High-temperature oxidation reaction anti-sintering reactor

Abstract

The utility model belongs to the technical field of reactors, and particularly relates to a high-temperature oxidation reaction anti-sintering reactor which comprises a feeding cavity and a reaction cavity, the feeding cavity and the reaction cavity are of a cylindrical structure, a plurality of gas distribution cylinders are evenly distributed on the periphery of the outer portion of the reaction cavity, the bottoms of the gas distribution cylinders are connected with gas inlet pipes, and a plurality of holes are formed in the inner sides of the gas distribution cylinders from top to bottom at intervals. According to the reaction chamber, gas enters the internal air caps in a uniform manner through the air distribution cylinder, the gas in the reaction chamber can form a cyclone when the gas is introduced, the air outlet directions in the air caps are consistent, and the gas moves in one direction, so that the reaction chamber is uniform in air distribution, and the reaction chamber is uniform in air distribution. The flowing air chamber provides upward air, the materials do suspension rotating rising motion in the reaction cavity, the materials can rotate in the reaction cavity in the rotating process, even if the external temperature is too high and reaches a sintering point, the sintered materials can be taken down under the motion of the materials, and sintering is prevented.

Description

Technical Field

[0001] The utility model belongs to the technical field of reactors, and in particular relates to a high-temperature oxidation reaction anti-sintering reactor. Background Art

[0002] When calcining anthracite vanadium to extract alum, the oxidation temperature required is relatively high. In order to make the material react better, we use suspended calcination to carry out the material reaction. However, the material reaction temperature is relatively high. When it reaches 900℃, the material will become hardened, eventually sticking to the inner wall of the reactor and continuing to grow and spread. Ultimately, it cannot reach the suspended state and blocks the reactor, making the reactor unusable and delaying normal production tests.

[0003] Existing reactors, such as Figure 1 As shown, the feed chamber and the reaction chamber are both rectangular structures, the overall material is 310S, the operating conditions are 1100 high temperature, the outside is a heating system, and the heat is conducted from the outside to the chamber to heat the material, so that it reacts with the gas to achieve the purpose of purification. However, during use, when the material reaches 1100 degrees, the material will cause high-temperature sintering at the right angles of the reaction chamber and on the outer wall of the entire reaction chamber. The reason is that when the heat is conducted, the temperature of the outer wall will be higher than the temperature of the internal chamber when the material passes through the outer wall. When the internal chamber reaches the reaction temperature, the outer wall often has a higher temperature, and the stone coal vanadium material will sinter. Utility Model Content

[0004] In view of the shortcomings of the existing technology, the present invention proposes a high-temperature oxidation reaction anti-sintering reactor, which aims to solve the problem of materials sintering and bonding to the inner wall of the reactor when in a high-temperature suspended state.

[0005] A high-temperature oxidation reaction anti-sintering reactor comprises a feed chamber and a reaction chamber, wherein the feed chamber is connected to the reaction chamber, a feed port is provided at the top of the feed chamber, and a discharge port is provided at the top side of the reaction chamber; a loose air chamber is provided at the bottom of the feed chamber, and a flow air chamber is provided at the bottom of the reaction chamber; the feed chamber and the reaction chamber are cylindrical structures, a plurality of sub-cylinders are evenly distributed around the outside of the reaction chamber, the bottom of the sub-cylinders is connected to the air inlet pipe, a plurality of holes are provided on the inner sides of the plurality of sub-cylinders from top to bottom at intervals, the holes on each sub-cylinder are provided in the same position, a hood is provided at the hole, and the air outlet directions of the plurality of hoods are consistent.

[0006] A dome-shaped cap is provided on the top of the reaction chamber.

[0007] The beneficial effects of the utility model are as follows:

[0008] The reaction chamber of the present invention is evenly distributed with multiple gas distribution cylinders around the outside, and the gas is uniformly introduced into the internal wind cap through the gas distribution cylinders. When the gas is introduced, the gas inside the reaction chamber can form a cyclone. The gas outlet direction in the gas cap is consistent, the gas moves in one direction, and the flow air chamber provides upward gas. The material performs a suspended, rotating and ascending movement inside the reaction chamber. During the rotation process, the material will rotate inside, so that even if the external temperature is too high and reaches the sintering point, the sintered material will be brought down by the movement of the material to prevent the occurrence of sintering. At the same time, the feed chamber and the reaction chamber are cylindrical structures, and the top of the reaction chamber is provided with a dome-type cap, which also prevents the sintered material from sticking to the corners of the feed chamber and the reaction chamber. BRIEF DESCRIPTION OF THE DRAWINGS

[0009] Figure 1 It is a structural schematic diagram of an existing high-temperature oxidation reactor;

[0010] Figure 2 This is a schematic structural diagram of a high-temperature oxidation reaction anti-sintering reactor of the utility model;

[0011] Figure 3 This is a schematic diagram of the gas outlet direction of a gas cap of a high-temperature oxidation reaction anti-sintering reactor of the present invention;

[0012] In the attached figure: 1. Feed chamber; 2. Reaction chamber; 3. Loose air chamber; 4. Flow air chamber; 5. Cap; 6. Discharge port; 7. Air cylinder; 8. Air inlet pipe; 9. Air hood; 10. Feed port. DETAILED DESCRIPTION

[0013] The present invention will be described in detail below with reference to the accompanying drawings.

[0014] like Figure 2-3As shown, a high-temperature oxidation reaction anti-sintering reactor includes a feed chamber 1 and a reaction chamber 2. The feed chamber 1 is connected to the reaction chamber 2. A feed port 10 is provided on the top of the feed chamber 1, and a discharge port 6 is provided on the top side of the reaction chamber 2; a loosening air chamber 3 is provided at the bottom of the feed chamber 1, and the wind in the loosening air chamber 3 will keep the material in a suspended state to prevent the material from directly accumulating and causing the material to be unable to flow; a flow air chamber 4 is provided at the bottom of the reaction chamber 2 to make the material in the reaction chamber 2 flow; the feed chamber 1 and the reaction chamber 2 are cylindrical structures, and a dome-shaped cap 5 is provided on the top of the reaction chamber 2 to prevent the material from accumulating on the inner wall and cap of the feed chamber 1 and the reaction chamber 2, and a plurality of gas distribution holes are evenly distributed around the outside of the reaction chamber 2. Cylinder 7, the bottom of the sub-cylinder 7 is connected to the air inlet pipe 8, and the gas enters the sub-cylinder 7 through the air inlet pipe 8. The gas can be evenly delivered to the reaction chamber 2 through the sub-cylinder 7, and due to the existence of the sub-cylinder 7, the temperature of the outer wall of the reaction chamber 2 and the internal chamber becomes closer, which indirectly increases the inlet temperature of the compressed air and saves resources; multiple holes are provided on the inner side of the multiple sub-cylinders 7 from top to bottom, and the positions of the holes on each sub-cylinder 7 are consistent. Wind caps 9 are set at the holes, and the air outlet directions of the multiple wind caps 9 are consistent. The air outlet direction of the wind caps is opened in a clockwise or counterclockwise direction as needed, so that the material has a rotational force when in suspension, so that the material does not stick to the inner wall of the reaction chamber 2.

[0015] After the material is discharged through the discharge port 6, the internal wind cap 9 can be opened, and the gas enters the gas distribution cylinder 7 through the air inlet pipe 8. The gas distribution cylinder 7 uniformly enters the internal wind cap 9, and the gas outlet direction in the gas cap 9 is consistent. When the gas is introduced, the gas inside the reaction chamber 2 can form a cyclone. The gas moves in one direction, and the flow air chamber 4 provides upward gas, and the material performs a suspended, rotating and rising movement inside the reaction chamber 2. In this way, even if the external temperature is too high and reaches the sintering point, the sintered material will be brought down under the movement of the material to prevent sintering. At the same time, the feed chamber 1 and the reaction chamber 2 are cylindrical structures, and the top of the reaction chamber 2 is provided with a dome-shaped cap 5, which also prevents the material from sintering and sticking to the corners of the feed chamber 1 and the reaction chamber 2.

Claims

1. A high-temperature oxidation reaction anti-sintering reactor, comprising a feed chamber and a reaction chamber, wherein the feed chamber is connected to the reaction chamber, a feed port is provided at the top of the feed chamber, and a discharge port is provided at the top side of the reaction chamber; a loose air chamber is provided at the bottom of the feed chamber, and a flow air chamber is provided at the bottom of the reaction chamber, characterized in that: The feed chamber and reaction chamber are cylindrical structures, and multiple sub-cylinders are evenly distributed around the outside of the reaction chamber. The bottom of the sub-cylinder is connected to the air intake pipe. Multiple holes are opened on the inner side of the multiple sub-cylinders from top to bottom. The positions of the holes on each sub-cylinder are consistent, and wind hoods are set at the holes. The air outlet directions of the multiple wind hoods are consistent.

2. The high-temperature oxidation reaction anti-sintering reactor according to claim 1, characterized in that: A dome-shaped cap is provided on the top of the reaction chamber.

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