Reaction furnace for producing and processing zinc oxide

Abstract

The utility model relates to the technical field of reaction furnaces, in particular to a reaction furnace for producing and processing zinc oxide. According to the technical scheme, the oxygen supply assembly comprises a heating plate, two lower oxygen pipes and two upper oxygen pipes, the inner wall of a reaction bin is fixedly connected with the heating plate, the ends of the lower oxygen pipes and the ends of the upper oxygen pipes are fixedly connected with the reaction bin, oxygen spraying openings of the lower oxygen pipes and the upper oxygen pipes face a zinc block, and the oxygen spraying openings of the lower oxygen pipes and the upper oxygen pipes face the zinc block. The lower oxygen pipe and the upper oxygen pipe are both communicated with the oxygen box. According to the utility model, the zinc blocks are crushed by the crushing device and then thrown out to perform parabolic motion, the zinc blocks with different gravities are subjected to different inertias, so that the zinc blocks are thrown in the air to separate different particle zinc blocks, and then the lower oxygen pipe and the upper oxygen pipe are arranged on the two sides of the moving track of the zinc blocks and spray oxygen to the zinc blocks; the contact area of the zinc block and oxygen is increased, and the oxidation efficiency is improved.

Description

Technical Field

[0001] The utility model relates to the technical field of reaction furnaces, in particular to a reaction furnace for producing and processing zinc oxide. Background Art

[0002] Zinc oxide is the oxide of zinc. There are two methods for producing zinc oxide: direct method and indirect method. The indirect method produces zinc with high purity. The indirect method requires a large amount of heat source to heat production equipment such as reactors and evaporators. Zinc is evaporated in a high temperature environment to form gaseous zinc. The steam is oxidized by oxygen in the air to produce zinc oxide. Finally, the zinc oxide is cooled and formed through a cooling tube.

[0003] In the prior art, a reactor uses an indirect method to produce zinc oxide, in which a zinc ingot is placed in a reactor and the high temperature of the reactor evaporates the zinc to form gaseous zinc.

[0004] However, when this reactor uses the indirect method to produce zinc oxide, the zinc raw material uses zinc ingots, which are large in size and require a long time for melting and then evaporation and gasification, which affects the preparation efficiency of zinc oxide. Utility Model Content

[0005] The utility model aims to provide a reactor for producing and processing zinc oxide in view of the problem in the background technology that the large volume of zinc ingots leads to slow gasification speed and affects the preparation efficiency of zinc oxide.

[0006] The technical solution of the utility model is: a reactor for producing and processing zinc oxide, comprising:

[0007] A base, a reaction chamber is fixedly installed on the top of the base, and an oxygen box is fixedly installed on the top of the reaction chamber;

[0008] A crushing assembly includes a feed inlet and a crushing device. The left side of the reaction bin is provided with an inclined feed inlet. The zinc block enters the interior of the reaction bin along a parabolic trajectory from the feed inlet. The crushing device is located at the moving trajectory of the zinc block.

[0009] The oxygen supply assembly comprises a lower oxygen pipe and an upper oxygen pipe, two of the lower oxygen pipes and two of the upper oxygen pipes are provided, the ends of the lower oxygen pipes and the upper oxygen pipes are fixedly connected to the reaction chamber, the oxygen spray ports of the lower oxygen pipes and the upper oxygen pipes face the zinc block, and the lower oxygen pipes and the upper oxygen pipes are connected to the oxygen box.

[0010] Optionally, the crushing device includes a main crushing roller and an auxiliary crushing roller, both of which are provided with crushing teeth, the positions of the crushing teeth on the main crushing roller and the auxiliary crushing roller are staggered, and the ends of the main crushing roller and the auxiliary crushing roller are rotatably connected to the reaction bin.

[0011] Optionally, a first gear is fixedly mounted on the end of the main crushing roller, and a second gear is fixedly mounted on the end of the auxiliary crushing roller, and the first gear is meshingly connected with the second gear.

[0012] Optionally, the oxygen supply component further includes a heating plate, the inner wall of the reaction chamber is fixedly connected to the heating plate, the heating plate is tilted, and the heating plate is located directly below the crushing device.

[0013] Optionally, a baffle is fixedly mounted on the side of the reaction chamber facing the heating plate, and the baffle is abutted against the front and back sides of the heating plate.

[0014] Optionally, a collecting tray is fixedly installed inside the right wall of the reaction chamber, a cooling pipe is fixedly installed at the end of the collecting tray, and a suction fan is rotatably connected inside the cooling pipe.

[0015] Optionally, a feeding platform is fixedly installed on the top of the base platform and located on the left side of the reaction bin, and an inclined feeding chute is provided on the top of the feeding platform.

[0016] Compared with the prior art, the utility model has the following beneficial technical effects:

[0017] The utility model crushes the zinc block by the main crushing roller and the first gear, so that the zinc block is crushed into small particles, the reaction efficiency of the zinc block is accelerated, and the zinc block is prevented from being too large, and the heat can only be gradually heated from the outside of the zinc block to the inside, resulting in the zinc block melting and evaporation speed being slow, so that the oxidation efficiency of zinc oxide is reduced.

[0018] Furthermore, after the zinc blocks are crushed by the crushing device, they are thrown out to perform parabolic motion. The crushed zinc blocks are of different sizes. Zinc blocks of different volumes, that is, zinc blocks of different gravity, are subjected to different inertias, so that zinc blocks of different particles are separated when they are thrown into the air, thereby preventing the zinc blocks from piling up.

[0019] Furthermore, a lower oxygen pipe and an upper oxygen pipe are placed on both sides of the moving track of the zinc block, and the lower oxygen pipe and the upper oxygen pipe spray oxygen to increase the contact area between the zinc block and oxygen. BRIEF DESCRIPTION OF THE DRAWINGS

[0020] Figure 1 A schematic diagram of the overall structure of an embodiment of the utility model is given;

[0021] Figure 2 A schematic cross-sectional view of a reaction chamber structure of an embodiment of the utility model is given;

[0022] Figure 3 Given Figure 2 A part of the main crushing roller structure enlarged schematic diagram;

[0023] Figure 4A schematic diagram of a front and cross-sectional view of a reaction chamber structure of an embodiment of the utility model is given.

[0024] Figure numerals: 1. base; 2. feed platform; 3. reaction chamber; 4. oxygen box; 5. crushing assembly; 51. feed port; 52. main crushing roller; 53. first gear; 54. second gear; 55. auxiliary crushing roller; 6. oxygen supply assembly; 61. heating plate; 62. lower oxygen pipe; 63. upper oxygen pipe; 64. collection tray; 65. cooling pipe. DETAILED DESCRIPTION

[0025] The technical solution of the present utility model will be clearly and completely described below in conjunction with the accompanying drawings. Obviously, the described embodiments are only part of the embodiments of the present utility model, rather than all of the embodiments.

[0026] The components of the embodiments of the present invention generally described and shown in the drawings herein can be arranged and designed in various different configurations. Therefore, the following detailed description of the embodiments of the present invention provided in the drawings is not intended to limit the scope of the claimed invention, but merely represents selected embodiments of the present invention.

[0027] Based on the embodiments of the present utility model, all other embodiments obtained by ordinary technicians in the field without making any creative work shall fall within the scope of protection of the present utility model.

[0028] In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicating the orientation or positional relationship, are based on the orientation or positional relationship shown in the drawings, and are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as limiting the present invention. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and cannot be understood as indicating or implying relative importance.

[0029] In the description of the present invention, it should be noted that, unless otherwise clearly specified and limited, the terms "installation", "connection" and "connection" should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection, or it can be indirectly connected through an intermediate medium, or it can be the internal communication of two components. For ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.

[0030] Example 1

[0031] This embodiment provides a reactor for producing and processing zinc oxide, such as Figure 1 As shown, it includes a base 1, a reaction chamber 3 is fixedly installed on the top of the base 1, and an oxygen box 4 is fixedly installed on the top of the reaction chamber 3; the oxygen box 4 supplies oxygen to the reaction chamber 3. A feeding platform 2 is fixedly installed on the top of the base 1 and on the left side of the reaction chamber 3, and an inclined feeding chute is opened on the top of the feeding platform 2, and a zinc block is arranged on the feeding chute.

[0032] like Figure 2 As shown, a crushing assembly 5 is arranged inside the base 1, and the crushing assembly 5 includes a feed port 51 and a crushing device. An inclined feed port 51 is opened on the left side of the reaction bin 3. The zinc block enters the interior of the reaction bin 3 from the feed port along a parabolic trajectory, and the crushing device is located at the moving trajectory of the zinc block.

[0033] like Figure 2 and 3 As shown, the crushing device includes a main crushing roller 52 and an auxiliary crushing roller 55. The end of the main crushing roller 52 is fixedly connected to a motor through a rotating shaft. The main crushing roller 52 and the auxiliary crushing roller 55 are both provided with crushing teeth. The positions of the crushing teeth on the main crushing roller 52 and the auxiliary crushing roller 55 are staggered. The ends of the main crushing roller 52 and the auxiliary crushing roller 55 are both rotatably connected to the reaction chamber 3. Since the zinc block is large in size and is not easy to melt or evaporate, the zinc block is crushed by the main crushing roller 52 and the auxiliary crushing roller 55 so that the zinc block is broken into small particles, and the small particles melt quickly when heated.

[0034] like Figure 3 As shown, a first gear 53 is fixedly mounted on the end of the main crushing roller 52, and a second gear 54 is fixedly mounted on the end of the auxiliary crushing roller 55, and the first gear 53 is meshedly connected with the second gear 54. The main crushing roller 52 drives the first gear 53 to rotate, and the first gear 53 drives the second gear 54 and the auxiliary crushing roller 55 to rotate, so that the main crushing roller 52 and the auxiliary crushing roller 55 rotate in opposite directions, thereby increasing the crushing effect.

[0035] In this embodiment, the zinc block is crushed into small particles by the main crushing roller 52 and the first gear 53 to increase the heating area of ​​the zinc block and avoid the zinc block being too large, which causes the zinc block to melt and evaporate slowly, thereby reducing the oxidation efficiency of zinc oxide.

[0036] Example 2

[0037] Based on Example 1, this example proposes a reactor for producing and processing zinc oxide, such as Figure 4As shown, an oxygen supply assembly 6 is arranged inside the base 1, and the oxygen supply assembly 6 includes a heating plate 61, a lower oxygen pipe 62 and an upper oxygen pipe 63. The lower oxygen pipe 62 and the upper oxygen pipe 63 are both connected to the oxygen box 4, and the oxygen spray ports of the lower oxygen pipe 62 and the upper oxygen pipe 63 face the zinc block. Two lower oxygen pipes 62 and two upper oxygen pipes 63 are provided, and the ends of the lower oxygen pipes 62 and the upper oxygen pipes 63 are fixedly connected to the reaction chamber 3. The lower oxygen pipe 62 is located below the moving track of the zinc block, and the upper oxygen pipe 63 is located above the moving track of the zinc block. Spraying is performed from both sides of the zinc block through the lower oxygen pipe 62 and the upper oxygen pipe 63, so as to expand the contact area between the zinc block and oxygen and accelerate the oxidation efficiency.

[0038] The inner wall of the reaction chamber 3 is fixedly connected to the heating plate 61, and the heating plate 61 is located directly below the crushing device. A baffle is fixedly installed on the side of the reaction chamber 3 facing the heating plate 61, and the baffle is attached to the front and back sides of the heating plate 61. The baffle intercepts the zinc block falling from the crushing device to prevent the zinc block from falling below the heating plate 61. After the crushed zinc block falls on the heating plate 61, if the zinc block is not completely melted, the high-pressure oxygen sprayed from the lower oxygen pipe 62 will move the zinc particles that are not completely melted, and the zinc particles roll along the heating plate 61 to gradually melt and evaporate.

[0039] A collecting tray 64 is fixedly installed on the inner wall of the reaction chamber 3 and just below the rear end of the heating plate 61. A cooling pipe 65 is fixedly installed at the end of the collecting tray 64. A suction fan is rotatably connected inside the cooling pipe 65. The zinc oxide gas is sucked into the cooling pipe 65 by the suction fan to cool and solidify to form zinc oxide particles.

[0040] In this embodiment, the zinc blocks are broken by the breaking device and then thrown out to perform parabolic motion. The inertia of zinc blocks with different gravities is different, and the resulting parabolic motion trajectories are different, so that the zinc blocks gathered together are thrown into the air and separated, avoiding a large number of zinc blocks gathering together and heat not circulating, resulting in the zinc blocks located outside melting while the zinc blocks located inside not melting, affecting the melting efficiency. The lower oxygen pipe 62 and the upper oxygen pipe 63 are placed on both sides of the moving trajectory of the zinc blocks to increase the contact area between the zinc blocks and oxygen and accelerate the oxidation efficiency.

[0041] The above-mentioned specific embodiments are only several optional embodiments of the present invention. Based on the technical solution of the present invention and the relevant inspiration of the above-mentioned embodiments, those skilled in the art can make various alternative improvements and combinations to the above-mentioned specific embodiments.

Claims

1. A reactor for producing and processing zinc oxide, characterized in that: include: A base (1), a reaction chamber (3) is fixedly mounted on the top of the base (1), an oxygen box (4) is fixedly mounted on the top of the reaction chamber (3), and a feeding platform (2) for conveying zinc blocks is fixedly mounted on the top of the base (1) and on the left side of the reaction chamber (3); The crushing assembly (5) comprises a feed inlet (51) and a crushing device. The left side of the reaction bin (3) is provided with an inclined feed inlet (51). The zinc block enters the interior of the reaction bin (3) from the feed inlet (51) along a parabolic trajectory. The crushing device is located at the moving trajectory of the zinc block. The oxygen supply assembly (6) comprises a lower oxygen pipe (62) and an upper oxygen pipe (63), wherein two of the lower oxygen pipe (62) and two of the upper oxygen pipe (63) are provided, and the ends of the lower oxygen pipe (62) and the upper oxygen pipe (63) are fixedly connected to the reaction chamber (3), and the oxygen spray ports of the lower oxygen pipe (62) and the upper oxygen pipe (63) face the zinc block, and the lower oxygen pipe (62) and the upper oxygen pipe (63) are both connected to the oxygen box (4).

2. A reactor for producing and processing zinc oxide according to claim 1, characterized in that: The crushing device comprises a main crushing roller (52) and an auxiliary crushing roller (55), the main crushing roller (52) and the auxiliary crushing roller (55) are both provided with crushing teeth, the positions of the crushing teeth on the main crushing roller (52) and the auxiliary crushing roller (55) are staggered, and the ends of the main crushing roller (52) and the auxiliary crushing roller (55) are both rotatably connected to the reaction chamber (3).

3. A reactor for producing and processing zinc oxide according to claim 2, characterized in that: A first gear (53) is fixedly mounted on the end of the main crushing roller (52), and a second gear (54) is fixedly mounted on the end of the auxiliary crushing roller (55), and the first gear (53) is meshingly connected with the second gear (54).

4. The reactor for producing and processing zinc oxide according to claim 1, characterized in that: The oxygen supply component (6) further comprises a heating plate (61), the inner wall of the reaction chamber (3) is fixedly connected to the heating plate (61), the heating plate (61) is arranged at an angle, and the heating plate (61) is located directly below the crushing device.

5. A reactor for producing and processing zinc oxide according to claim 4, characterized in that: A collecting tray (64) is fixedly installed inside the right wall of the reaction chamber (3), a cooling pipe (65) is fixedly installed at the end of the collecting tray (64), and a suction fan is rotatably connected inside the cooling pipe (65).

6. A reactor for producing and processing zinc oxide according to claim 5, characterized in that: A baffle is fixedly mounted on one side of the reaction chamber (3) facing the heating plate (61), and the baffle is abutted against the front and back sides of the heating plate (61).

7. A reactor for producing and processing zinc oxide according to claim 6, characterized in that: The top of the feeding platform (2) is provided with an inclined feeding slideway.

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