High-pressure aerodynamic spiral dehydrator

Abstract

The high-pressure aerodynamic force spiral dehydrator comprises a base, a box body is arranged at the upper end of the base, a semicircular baffle is arranged in the box body, inclined plates are arranged on the two sides of the semicircular baffle, a feeding port is formed in the upper end of the left side of the box body, and a discharging port is formed in the side wall of the right side of the box body. A main rotating shaft is rotatably connected to the left side wall of the box body in a penetrating mode, a main driving shaft is rotatably connected between the left side inner wall of the box body and the discharging port, a spiral linear air outlet is formed in the outer wall of the main driving shaft, and the main rotating shaft is connected with the main driving shaft. According to the spiral dehydrator, the main driving shaft drives the discontinuous crossed bolt and the continuous screw to rotate, so that the discontinuous crossed bolt and the continuous screw push a mixture forwards to generate relative motion, solid and liquid are separated through the spiral structure of the spiral dehydrator, and the spiral dehydrator is equipment for realizing solid-liquid separation of high-humidity materials by utilizing extrusion of the spiral blade.

Description

Technical Field

[0001] The utility model relates to the technical field of spiral dehydrators, in particular to a high-pressure pneumatic power spiral dehydrator. Background Art

[0002] Industrial dehydrators generally have a three-foot suspended swing structure. Springs are installed on the three feet to avoid vibration caused by unbalanced load. The inner and outer shells are made of refined stainless steel plates, which are firm and durable. Braking generally adopts a braking opening and closing arm device, with good braking performance, safety and reliability. It uses triangular belt drive. The motor drives the starting wheel, and it starts slowly to the normal speed, running smoothly without vibration.

[0003] The spiral dehydrators in the prior art generally dehydrate the mixture by rotating. However, this dehydration device cannot move the mixture, but only separates the solid and liquid of the mixture, reducing the adaptability of the device. Moreover, when the existing dehydrators are operating, the friction between the mixture and the device is relatively large, and efficient dehydration of the mixture cannot be achieved. Summary of the Utility Model

[0004] The purpose of the utility model is to solve the defects existing in the prior art. The intermittent cross bolts and the continuous spiral are driven by the main drive shaft to push the mixture forward, generating relative movement. And through its own spiral structure, the solid and liquid are separated. The spiral dehydrator is a device that uses the extrusion of spiral blades to realize the solid-liquid separation of high-moisture materials, and a high-pressure pneumatic power spiral dehydrator is proposed.

[0005] In order to achieve the above purpose, the utility model adopts the following technical scheme:

[0006] A high-pressure pneumatic power spiral dehydrator, including a base. A box body is provided at the upper end of the base. A semi-circular baffle is provided inside the box body. Inclined plates are provided on both sides of the semi-circular baffle. A feed inlet is opened at the upper left end of the box body. A discharge outlet is opened on the side wall of the right side of the box body. A main rotating shaft is rotatably connected through the side wall of the left side of the box body. A main drive shaft is rotatably connected between the inner wall of the left side of the box body and the discharge outlet. A spiral linear air outlet is opened on the outer wall of the main drive shaft. The main rotating shaft is connected to the main drive shaft. A pushing mechanism for pushing the mixture is provided on the outer wall of the main drive shaft. A driving mechanism for driving the pushing mechanism is provided at the upper end of the base.

[0007] Preferably, the pushing mechanism includes an intermittent cross spiral and a continuous spiral provided on the outer wall of the main drive shaft. The ratio of the part of the intermittent cross spiral and the continuous spiral on the outer wall of the main drive shaft is 3:1.

[0008] Preferably, the driving mechanism includes a speed reducer disposed at the upper end of the base. The output end of the speed reducer is connected to the main rotating shaft through a shaft coupling. An coupling cover is provided at the upper end of the base, and the shaft coupling is located within the coupling cover.

[0009] Preferably, an installation block is provided at the upper end of the base. A spring washer is provided at the upper end of the installation block, and a power motor is provided at the upper end of the spring washer. A rotating shaft is provided at the end of the output shaft of the power motor. Transmission belt pulleys are provided on the outer walls of the rotating shaft and the input end of the speed reducer. The two transmission belt pulleys are connected by belt drive, and a belt pulley cover is sleeved between the two transmission belt pulleys.

[0010] Preferably, a cavity is formed within the main drive shaft, and an air compressor is provided outside the base. The output end of the air compressor is communicated with the cavity.

[0011] Preferably, a plurality of circumferentially arranged through slots are formed at the lower end of the semi-circular baffle, and a drain port is provided at the lower end of the box body.

[0012] Advantages of the present utility model:

[0013] 1. The intermittent cross bolts and the continuous spiral are driven by the main drive shaft to rotate, so that the two push the mixture forward to generate relative movement, and the solid and liquid are separated by their own spiral structures. The screw dehydrator is a device that realizes the solid-liquid separation of high-moisture materials by the extrusion of screw blades.

[0014] 2. By forming a layer of tiny bubbles on the surface of the spiral, these bubbles can change the way the material contacts the spiral, reduce friction, and thus reduce the resistance of the speed reducer and increase the effective torque. During the continuous generation and rupture of the bubbles, a passage will be formed by the main drive shaft, and the free water will also drain along the passage, thereby realizing efficient dehydration of the material. Description of the Drawings

[0015] Figure 1 is a top view schematic diagram of the overall structure of the present utility model;

[0016] Figure 2 is a side view schematic diagram of the overall structure of the present utility model;

[0017] Figure 3 is a side view sectional schematic diagram of the overall structure of the present utility model;

[0018] Figure 4 is a sectional top view schematic diagram of the overall structure of the present utility model.

[0019] In the figure: 1 base, 2 mounting block, 3 spring washer, 4 power motor, 5 rotating shaft, 6 speed reducer, 7 pulley cover, 8 main rotating shaft, 9 coupling cover, 10 box body, 11 discharge port, 12 drain port, 13 main drive shaft, 14 cavity, 15 semi-circular baffle, 16 through slot, 17 drive pulley, 18 shaft coupling, 19 intermittent cross helix, 20 air compressor, 21 continuous helix, 22 feed port. Specific implementation manner

[0020] Next, the technical solutions in the embodiments of the present invention will be clearly and completely described in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments.

[0021] In the description of the present invention, it should be understood that the orientation or positional relationship indicated by the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", "outer", etc. is based on the orientation or positional relationship shown in the accompanying drawings, and is 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 should not be construed as a limitation to the present invention.

[0022] Refer to Figures 1-4 , the high-pressure pneumatic power spiral dewatering machine includes a base 1. An upper end of the base 1 is provided with a box body 10. A semi-circular baffle 15 is provided inside the box body 10. Both sides of the semi-circular baffle 15 are provided with inclined plates. A feed port 22 is opened at an upper end of a left side of the box body 10. A discharge port 11 is opened on a side wall of a right side of the box body 10. A main rotating shaft 8 is rotatably connected through a side wall of a left side of the box body 10. A main drive shaft 13 is rotatably connected between an inner wall of a left side of the box body 10 and the discharge port 11. A spiral-shaped air outlet is opened on an outer wall of the main drive shaft 13. The main rotating shaft 8 is connected to the main drive shaft 13. A pushing mechanism for pushing the mixture is provided on an outer wall of the main drive shaft 13. The pushing mechanism includes an intermittent cross helix 19 and a continuous helix 21 provided on the outer wall of the main drive shaft 13. The ratio of the proportion of the intermittent cross helix 19 and the continuous helix 21 on the outer wall of the main drive shaft 13 is 3:1. By driving the intermittent cross bolt 19 and the continuous helix 21 to rotate through the main drive shaft 13, the two push the mixture forward, generating relative movement, and separating the solid and the liquid through their own spiral structures. The spiral dewatering machine is a device that realizes the solid-liquid separation of high-moisture materials by the extrusion of spiral blades.

[0023] An upper end of the base 1 is provided with a driving mechanism for driving the pushing mechanism. The driving mechanism includes a speed reducer 6 provided at an upper end of the base 1. An output end of the speed reducer 6 is connected to the main rotating shaft 8 through a shaft coupling 18. An upper end of the base 1 is provided with a coupling cover 9. The shaft coupling 18 is located inside the coupling cover 9.

[0024] At the upper end of the base 1, there is an installation block 2. At the upper end of the installation block 2, there is a spring washer 3. At the upper end of the spring washer 3, there is a power motor 4. At the end of the output shaft of the power motor 4, there is a rotating shaft 5. Both the outer wall of the input end of the rotating shaft 5 and the speed reducer 6 are provided with transmission belt pulleys 17. The two transmission belt pulleys 17 are connected by belt drive, and a belt pulley cover 7 is sleeved between the two transmission belt pulleys 17.

[0025] A cavity 14 is formed inside the main drive shaft 13. An air compressor 20 is provided outside the base 1. The output end of the air compressor 20 is communicated with the cavity 14. By forming a layer of tiny bubbles on the spiral surface, these bubbles can change the way the material contacts the spiral, reduce friction, and thus reduce the resistance of the speed reducer 6 and increase the effective torque. During the continuous generation and rupture of the bubbles, a passage will be formed by the main drive shaft 13, and the free water will also drain along the passage, thereby achieving efficient material dehydration.

[0026] At the lower end of the semi-circular baffle 15, a plurality of circumferentially arranged through grooves 16 are formed, and a drain port 12 is provided at the lower end of the box body 10.

[0027] When the utility model is in use, the solids in the mixture are separated by using the rotational movement of the main drive shaft 13. Specifically, the mixture first enters the inside of the screw dehydrator through the feed port 22. Inside, the main drive shaft 13 drives the intermittent cross bolts 19 and the continuous screw 21 to rotate, causing the two to push the mixture forward, generating relative movement, and separating the solid from the liquid through its own screw structure. The screw dehydrator is a device that uses the extrusion of screw blades to achieve solid-liquid separation of high-moisture materials. The moisture content of the material after being processed by the screw dehydrator is approximately around 60% - 70%.

[0028] To further reduce the moisture content of the processed material, the main drive shaft 13 of the screw dehydrator is changed from a solid shaft to a hollow shaft and spiral linear air outlets are opened, and medium-pressure air (1.6 MPa) is introduced to release bubbles, forming a layer of bubble film, thereby reducing the frictional resistance between the material and the spiral surface. This technology forms a layer of tiny bubbles on the spiral surface. These bubbles can change the way the material contacts the spiral, reduce friction, and thus reduce the resistance of the speed reducer 6 and increase the effective torque. During the continuous generation and rupture of the bubbles, a passage will be formed by the main drive shaft 13, and the free water will also drain along the passage, thereby achieving efficient material dehydration.

[0029] The above is only the preferred specific implementation manner of the utility model, but the protection scope of the utility model is not limited thereto. Any person skilled in the art within the technical scope disclosed by the utility model, according to the technical solution of the utility model and its inventive concept, makes equivalent substitutions or changes, and all should be covered within the protection scope of the utility model.

Claims

1. A high pressure pneumatic screw dehydrator, comprising a base (1), characterized in that: A box body (10) is provided at the upper end of the base (1), a semicircular baffle (15) is provided inside the box body (10), and inclined plates are provided on both sides of the semicircular baffle (15). A feed port (22) is provided at the upper left end of the box body (10), and a discharge port (11) is provided at the right side wall of the box body (10). A main rotating shaft (8) is rotatably connected to the left side wall of the box body (10), and a main driving shaft (13) is rotatably connected between the left inner wall of the box body (10) and the discharge port (11). A spiral air outlet is provided on the outer wall of the main driving shaft (13), and the main rotating shaft (8) is connected to the main driving shaft (13). A driving mechanism for driving the driving mechanism is provided on the outer wall of the main driving shaft (13). A driving mechanism for driving the driving mechanism is provided at the upper end of the base (1).

2. The high-pressure pneumatic screw dehydrator according to claim 1, characterized in that: The pushing mechanism comprises an intermittent cross spiral (19) and a continuous spiral (21) arranged on the outer wall of the main driving shaft (13), and the ratio of the intermittent cross spiral (19) and the continuous spiral (21) located on the outer wall of the main driving shaft (13) is 3:

1.

3. The high-pressure pneumatic screw dehydrator according to claim 2, characterized in that: The driving mechanism comprises a reducer (6) arranged at the upper end of the base (1); the output end of the reducer (6) is connected to the main rotating shaft (8) via a rotating shaft coupling (18); a coupling cover (9) is provided at the upper end of the base (1); and the rotating shaft coupling (18) is located inside the coupling cover (9).

4. The high-pressure pneumatic screw dehydrator according to claim 3, characterized in that: The upper end of the base (1) is provided with a mounting block (2), the upper end of the mounting block (2) is provided with a spring washer (3), the upper end of the spring washer (3) is provided with a power motor (4), the end of the output shaft of the power motor (4) is provided with a rotating shaft (5), the rotating shaft (5) and the outer wall of the input end of the reducer (6) are both provided with a driving pulley (17), the two driving pulleys (17) are connected by belt transmission, and a pulley cover (7) is sleeved between the two driving pulleys (17).

5. The high pressure pneumatic screw dehydrator according to claim 4, characterized in that: A cavity (14) is provided in the main drive shaft (13), an air compressor (20) is provided outside the base (1), and an output end of the air compressor (20) is connected to the cavity (14).

6. The high-pressure pneumatic screw dehydrator according to claim 5, characterized in that: The lower end of the semicircular baffle (15) is provided with a plurality of circumferentially arranged through grooves (16), and the lower end of the box body (10) is provided with a drainage port (12).

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