Petroleum coke calcining apparatus with rotary calcination

Abstract

This utility model provides a petroleum coke calcination device with rotary calcination, belonging to the field of petroleum coke calcination technology. It includes a fixed plate and a fixed shell. The fixed shell is fixedly connected to the top of the fixed plate, and a calcination shell is rotatably connected to the inner side of the fixed shell. A first shielding shell is fitted into one side of the calcination shell, and a second shielding shell is fitted into the other side. Support plates are fixedly connected to the outer sides of both the first and second shielding shells. An air inlet pipe and a blower are both connected through one side of the first shielding shell. This utility model adds a first filter layer and a second filter layer to the exhaust shell. The first filter layer is made of multiple layers of filter cloth to intercept large particulate impurities inside the exhaust shell, and the second filter layer is made of activated carbon to intercept pollutants inside the exhaust shell, thereby completing the exhaust gas treatment.

Description

Technical Field

[0001] This utility model belongs to the field of petroleum coke calcination technology, and particularly relates to a petroleum coke calcination device with rotary calcination. Background Technology

[0002] Petroleum coke, a black or dark gray hard solid petroleum product, is often used in the steelmaking industry to produce ordinary power graphite electrodes. However, the existing petroleum coke production process often requires calcining the raw materials to complete the production of petroleum coke.

[0003] In existing technologies, such as patent publication number CN203545685U, there is a petroleum coke calcination device to solve the problem that in the existing production process of calcining petroleum coke using a rotary kiln, the surface area of ​​fine petroleum coke material in contact with air is relatively large, making it easily burned and carried away by flue gas, thus reducing the actual yield of petroleum coke calcination. The device includes a silo, a feeder, and a rotary kiln. The feed end of the rotary kiln is located below the end of the feeder's conveying mechanism. The device also includes a briquetting machine. The silo includes a granular silo and a fine silo. The discharge end of the granular silo is located above the feeder, and the discharge end of the fine silo is located above the feed end of the briquetting machine. The discharge end of the briquetting machine is also located above the feeder.

[0004] Existing petroleum coke calcination equipment lacks exhaust gas treatment components, making it impossible to filter and treat the polluting exhaust gas generated during calcination, thus affecting the user experience. Utility Model Content

[0005] To achieve the above objectives, the present invention adopts the following technical solution:

[0006] A petroleum coke calcining device with rotary calcination includes a fixed plate and a fixed shell. The fixed shell is fixedly connected to the top of the fixed plate, and a calcining shell is rotatably connected to the inner side of the fixed shell. A first shielding shell is fitted into one side of the calcining shell, and a second shielding shell is fitted into the other side of the calcining shell. Support plates are fixedly connected to the outer sides of both the first and second shielding shells, and the support plates are connected to the fixed plate. An air inlet pipe is penetrating through one side of the first shielding shell, and the air inlet pipe is located behind the support plate. A blower is penetrating through one side of the first shielding shell, and the blower is located in front of the support plate. An igniter is fixedly connected to the inner side of the first shielding shell.

[0007] Preferably, the top of the calcined shell is threaded with a shielding cover.

[0008] Preferably, the bottom of the fixing plate is fixedly connected with a support foot, and four support feet are provided.

[0009] Preferably, an output pipe is connected through the other side of the second shielding shell, and the output pipe is located above the support plate. An exhaust shell is fixedly connected to the tail end of the output pipe, and an exhaust fan is fixedly connected to the inner side of the exhaust shell.

[0010] Preferably, a first filter layer is fixedly connected to the inner side of the exhaust shell, and a second filter layer is fixedly connected to the inner side of the exhaust shell, with the second filter layer located above the first filter layer.

[0011] Preferably, a geared motor is fixedly connected to the other side of the fixed housing, and a transmission wheel is fixedly connected to the output end of the geared motor.

[0012] Preferably, a driven wheel is fixedly connected to the outer surface of the calcined shell, and the driven wheel meshes with the surface of the transmission wheel.

[0013] Preferably, the inner walls of the calcination shell, the first shielding shell, and the second shielding shell are all provided with a heat insulation layer.

[0014] Compared with the prior art, the present invention has the following advantages:

[0015] This invention adds a first filter layer and a second filter layer. The first filter layer is made of multiple layers of filter cloth to intercept large particulate impurities inside the exhaust shell. The second filter layer is made of activated carbon wrapped and connected to intercept pollutants inside the exhaust shell, thereby completing the treatment of exhaust gas.

[0016] This invention adds a geared motor, a transmission wheel, and a driven wheel. The geared motor transmits rotational power to the inside of the transmission wheel, which in turn transmits rotational power to the inside of the driven wheel. The driven wheel then drives the calcining shell to rotate, completing the rotary calcination of petroleum coke. Compared with the traditional calcination method, rotary calcination can make the raw materials heat evenly during calcination, thereby improving the calcination effect of petroleum coke.

[0017] This invention adds a heat insulation layer, which is made of heat insulation cotton. During the calcination of petroleum coke, it can block the rapid conduction of heat to the external environment, thereby reducing the energy consumption required for heating during the calcination process and improving the calcination effect of the device. Attached Figure Description

[0018] Figure 1 This is a schematic diagram of the structure of a petroleum coke calcining device with rotary calcination proposed in this utility model.

[0019] Figure 2 This is a schematic diagram of the back structure of a petroleum coke calcining device with rotary calcination proposed in this utility model.

[0020] Figure 3 This is a cross-sectional view of the connecting part of the calcined shell proposed in this utility model;

[0021] Figure 4 This is a cross-sectional view of the connecting part of the first shielding shell proposed in this utility model;

[0022] Figure 5 This is a cross-sectional view of the connecting part of the second shielding shell proposed in this utility model;

[0023] Figure 6 This is a schematic diagram of the connection structure of the geared motor proposed in this utility model;

[0024] Figure 7 This is a cross-sectional view of the connecting part of the exhaust shell proposed in this utility model.

[0025] In the diagram: 1. Fixing plate; 2. Fixing shell; 3. Calcination shell; 4. First shielding shell; 5. Second shielding shell; 6. Support plate; 7. Air inlet pipe; 8. Blower; 9. Ignition device; 10. Shielding cover; 11. Support foot; 12. Output pipe; 13. Exhaust shell; 14. Ventilation fan; 15. First filter layer; 16. Second filter layer; 17. Gear motor; 18. Transmission wheel; 19. Driven wheel. Detailed Implementation

[0026] The technical solution of this utility model will be further described below with reference to the accompanying drawings and embodiments.

[0027] Reference Figures 1-5A petroleum coke calcining device with rotary calcination includes a fixed plate 1 and a fixed shell 2. The fixed shell 2 is fixedly connected to the top of the fixed plate 1. The fixed plate 1 provides fixing points for the fixed shell 2, support plate 6, and support foot 11 fixedly connected to its outer surface. The fixed shell 2 provides connection points for the calcining shell 3 fitted inside it, and also provides fixing points for the geared motor 17 fixedly connected to its outer surface. The calcining shell 3 is rotatably connected to the inner side of the fixed shell 2. The calcining shell 3 is rotatably connected to the inner side of the fixed shell 2, providing calcination space for the raw materials injected inside it, and also provides fixing points for the first shielding shell 4, the second shielding shell 5, the shielding cover 10, and the driven wheel 19 connected to its outer surface. The first shielding shell 3 is fitted to one side of its outer surface. A first shielding shell 4 is fitted into the calcining shell 3, providing shielding on one side of the calcining shell 3 and providing fixing points for the air intake pipe 7, blower 8, and igniter 9, which are fixedly connected to its outer and inner surfaces. A second shielding shell 5 is fitted into the other side of the calcining shell 3, providing shielding on the other side and providing fixing points for the output pipe 12, which is fixedly connected to its outer surface. Support plates 6 are fixedly connected to the outer sides of both the first shielding shell 4 and the second shielding shell 5. The support plates 6 are connected to the first shielding shell 4 and the second shielding shell 5 respectively, and also to the fixing plate 1, thus fixing the first shielding shell 4 and the second shielding shell 5. The support plates 6 are connected to the fixing plate 1. Next, an air inlet pipe 7 is connected through one side of the first shielding shell 4. The air inlet pipe 7 is connected through one side of the first shielding shell 4 and connected to an external pipe to deliver gas to the inside of the calcining shell 3. The air inlet pipe 7 is located behind the support plate 6. A blower 8 is connected through one side of the first shielding shell 4. When air needs to be supplied to the inside of the calcining shell 3, electrical energy can be supplied to the blower 8 through an external control component. At this time, the blower 8 generates suction force on the air in the external environment and continuously delivers air to the inside of the calcining shell 3 to replenish the air in the calcining shell 3. The blower 8 is located in front of the support plate 6. An igniter 9 is fixedly connected to the inside of the first shielding shell 4. Inside the calcining shell 3, after the gas is delivered to the inside of the calcining shell 3, electrical energy can be delivered to the inside of the igniter 9 through an external control component. At this time, the igniter 9 generates an electric spark to ignite the gas and continuously conduct heat to the inside of the calcining shell 3. The top of the calcining shell 3 is threaded with a shielding cover 10, which provides shielding for the top of the calcining shell 3 and provides output space for petroleum coke inside the calcining shell 3. At the same time, it provides space for raw materials to be injected into the inside of the calcining shell 3. The bottom of the fixing plate 1 is fixedly connected with a support foot 11, which is fixedly connected to the bottom of the fixing plate 1. The support force transmitted to its interior through the ground provides support for the whole device, and four support feet 11 are provided.

[0028] Reference Figure 1 , Figure 2 and Figure 7 An output pipe 12 is connected through the other side of the second shielding shell 5. The output pipe 12 provides a fixing point for the exhaust shell 13, which is fixedly connected to its tail end. When the air pressure inside the calcining shell 3 is too high, the output pipe 12 delivers the exhaust gas to the interior of the exhaust shell 13. The output pipe 12 is located above the support plate 6. The exhaust shell 13 is fixedly connected to the tail end of the output pipe 12. The exhaust shell 13 is connected through the tail end of the output pipe 12, providing a fixing point for the ventilation fan 14, the first filter layer 15, and the second filter layer 16, which are fixedly connected to its inner side. At the same time, it provides space for the exhaust gas to be output to the external environment. The ventilation fan 14 is fixedly connected to the inner side of the exhaust shell 13. When it is necessary to output the exhaust gas, electrical energy can be transmitted through an external control component. The exhaust gas flows into the ventilation fan 14, where it draws in the exhaust gas from the output pipe 12 and the inner side of the calcining shell 3, and delivers the exhaust gas to the external environment to complete the exhaust gas output. A first filter layer 15 is fixedly connected to the inner side of the exhaust shell 13. The first filter layer 15 is made of multiple layers of filter cloth. When the exhaust gas is delivered into the interior of the exhaust shell 13, the first filter layer 15 intercepts large particulate impurities inside the exhaust shell 13. A second filter layer 16 is fixedly connected to the inner side of the exhaust shell 13. The second filter layer 16 is made of activated carbon. When the exhaust gas is delivered into the interior of the exhaust shell 13, the second filter layer 16 intercepts pollutants inside the exhaust shell 13, thereby completing the exhaust gas treatment. The second filter layer 16 is located above the first filter layer 15.

[0029] Reference Figure 1 , Figure 2 , Figure 3 and Figure 6 A geared motor 17 is fixedly connected to the other side of the fixed shell 2. When it is necessary to perform rotary calcination of the petroleum coke inside the calcination shell 3, electrical energy can be transmitted to the inside of the geared motor 17 through an external control component. At this time, the geared motor 17 transmits the rotational power to the inside of the transmission wheel 18. The output end of the geared motor 17 is fixedly connected to the transmission wheel 18. When the rotational power is transmitted to the inside of the transmission wheel 18 through the geared motor 17, the transmission wheel 18 rotates and transmits the rotational power to the inside of the driven wheel 19. The driven wheel 19 is fixedly connected to the outer surface of the calcination shell 3. When the rotational power is transmitted to the inside of the driven wheel 19 through the transmission wheel 18, the driven wheel 19 rotates, causing the calcination shell 3 to rotate and the petroleum coke to be calcined in a rotary manner. The driven wheel 19 meshes with the surface of the transmission wheel 18.

[0030] Reference Figures 3-5 The inner walls of the calcining shell 3, the first shielding shell 4, and the second shielding shell 5 are all equipped with heat insulation layers 20. The heat insulation layers 20 are made of heat insulation cotton. During the calcination of petroleum coke, they can block the rapid conduction of heat to the external environment, thereby reducing the energy consumption required for heating during the calcination process and improving the calcination effect of the device.

[0031] The functional principle of this utility model can be explained by the following operation: First, the raw material is injected into the inside of the calcining shell 3 by rotating the cover 10 with external force. Then, the cover 10 is fixed to the top of the calcining shell 3. Then, the air inlet pipe 7 is connected to the external pipe by external force. At this time, the air inlet pipe 7 delivers the gas to the inside of the calcining shell 3. The blower 8 generates suction to the air in the external environment and continuously delivers air to the inside of the calcining shell 3 to replenish the air in the calcining shell 3. The igniter 9 generates an electric spark to ignite the gas and continuously conduct heat to the inside of the calcining shell 3 to complete the calcination of petroleum coke. After the calcination is completed, the petroleum coke is removed by rotating the cover 10 again with external force to complete the output of petroleum coke.

[0032] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of this utility model and are not intended to limit it. Although this utility model has been described in detail with reference to preferred embodiments, those skilled in the art should understand that modifications or equivalent substitutions can be made to the technical solutions of this utility model without departing from the spirit and scope of the technical solutions of this utility model, and all such modifications or substitutions should be covered within the scope of the claims of this utility model.

Claims

1. Petroleum coke calcining plant with rotary calcination, comprising a fixed plate (1) and a fixed shell (2), characterized in that, A fixed shell (2) is fixedly connected to the top of the fixed plate (1). A calcining shell (3) is rotatably connected to the inner side of the fixed shell (2). A first shielding shell (4) is fitted to one side of the calcining shell (3). A second shielding shell (5) is fitted to the other side of the calcining shell (3). A support plate (6) is fixedly connected to the outer side of both the first shielding shell (4) and the second shielding shell (5). The support plate (6) is connected to the fixed plate (1). An air inlet pipe (7) is connected through one side of the first shielding shell (4). The air inlet pipe (7) is located behind the support plate (6). A blower (8) is connected through one side of the first shielding shell (4). The blower (8) is located in front of the support plate (6). A lighter (9) is fixedly connected to the inner side of the first shielding shell (4).

2. A petroleum coke calcining plant with rotary calcining according to claim 1, characterized in that, The top of the calcined shell (3) is threaded with a cover (10).

3. A petroleum coke calcining plant with rotary calcining as claimed in claim 1, wherein, The bottom of the fixed plate (1) is fixedly connected with a support foot (11), and there are four support feet (11).

4. A petroleum coke calcining plant with rotary calcination as claimed in claim 1, wherein, The other side of the second shielding shell (5) is connected to an output pipe (12), and the output pipe (12) is located above the support plate (6). The tail end of the output pipe (12) is fixedly connected to an exhaust shell (13), and the inner side of the exhaust shell (13) is fixedly connected to an air exchange fan (14).

5. A petroleum coke calcining plant with rotary calcining according to claim 4, characterized in that, The exhaust shell (13) is fixedly connected to the inner side of a first filter layer (15), and the exhaust shell (13) is fixedly connected to a second filter layer (16), with the second filter layer (16) located above the first filter layer (15).

6. A petroleum coke calcining plant with rotary calcination as claimed in claim 1, wherein, A geared motor (17) is fixedly connected to the other side of the fixed housing (2), and a transmission wheel (18) is fixedly connected to the output end of the geared motor (17).

7. A petroleum coke calcining plant with rotary calcining according to claim 6, characterized in that, A driven wheel (19) is fixedly connected to the outer surface of the calcined shell (3), and the driven wheel (19) meshes with the surface of the transmission wheel (18).

8. A petroleum coke calcining plant with rotary calcination as claimed in claim 1, wherein, The inner walls of the calcined shell (3), the first shielding shell (4), and the second shielding shell (5) are all provided with heat insulation layers (20).

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