the filter cloth 5 is respectively fixed with a guide sleeve 19 and a guide shaft 20 that form a movable docking with each other. The load of the annular electromagnet 801 is transferred to the filter plate 4, thereby preventing the filter cloth 5 from being excessively loaded due to the setting of the annular electromagnet 801, so as to ensure the practical effect of the present invention.
[0070] The filter press also includes a washing mechanism 10, which includes a washing liquid distributing pipe 1001 connected between the filter cloths 5 of two adjacent filter plates 4, and the washing liquid distributing pipe 1001 is connected to an external washing liquid source through a corresponding washing liquid inlet pipe 1002. After the filter cake is formed, the filter cake can be washed by injecting washing liquid. After washing is completed, the annular electromagnet 801 is energized and the negative pressure pumping mechanism is started to pump negative pressure, so as to enhance the use function of the present invention.
[0071] A corresponding material guide cone 31 is fixedly connected to the fixed tank body 21 in the middle of the feed hopper 22, and a plurality of corresponding material discharge ports 32 are evenly distributed on the fixed tank body 21 outside the material guide cone 31. Under the action of the material guide cone 31, the material entering the feed hopper 22 is dispersed and discharged, thereby ensuring the uniformity of material discharge, improving the uniformity of the material in the subsequent shoveling process, and further effectively improving the drying effect of the material.
[0072] A corresponding fixed ring plate 33 is fixedly connected to the bottom side of the top of the fixed tank body 21, and a corresponding annular material discharge trough 34 is movably installed inside the fixed ring plate 33. The bottom surface of the annular material discharge trough 34 is evenly distributed with many corresponding material discharge holes 35; the inner side of the annular material discharge trough 34 is evenly distributed with a plurality of corresponding protrusions 36, and a driving block 37 adapted to the protrusions 36 is fixedly connected to the driving shaft 2601. During the rotation of the driving shaft 2601, the driving block 37 gradually blocks and pushes the protrusions 36 to drive the annular material discharge trough 34 to vibrate. In this way, the material after discharge can be further dispersed to ensure the uniformity of material discharge.
[0073] In this embodiment, the outer side of the annular material discharge chute 34 is connected to the fixed ring plate 33 via a plurality of connecting springs 38 .
[0074] The first heating plate 23 and the second heating plate 24 are respectively hollow, and one side of the first heating plate 23 and the second heating plate 24 are respectively connected to the corresponding hot air inlet pipe 39 through the corresponding air intake duct, and the other side of the first heating plate 23 and the second heating plate 34 are respectively connected to the corresponding exhaust pipe 40 through the corresponding exhaust duct.
[0075] The magnet pieces are respectively fixedly embedded in the top and bottom sides of the first heating plate 23 and the second heating plate 24. The peripheries of the first heating plate 23 and the second heating plate 34 are respectively fixedly connected to the fixed tank body 21 through corresponding connecting rods.
[0076] The guide hole of the first heating plate 23 is fixedly connected with a circle of corresponding first material baffle plates 41 in an inclined manner inwardly. The periphery of the second heating plate 24 is fixedly connected with a circle of corresponding second baffle plates 42 in an inclined manner outwardly. The top of the fixed tank body 21 is connected with a corresponding dehumidification pipe 43 outwardly.
[0077] The above is only a preferred embodiment of the present invention. It should be pointed out that for ordinary technicians in this technical field, several improvements and modifications can be made without departing from the principle of the present invention. These improvements and modifications should also be regarded as the scope of protection of the present invention.
Claims
1. A solid-liquid separation device for ternary precursor production, comprising a filter press and a disc dryer, characterized in that: The filter press comprises: A frame (1), wherein a corresponding guide bracket (2) is arranged on the upper part of the frame (1), and a guide hopper (3) with a feed opening facing the guide bracket (2) is fixedly mounted on the frame (1) below the guide bracket (2); A plurality of filter plates (4) are laterally movably mounted on the guide bracket (2), a corresponding accommodating cavity (401) is respectively provided on opposite sides of two adjacent filter plates (4), a material guide pipe (402) located in the middle of the accommodating cavity (401) is respectively provided through the middle of the filter plate (4), a corresponding filter cloth (5) is respectively fixedly connected to one side of the filter plate (4) provided with the accommodating cavity (401), and the middle of the filter cloth (5) is respectively sealed and connected to the material guide pipe (402); The clamping mechanism (6) comprises a pushing hydraulic cylinder (601) fixedly mounted on one end of the guide bracket (2); when the piston rod of the pushing hydraulic cylinder (601) is extended, the plurality of filter plates (4) are closed and connected to each other under the pushing action of the pushing hydraulic cylinder (601); after the filter plates (4) are closed and connected to each other, two adjacent material guide pipes (402) are respectively arranged at intervals; A feed pipe (7) is fixedly mounted on the other end of the guide bracket (2); the feed end of the feed pipe (7) is connected to an external material source by a pump, and the discharge end of the feed pipe (7) is connected to a material guide pipe (402) of a filter plate (4) located at the end, so as to pump the material into between the filter cloths (5) of two adjacent filter plates (4); The filter press strengthening mechanism comprises a plurality of annular electromagnets (801) and a plurality of negative pressure extraction pipes (802), wherein the annular electromagnets (801) are respectively sleeved on the periphery of the corresponding material guide pipe (402) and fixedly connected to the inner side of the corresponding filter cloth (5), and the feed ends of the negative pressure extraction pipes (802) are respectively connected to the filter plates (4) on the inner side of the filter cloth (5) for vacuumizing the accommodating chamber (401) on the filter plate (4), and the plurality of negative pressure extraction pipes (802) are connected in parallel to the corresponding negative pressure extraction mechanism; when the material enters between the filter cloths (5) of two adjacent filter plates (4), the annular electromagnets (801) are energized, and the distance between the filter cloths (5) of the two adjacent filter plates (4) is reduced under the action of the adsorption force, so as to squeeze and filter out the liquid material in the filter cake, and at the same time, the negative pressure extraction mechanism starts to extract the negative pressure, so as to accelerate the extraction of the liquid material in the filter cake; The feed end of the disc dryer is connected to the discharge end of the guide hopper (3) of the filter press via a corresponding material transmission mechanism (30), so as to heat and dry the material after the filter press; The disc dryer comprises: A fixed tank body (21), wherein a corresponding feed hopper (22) is arranged at the top of the fixed tank body (21), and a discharge pipe (2101) is arranged at the bottom of the fixed tank body (21); a first heating plate (23) and a second heating plate (24) are arranged alternately in height in the fixed tank body (21), corresponding guide holes (25) are arranged in the middle of the first heating plate (23) and the second heating plate (24), respectively, the periphery of the second heating plate (24) is extended to the outside of the first heating plate (23), and the guide hole diameter of the first heating plate (23) is smaller than the guide hole diameter of the second heating plate (24); A scraper drive mechanism (26), comprising a drive shaft (2601) that passes through the guide holes (25) installed on the first heating plate (23) and the second heating plate (24), wherein the drive shaft (2601) is driven by a corresponding drive motor (2602); The first scraping mechanism (27) comprises a first fixed rod (2701) fixed in an annular array to a driving shaft (2601) on the upper side of the first heating disk (23), a plurality of corresponding first fixed shafts (2702) being fixed side by side downwardly to the first fixed rod (2701), first scrapers (2703) for scraping materials on the first heating disk (23) outwardly being rotatably mounted on the first fixed shafts (2702), and the first scrapers (2703) and the first fixed shafts (2702) being limited by corresponding first limit springs (2704); The second scraping mechanism (28) comprises a second fixed rod (2801) fixed in an annular array to a driving shaft (2601) on the upper side of the second heating disk (24), a plurality of corresponding second fixed shafts (2802) being fixed side by side downwardly to the second fixed rod (2801), second scrapers (2803) for scraping materials on the second heating disk (24) inwardly being rotatably mounted on the second fixed shafts (2802), and the second scrapers (2803) and the second fixed shafts (2802) being limited by corresponding second limit springs (2804); The scraper driving mechanism (29) comprises a plurality of magnet sheets which are fixedly connected to the upper sides of the first heating plate (23) and the second heating plate (24) at intervals in a circular array. The magnet sheets are respectively arranged corresponding to the first scraper (2703) and the second scraper (2803). When the first scraper (2703) and the second scraper (2803) rotate and pass the positions where the magnet sheets are located, the first scraper (2703) and the second scraper (2803) are adsorbed, and the first limit spring (2704) and the second limit spring (2804) are compressed. When the compression force of the first limit spring (2704) and the second limit spring (2804) is greater than the adsorption force of the magnet sheets, the first scraper (2703) and the second scraper (2803) leave the positions where the magnet sheets are located, and swing under the elastic force of the first limit spring (2704) and the second limit spring (2804), so as to break up the materials when scraping them.
2. The solid-liquid separation device for ternary precursor production according to claim 1, characterized in that: A corresponding lower hopper (11) is fixedly mounted on the lower side of the discharge end of the guide hopper (3); the top of the lower hopper (11) is folded inwardly in an inverted L shape and is provided with a corresponding cover (12); the discharge end of the guide hopper (3) extends through the cover (12); a sieve plate (13) arranged in a ring shape is rotatably mounted on the bottom side of the cover (12); a plurality of corresponding sieve holes are evenly distributed on the sieve plate (13), and a plurality of corresponding crushing ridges (14) are fixedly connected to the top surface of the sieve plate (13) at intervals; the sieve plate (13) is driven by a rotary drive motor (15) fixedly mounted on the guide hopper (3).
3. The solid-liquid separation device for producing a ternary precursor according to claim 2, characterized in that: A plurality of material blocking plates (16) are arranged at intervals in the cover (12) and have bottoms spaced apart from the material crushing ridge (14).
4. The solid-liquid separation device for producing a ternary precursor according to claim 3, characterized in that: The screening plate (13) is provided with a plurality of fixed connecting rods (17) fixedly connected to the output shaft end of the rotary drive motor (15) at intervals inwardly.
5. The solid-liquid separation equipment for ternary precursor production according to claim 1, characterized in that: The negative pressure extraction mechanism comprises a negative pressure extraction container (901), a plurality of negative pressure extraction tubes (802) are connected in parallel to the negative pressure extraction container (901), and a top pump of the negative pressure extraction container (901) is connected to a corresponding vacuum pump (902).
6. The solid-liquid separation equipment for ternary precursor production according to claim 1, characterized in that: A corresponding push plate (602) is fixedly connected to the piston rod end of the push hydraulic cylinder (601); when the piston rod of the push hydraulic cylinder (601) is extended, the push plate (602) pushes the plurality of filter plates (4) to form a closed connection with each other.
7. The solid-liquid separation device for producing a ternary precursor according to claim 1, characterized in that: The side of the annular electromagnet (801) on the filter plate (4) at the end that is not connected to the filter cloth (5) is respectively provided with a corresponding plug-in shaft (18), and the plug-in shaft (18) is respectively movably plugged into the filter plate (4) at the end.
8. The solid-liquid separation device for producing a ternary precursor according to claim 7, characterized in that: The sides of the annular electromagnets (801) on both sides of the filter plate (4) located in the middle that are not connected to the filter cloth (5) are respectively fixedly connected with a guide sleeve (19) and a guide shaft (20) that are movably connected to each other.
9. The solid-liquid separation device for ternary precursor production according to claim 1, characterized in that: The filter press further comprises a washing mechanism (10), wherein the washing mechanism (10) comprises a washing liquid distribution pipe (1001) connected between the filter cloths (5) of two adjacent filter plates (4), and the washing liquid distribution pipe (1001) is connected to an external washing liquid source via a corresponding washing liquid inlet pipe (1002) pump.
