Refining furnace for fly ash ionization reduzate
The refining furnace addresses the inconvenience and safety issues of manual handling by incorporating a rotating mechanism and hydraulic cylinders for automated discharge, enhancing safety and efficiency in refining processes.
Patent Information
- Application Number
- CN202420952384.6
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-05-06
- Publication Date
- 2024-12-20
- Estimated Expiration
- 2034-05-06
AI Technical Summary
Existing refining furnaces are inconvenient for exporting refined materials, requiring manual handling of high-temperature metal solutions, which increases labor intensity and poses safety hazards.
A refining furnace design featuring a rotating mechanism and hydraulic cylinders to tilt and discharge materials, along with a sealing cover for easy cleaning, and a system for adjusting the distance between the furnace body and heat source, allowing automated discharge of refined solutions.
Automated discharge of refined materials reduces labor intensity and safety hazards by eliminating manual handling, while enabling precise control of heating effects and facilitating easy cleaning.
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Figure CN222211219U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of refining furnaces, in particular to a refining furnace for fly ash ionization reduction products. Background Art
[0002] Fly ash is a volcanic ash material, which comes from inorganic components in coal. The inorganic components in coal are mainly clay minerals, and there are also small amounts of pyrite, calcite, quartz and other minerals. Therefore, the chemical composition of fly ash is mainly silicon dioxide and aluminum oxide, and other components are iron oxide, calcium oxide, magnesium oxide, potassium chloride, sodium oxide, sulfur trioxide and unburned organic matter. Fly ash obtains aluminum, silicon and iron by ionization.
[0003] Fly ash contains about 8% unburned carbon. According to rough calculations, the carbon slag in the electrolytic cell and the unburned carbon in the fly ash can just reduce aluminum, silicon and iron. According to the different specifications of aluminum silicon or aluminum silicon iron alloy produced, the difference in aluminum silicon and iron content in the fly ash can be considered to adjust the addition ratio of fly ash and alumina powder. If aluminum silicon alloy is produced, the iron content may be high, and iron removal agent (borax flux, manganese chloride solvent) can be used for iron removal. If aluminum silicon iron alloy is produced, iron removal is not required. Other metal elements can be removed by high-temperature burning or adding refining agents and slag removal agents. The reaction equation in the electrolytic cell is:
[0004] SiO2+2C→2CO+Si(reduction)
[0005] 3SiO+4Al→2Al2O3+3Si(reduction)
[0006] Al 2O3+3C→3CO+2Al (electrolysis)
[0007] Fe2O3+3C→3CO+2Fe(reduction)
[0008] The main element yields during the electrolytic reduction of fly ash: If the fly ash contains 50% silicon dioxide, 27% aluminum oxide, and 8% iron oxide, 1000kg of fly ash can theoretically produce 233kg of elemental silicon, 143kg of metallic aluminum, and 56kg of metallic iron. In order to remove impurities, the obtained metals need to be refined for elemental silicon, metallic aluminum, or metallic iron. Refining requires the use of a refining furnace, which is a smelting equipment in the hot processing industry and is mostly used for the final deoxidation and alloying of molten steel in ferrous metallurgy.
[0009] Existing refining furnaces are not convenient for exporting refined materials. The traditional method requires workers to manually export the refined high-temperature metal solution, which increases labor intensity and poses a high safety hazard. Utility Model Content
[0010] In view of the defects existing in the prior art, the technical problem solved by the utility model is that the existing refining furnace is not convenient for exporting the refined materials, and the traditional method requires workers to manually export the refined high-temperature metal solution, which increases the labor intensity and has high safety hazards. A refining furnace for fly ash ionization reduction is provided.
[0011] In order to achieve the above objectives, the utility model provides:
[0012] A refining furnace for fly ash ionization reduction includes a base, a high-temperature heating furnace is arranged on the top of the base, two straight plates are symmetrically arranged on the top of the base, vertical grooves are opened on the tops of the two straight plates, and force-bearing plates are slidably installed in the two vertical grooves;
[0013] The refining furnace body is located above the high-temperature heating furnace. A discharge port is inclined on the top side of the refining furnace body. A rotating mechanism for driving the refining furnace body to tilt and discharge materials is arranged on the two force-bearing plates. A sealing cover is installed at the top opening of the refining furnace body.
[0014] Preferably, two reinforcement rods for reinforcing and supporting the straight board are installed between the outer side of the straight board and the base.
[0015] Preferably, the same top plate is installed on the top of the two force-bearing plates, and a linear motor is installed on the top of the top plate, and the output shaft of the linear motor is connected to the sealing cover; the linear motor drives the sealing cover to adjust the height, and the sealing cover leaves the refining furnace body, which is convenient for cleaning the inside of the refining furnace body.
[0016] Preferably, the top of the sealing cover is provided with an exhaust hole, a feeding port, and an impurity remover storage tank, the bottom of the impurity remover storage tank is connected to the sealing cover via a straight pipe, and an electric valve is provided on the straight pipe.
[0017] Preferably, two hydraulic cylinders are arranged in the vertical groove, and the output ends of the two hydraulic cylinders are fixedly mounted on the bottom of the force-bearing plate; the hydraulic cylinders are used to drive the vertical height adjustment of the force-bearing plate, and the two force-bearing plates drive the refining furnace body to adjust the height, adjust the height between the refining furnace body and the high-temperature heating furnace, adjust the distance between the refining furnace body and the heat source, and adjust the heating effect of the refining furnace body.
[0018] Preferably, the rotating mechanism includes a rotating shaft and a synchronous motor. The rotating shaft is installed on the force plate for transverse rotation through a bearing. The inner end of the rotating shaft is welded to the outer side of the refining furnace body. The synchronous motor is installed on the outer side of the force plate. A driving gear is installed on the output shaft of the synchronous motor. A driven gear is installed on the outer end of the rotating shaft, and the driving gear is meshed with the driven gear. The two synchronous motors drive the two driven gears to rotate through the two driving gears, and the two driven gears drive the refining furnace body to rotate through the two rotating shafts, so that the discharge port is tilted downward, and the refined solution can be poured out through the discharge port, avoiding manual operation of the staff, reducing labor intensity and safety hazards.
[0019] Compared with the prior art, the advantages of the utility model are:
[0020] 1. The impurity remover is stored in the impurity remover storage tank. The electric valve can be opened to introduce the impurity remover into the main body of the refining furnace. The main body of the refining furnace is heated by a high-temperature heating furnace. After refining, two synchronous motors drive two driving gears to rotate, and the two driving gears drive two driven gears to rotate. The two driven gears drive two rotating shafts to rotate, and the two rotating shafts drive the main body of the refining furnace to rotate, so that the discharge port is tilted downward, and the refined solution can be poured out through the discharge port, avoiding manual operation of the staff, reducing labor intensity and safety hazards;
[0021] 2. Use hydraulic cylinders to drive the vertical height adjustment of the force-bearing plates. The two force-bearing plates drive the height adjustment of the refining furnace body through two rotating mechanisms, adjust the height between the refining furnace body and the high-temperature heating furnace, adjust the distance between the refining furnace body and the heat source, and adjust the heating effect of the refining furnace body;
[0022] 3. The linear motor drives the sealing cover to adjust its height, and the sealing cover leaves the refining furnace body, which is convenient for cleaning the inside of the refining furnace body;
[0023] The utility model drives the refining furnace body to rotate through two rotating mechanisms, so that the discharge port is inclined downward, and the refined solution can be poured out through the discharge port, avoiding manual operation of the staff, reducing labor intensity and safety hazards, and can adjust the distance between the refining furnace body and the heat source, and adjust the heating effect of the refining furnace body. BRIEF DESCRIPTION OF THE DRAWINGS
[0024] Figure 1 This is the left view structural diagram of this design;
[0025] Figure 2 This is the right view structural diagram of this design;
[0026] Figure 3 This is a schematic diagram of the structure of the sealing cover, feeding port, exhaust hole and impurity removal agent storage tank in this design;
[0027] Figure 4 This is a schematic diagram of the cross-sectional structure of the straight plate, load-bearing plate and two hydraulic cylinders in this design.
[0028] In the figure: 1. base; 11. high-temperature heating furnace; 12. reinforcement rod; 2. straight plate; 21. force plate; 22. vertical groove; 23. hydraulic cylinder; 3. rotating mechanism; 31. rotating shaft; 32. driven gear; 33. synchronous motor; 34. driving gear; 4. refining furnace body; 41. discharge port; 42. sealing cover; 43. exhaust hole; 44. feeding port; 5. top plate; 51. linear motor; 6. impurity removal agent storage tank; 61. electric valve; 62. straight pipe. DETAILED DESCRIPTION
[0029] The embodiments of the present invention are further described in detail below in conjunction with the accompanying drawings.
[0030] See also Figure 1-4 As shown, a refining furnace for fly ash ionization reduction includes a base 1, a high-temperature heating furnace 11 is arranged on the top of the base 1, two straight plates 2 are symmetrically arranged on the top of the base 1, two reinforcing rods 12 for reinforcing and supporting the straight plates 2 are installed between the outer sides of the straight plates 2 and the base 1, vertical grooves 22 are opened on the tops of the two straight plates 2, and force-bearing plates 21 are slidably installed in the two vertical grooves 22;
[0031] The refining furnace body 4 is located above the high-temperature heating furnace 11. A discharge port 41 is obliquely arranged on the top side of the refining furnace body 4. A rotating mechanism 3 for driving the refining furnace body 4 to tilt and discharge materials is arranged on the two force-bearing plates 21. A sealing cover 42 is installed on the top opening of the refining furnace body 4.
[0032] In this embodiment, the same top plate 5 is installed on the top of the two force-bearing plates 21, and a linear motor 51 is installed on the top of the top plate 5. The output shaft of the linear motor 51 is connected to the sealing cover 42; the linear motor 51 drives the sealing cover 42 to adjust the height, and the sealing cover 42 leaves the refining furnace body 4, which is convenient for cleaning the inside of the refining furnace body 4.
[0033] In this embodiment, the top of the sealing cover 42 is provided with an exhaust hole 43, a feeding port 44, and an impurity remover storage tank 6. A straight pipe 62 is connected between the bottom of the impurity remover storage tank 6 and the sealing cover 42, and an electric valve 61 is provided on the straight pipe 62.
[0034] In this embodiment, two hydraulic cylinders 23 are arranged in the vertical groove 22, and the output ends of the two hydraulic cylinders 23 are fixedly installed on the bottom of the force-bearing plate 21; the hydraulic cylinders 23 are used to drive the vertical height adjustment of the force-bearing plate 21, and the two force-bearing plates 21 drive the refining furnace body 4 to adjust the height, adjust the height between the refining furnace body 4 and the high-temperature heating furnace 11, adjust the distance between the refining furnace body 4 and the heat source, and adjust the heating effect of the refining furnace body 4.
[0035] In this embodiment, the rotating mechanism 3 includes a rotating shaft 31 and a synchronous motor 33. The rotating shaft 31 is installed on the force plate 21 for transverse rotation through a bearing. The inner end of the rotating shaft 31 is welded to the outer side of the refining furnace body 4. The synchronous motor 33 is installed on the outer side of the force plate 21. A driving gear 34 is installed on the output shaft of the synchronous motor 33. A driven gear 32 is installed on the outer end of the rotating shaft 31, and the driving gear 34 is meshed with the driven gear 32. The two synchronous motors 33 drive the two driven gears 32 to rotate through the two driving gears 34, and the two driven gears 32 drive the refining furnace body 4 to rotate through the two rotating shafts 31, so that the discharge port 41 is tilted downward, and the refined solution can be poured out through the discharge port 41, avoiding manual operation of the staff, reducing labor intensity and safety hazards.
[0036] Working principle: When in use, turn on the power supply and controller, add raw materials into the refining furnace body 4 through the feeding port 44, store the impurity remover in the impurity remover storage tank 6, open the electric valve 61 to introduce the impurity remover into the refining furnace body 4, use the high-temperature heating furnace 11 to heat the refining furnace body 4, and after refining, the two synchronous motors 33 drive the two driving gears 34 to rotate, the two driving gears 34 drive the two driven gears 32 to rotate, the two driven gears 32 drive the two rotating shafts 31 to rotate, and the two rotating shafts 31 drive the refining furnace body 4 to rotate, so that the discharge port 41 is tilted downward, and the refined solution can be poured out through the discharge port 41, avoiding manual operation of the staff, reducing labor intensity and safety hazards;
[0037] The hydraulic cylinder 23 is used to drive the force-bearing plate 21 to adjust its vertical height. The two force-bearing plates 21 drive the refining furnace body 4 to adjust its height through the two rotating mechanisms 3, thereby adjusting the height between the refining furnace body 4 and the high-temperature heating furnace 11, adjusting the distance between the refining furnace body 4 and the heat source, and adjusting the heating effect of the refining furnace body 4;
[0038] The linear motor 51 drives the sealing cover 42 to adjust its height, and the sealing cover 42 leaves the refining furnace body 4, so as to facilitate cleaning of the interior of the refining furnace body 4.
[0039] The present invention is not limited to the above-mentioned optimal implementation mode. Anyone can derive other various forms of products under the inspiration of the present invention. However, no matter what changes are made in the shape or structure, any technical solution that is the same or similar to the present invention is within the scope of protection.
Claims
1. A refining furnace for fly ash ionization reduction, comprising a base (1), a high-temperature heating furnace (11) being arranged on the top of the base (1), characterized in that: Two straight plates (2) are symmetrically arranged on the top of the base (1), and vertical grooves (22) are respectively provided on the tops of the two straight plates (2), and force-bearing plates (21) are slidably installed in the two vertical grooves (22); The refining furnace body (4) is located above the high-temperature heating furnace (11), and a discharge port (41) is obliquely arranged on the top side of the refining furnace body (4). A rotating mechanism (3) for driving the refining furnace body (4) to tilt and discharge materials is arranged on the two force-bearing plates (21), and a sealing cover (42) is installed at the top opening of the refining furnace body (4).
2. The fly ash ionization reduction product refining furnace according to claim 1, characterized in that: The top of the two force-bearing plates (21) is equipped with a same top plate (5), the top of the top plate (5) is equipped with a linear motor (51), and the output shaft of the linear motor (51) is connected to the sealing cover (42).
3. The refining furnace for fly ash ionization reduction according to claim 1, characterized in that: The top of the sealing cover (42) is provided with an exhaust hole (43), a feeding port (44), and an impurity remover storage tank (6); a straight pipe (62) is connected between the bottom of the impurity remover storage tank (6) and the sealing cover (42); and an electric valve (61) is provided on the straight pipe (62).
4. The refining furnace for fly ash ionization reduction according to claim 1, characterized in that: Two hydraulic cylinders (23) are arranged in the vertical groove (22), and the output ends of the two hydraulic cylinders (23) are fixedly mounted on the bottom of the force-bearing plate (21).
5. The refining furnace for fly ash ionization reduction according to claim 1, characterized in that: The rotating mechanism (3) comprises a rotating shaft (31) and a synchronous motor (33). The rotating shaft (31) is installed on the force-bearing plate (21) via a bearing for transverse rotation. The inner end of the rotating shaft (31) is welded to the outer side of the refining furnace body (4). The synchronous motor (33) is installed on the outer side of the force-bearing plate (21). A driving gear (34) is installed on the output shaft of the synchronous motor (33). A driven gear (32) is installed on the outer end of the rotating shaft (31). The driving gear (34) is meshed with the driven gear (32).
6. The refining furnace for fly ash ionization reduction according to claim 1, characterized in that: Two reinforcement rods (12) for reinforcing and supporting the straight plate (2) are installed between the outer side of the straight plate (2) and the base (1).
