Receiving tank

By adding a reinforcement ring to the feed tank of the gas-solid separator and designing a cyclone gas separation structure, the problem of safety hazards of traditional devices is solved, and more efficient impurity separation and gas purification are achieved.

CN222489459UActive Publication Date: 2025-02-18JIANGSU CLASSIC ENERGY EQUIP
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Patent Information

Application Number
CN202421166273.9
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-05-27
Publication Date
2025-02-18
Estimated Expiration
2034-05-27

AI Technical Summary

Technical Problem

Traditional gas-solid separators lack reinforcement when connecting the upper and lower devices, resulting in easy pouring after a long period of use, which poses safety hazards.

Method used

A feed receiving tank is designed to enhance the connection strength by adding a reinforcement ring between the upper cylinder and the sealing head, and a limiting plate and a through-hole plate are provided in the drainage inner cylinder to form a cyclone gas to separate impurities.

Benefits of technology

It effectively prevents the pouring between the upper cylinder and the cylinder, improves the safety of the equipment, and improves the purity of the gas through secondary separation, and meets the emission standards.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the field of gas impurity removal equipment, and discloses a material receiving tank which comprises a separation structure, a gas inlet structure and a barrel, a gas inlet is located between the separation structure and the barrel, the separation structure comprises a filter element located in an upper barrel, the gas inlet comprises a gas inlet connecting pipe and a drainage inner barrel, and the drainage inner barrel is located in the upper barrel. A limiting plate is arranged in the drainage inner cylinder, the air inlet connecting pipe is located on the side edge of the upper cylinder body, and a reinforcing ring is further connected between the upper cylinder body and the end socket on the upper portion of the cylinder body. Impurity-containing gas forms rotational flow through the drainage inner cylinder, the impurity-containing gas is primarily separated firstly, so that some large impurity particles fall off, the upper portion of the drainage inner pipe is arranged in the upper cylinder body, the lower portion of the drainage inner pipe is arranged in the cylinder body, and impurities rapidly fall off from the drainage inner cylinder and then fall off the lower cylinder body. The reinforcing ring is reinforced between the upper barrel body and the end socket, so that the upper barrel body is prevented from being separated from the end socket of the barrel body after being used for a long time, and the overall safety of the receiving tank is improved.
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Description

Technical Field

[0001] The utility model relates to the field of gas impurity removal equipment, in particular to a receiving tank. Background Art

[0002] After use, the gas will carry catalysts or other particulate impurities. According to emission requirements, it cannot be discharged directly into the air. In addition, some impurities in the gas, such as catalysts, can be recycled and reused, so it is necessary to separate the impure gas.

[0003] When traditional devices are used to separate impure gases, there is a risk of tipping over because the upper device and the lower device are not reinforced when connected.

[0004] In the prior art document CN202020719788, a gas-solid separator and a gas-solid separation system are disclosed, wherein the gas-solid separator includes: an outer cylinder, the outer cylinder is provided with a discharge port; a discharge pipe, the discharge pipe is connected to the discharge port; a stirring device, the stirring device is arranged at the discharge port or is entirely arranged in the discharge pipe, so as to crush the solid particles separated by the gas-solid separator. In this structural device, there is no reinforcement device between the outer cylinder and the stirring device. After long-term use, the outer cylinder is prone to tipping over, which is dangerous.

[0005] Therefore, a new technical solution is needed to solve the above technical problems. Summary of the invention

[0006] In order to solve the above problems, the utility model discloses a receiving tank, which can effectively avoid the tilting between the upper cylinder and the cylinder, and can quickly separate impurities.

[0007] The technical solution of the utility model is: a receiving tank, comprising a separation structure, a gas inlet structure and a cylinder, the gas inlet is located between the separation structure and the cylinder, the separation structure comprises a filter element located in the upper cylinder, the gas inlet comprises an air inlet pipe and a drainage inner cylinder, the drainage inner cylinder is located in the upper cylinder, a limiting plate parallel to the diameter direction is provided inside the drainage inner cylinder, the air inlet pipe is located on the side of the upper cylinder, and a reinforcement ring is connected between the upper cylinder and the head on the upper part of the cylinder.

[0008] By adopting the above technical solution, the impure air flow enters the drainage inner cylinder through the air inlet pipe, some larger impurity particles fall into the lower cylinder below the cylinder, and then fall out of the lower cylinder, and some smaller particles are separated from the filter element in the cylinder, and finally the impure gas is purified.

[0009] Preferably, the air inlet pipe passes through the upper cylinder, one end of which is located outside the upper cylinder, the upper cylinder is wrapped with an insulation ring I, and the other end is located inside the drainage inner cylinder, and the air inlet pipe is connected to the external impure gas.

[0010] By adopting the above technical solution, the air inlet pipe is connected to the external impurity-containing gas, and the impurity-containing gas enters the drainage inner cylinder from the air inlet pipe to form a swirling gas, so that a part of the larger particle impurities are separated from the drainage inner cylinder and then fall from the cylinder into the lower cylinder.

[0011] Preferably, the drainage inner tube is in an I-shape as a whole, the upper part of the drainage inner tube is located below the filter element, the middle part of the drainage inner tube is in a straight tube shape, and the lower part of the drainage inner tube is in an outward trumpet shape, and the trumpet shape of the lower part of the drainage inner tube is located inside the cylinder.

[0012] By adopting the above technical solution, the shape of the drainage inner cylinder is convenient for forming swirling gas, so that the gas and solid in the impurity-containing gas are separated, forming a preliminary separation of the impurity-containing gas, and separating out larger particle impurities.

[0013] Preferably, the cylinder is cylindrical, and is wrapped with an insulation ring II outside the cylinder. An ear-type support is also provided at the upper position of the cylinder, and an electrostatic grounding plate is also provided on the ear-type support. A reserved opening is provided on the cylinder above the ear-type support.

[0014] By adopting the above technical solution, the insulation ring can keep the cylinder body warm, the ear-type support is easy to install, and when the staff touches the receiving tank, the electrostatic grounding plate can prevent the entire receiving tank from generating static electricity.

[0015] Preferably, the limiting plate is located in the straight cylinder in the middle of the drainage inner cylinder, and the limiting plate is provided with a through hole, the diameter of the through hole is much larger than the diameter of the solid in the impurity-containing gas.

[0016] By adopting the above technical solution, the limiting plate is a through-hole plate, which will not hinder the upward movement of impurities and play a role in preventing the filter element from falling.

[0017] Preferably, the top and bottom of the cylinder are the head and the lower cylinder respectively. The lower cylinder as a whole presents a cone with a larger top and a smaller bottom. The angle of the cone is 30-50°. The bottom of the lower cylinder is connected by a discharge pipe and a connecting flange. The connecting flange is connected to an external impurity solid collection barrel. A safety valve port and a lifting ear are provided on the head. The head is wrapped with a head insulation ring. A thermometer port pipe is provided on the side of the lower cylinder.

[0018] By adopting the above technical solution, the lower cylinder is in a downward cone shape, so when impurities fall downward, they can directly fall down along the inner side of the cone-shaped lower cylinder, which can prevent the impurities from accumulating in the lower cylinder and falling directly downward.

[0019] Preferably, the filter element is located on the connecting plate at the top of the upper cylinder, an upper head cover is provided on the top of the upper cylinder, the upper cylinder and the upper head cover are connected by a flange, a stud and a nut, and a positioning pin is provided on the stud.

[0020] By adopting the above technical solution, the filter element can further separate the impurity-containing gas, and the upper cylinder and the cylinder are fixed to prevent displacement between the upper cylinder and the cylinder.

[0021] Preferably, a backflush distributor is provided above the filter element in the upper head cover, a gas outlet is provided at the top of the upper head cover, a backflush gas storage tank is connected to the gas outlet, and a pressure difference port is provided on the side of the gas outlet.

[0022] The benefits of the utility model are as follows: 1. The utility model forms a vortex of impurity-containing gas through the drainage inner cylinder, and can first perform preliminary separation of the impurity-containing gas, so that some larger impurity particles fall down, and perform preliminary separation of the impurity-containing gas. The upper part of the drainage inner tube is arranged in the upper cylinder body, and the lower part is arranged in the cylinder body, so that impurities separated from the gas can be quickly dropped from the drainage inner cylinder into the lower cylinder body.

[0023] 2. The utility model provides a reinforcing ring between the upper cylinder and the head, which can strengthen the connection strength between the upper cylinder and the head, prevent the upper cylinder and the head from being separated after a long period of use, and improve the overall safety of the receiving tank.

[0024] 3. The utility model can perform secondary separation on impure gases, effectively improve the purity of the discharged gases, protect the environment, and meet emission standards. BRIEF DESCRIPTION OF THE DRAWINGS

[0025] Figure 1 It is a structural schematic diagram of the utility model;

[0026] Figure 2 For this utility model Figure 1 A structural diagram of the enlarged view of part A;

[0027] Figure 3 This is a schematic diagram of the structure of the limit plate of the utility model;

[0028] Figure 4 It is a schematic structural diagram of a top view of the utility model.

[0029] Among them: 1. connecting flange, 2. discharge pipe, 3. lower cylinder, 4. thermometer port pipe, 5. limit plate, 5-1, through hole, 6. gas outlet, 7. cylinder, 8. pressure difference port, 9. ear support, 10. electrostatic grounding plate, 11. reserved port, 12. insulation ring II, 13. head, 14. reinforcement ring, 15. air inlet pipe, 16. drainage inner cylinder, 17. upper cylinder, 18. filter element, 19. head insulation ring, 20. lifting ear, 21. stud, 22. nut, 23. safety valve port, 24. backflush gas storage tank, 25. insulation ring I, 26. positioning pin, 27. upper head cover, 28. backflush distributor. DETAILED DESCRIPTION

[0030] The technical solutions in the embodiments of the present invention will be described clearly and completely below in conjunction with the accompanying drawings in the embodiments of the present invention.

[0031] like Figure 1-4 As shown, the receiving tank includes a separation structure, a gas inlet structure and a cylinder 7. The gas inlet is located between the separation structure and the cylinder 7. The separation structure includes a filter element 18 located in the upper cylinder 17. The gas inlet includes an air inlet pipe 15 and a drainage inner cylinder 16. The drainage inner cylinder 16 is located in the upper cylinder 17. The interior of the drainage inner cylinder 16 is provided with a limit plate 5 parallel to the diameter direction. The air inlet pipe 15 is located on the side of the upper cylinder 17. A reinforcement ring 14 is also connected between the upper cylinder 17 and the head 13 on the upper part of the cylinder 7. The impure airflow enters the drainage inner cylinder 16 through the air inlet pipe 15, and some larger impurity particles fall into the lower cylinder 3 below the cylinder 7, and then fall out from the lower cylinder 3. Some smaller particles are separated from the filter element 18 in the cylinder 7, and finally the impure gas is purified.

[0032] The air inlet pipe 15 passes through the upper cylinder 17, one end of which is located outside the upper cylinder 17, and the upper cylinder 17 is wrapped with an insulation ring I25, and the other end is located inside the drainage inner cylinder 16. The air inlet pipe 15 is connected to the external impurity-containing gas. The air inlet pipe 15 is connected to the external impurity-containing gas, and the impurity-containing gas enters the drainage inner cylinder 16 from the air inlet pipe 15 to form a swirling gas, so that a part of the larger particle impurities are separated from the drainage inner cylinder 16, and then fall from the cylinder 7 into the lower cylinder 3.

[0033] The drainage inner tube 16 is in an I-shape as a whole, the upper part of the drainage inner tube 16 is located below the filter element 18, the middle part of the drainage inner tube 16 is in a straight tube shape, and the lower part of the drainage inner tube 16 is in an outward trumpet shape. The trumpet shape of the lower part of the drainage inner tube 16 is located in the cylinder 7. The shape of the drainage inner tube 16 is convenient for forming a swirling gas, so that the gas-solid separation in the impurity-containing gas is achieved, forming a preliminary separation of the impurity-containing gas, and separating larger particle impurities.

[0034] The cylinder 7 is cylindrical and is wrapped with an insulation ring II12. An ear-type support 9 is also provided on the upper part of the cylinder 7. An electrostatic grounding plate 10 is also provided on the ear-type support 9. A reserved opening is provided on the cylinder 7 above the ear-type support 9. The insulation ring can keep the cylinder 7 warm. The ear-type support 9 is easy to install. When the staff touches the receiving tank, the electrostatic grounding plate 10 can prevent the receiving tank from generating static electricity as a whole.

[0035] The limit plate 5 is located in the straight cylinder in the middle of the drainage inner cylinder 16. The limit plate 5 is provided with a through hole 5-1. The diameter of the through hole 5-1 is much larger than the diameter of the solid in the impurity-containing gas. The through hole of the limit plate 5 is as large as possible as long as the filter element is not allowed to fall. The limit plate 5 is a through-hole plate and will not hinder the upward movement of impurities, thereby preventing the filter element 18 from falling.

[0036] The top and bottom of the cylinder 7 are the head 13 and the lower cylinder 3 respectively. The lower cylinder 3 as a whole presents a cone with a larger top and a smaller bottom. The angle of the cone is 30-50°. The bottom of the lower cylinder 3 is connected to the connecting flange 1 through a discharge pipe 2. The connecting flange 1 is connected to the external impurity solid collection bucket. The head 13 is provided with a safety valve port 23 and a lifting ear 20. The head 13 is wrapped with a head insulation ring 19. The side of the lower cylinder 3 is provided with a thermometer port pipe 4. The lower cylinder 3 is in a downward cone. When impurities fall downward, they can directly fall down along the inner side of the tapered lower cylinder 3. This can prevent the impurities from accumulating in the lower cylinder 3 and falling directly downward.

[0037] The filter element 18 is located on the connecting plate at the top of the upper cylinder 17. An upper head cover 27 is provided on the top of the upper cylinder 17. The upper cylinder 17 and the upper head cover 27 are connected by a flange, a stud 21 and a nut 22. A positioning pin 26 is provided on the stud 21. The filter element 18 can further separate the impurity-containing gas. The upper cylinder 17 and the cylinder 7 are fixed to prevent displacement between the upper cylinder 17 and the cylinder 7. A backflush distributor 28 is provided above the filter element 18 in the upper head cover 27. A gas outlet 6 is provided on the top of the upper head cover 27. A backflush gas storage tank 24 is connected to the gas outlet 6. A pressure difference port 8 is provided on the side of the gas outlet 6. The pressure difference port 8 can ensure that the pressure inside and outside the cylinder is consistent.

[0038] Working principle: connect the impure gas and the air inlet pipe 15, so that the impure gas is located in the drainage inner cylinder 16 in the form of cyclone gas, so that the larger diameter particles and impurities in the cyclone gas are separated and fall from the lower cylinder 3 through the cylinder 7 and are collected, and the remaining gas is separated by the separation core 18 and finally passes through the gas outlet 6 to complete the separation of the impure gas flow.

[0039] Those skilled in the art should understand that the embodiments of the present invention described above and shown in the accompanying drawings are only examples and do not limit the present invention, and the purpose of the present invention has been fully and effectively achieved. The functions and structural principles of the present invention have been demonstrated and explained in the embodiments, and the implementation methods of the present invention may be deformed or modified in any way without departing from the principles.

Claims

1. A receiving tank, comprising a separation structure, a gas inlet structure and a cylinder, wherein the gas inlet is located between the separation structure and the cylinder, the separation structure comprises a filter element located in the upper cylinder, and the gas inlet comprises an air inlet pipe and a drainage inner cylinder, characterized in that: The drainage inner cylinder is located in the upper cylinder, and a limit plate parallel to the diameter direction is provided inside the drainage inner cylinder. The air inlet pipe is located on the side of the upper cylinder, and a reinforcement ring is connected between the upper cylinder and the head on the upper part of the cylinder.

2. The receiving tank according to claim 1, characterized in that: The air inlet pipe penetrates the upper cylinder, one end of which is located outside the upper cylinder, and the upper cylinder is wrapped with an insulation ring I, and the other end is located inside the drainage inner cylinder. The air inlet pipe is connected to the external impure gas.

3. The receiving tank according to claim 1, characterized in that: The drainage inner tube is in an I-shape as a whole, the upper part of the drainage inner tube is located below the filter element, the middle part of the drainage inner tube is in a contracted straight tube shape, the lower part of the drainage inner tube is in an outward trumpet shape, and the trumpet shape of the lower part of the drainage inner tube is located inside the cylinder.

4. The receiving tank according to claim 1, characterized in that: The cylinder is cylindrical, and is wrapped with a heat preservation ring II outside the cylinder. An ear-type support is also provided at the upper part of the cylinder, and an electrostatic grounding plate is also provided on the ear-type support. A reserved opening is provided on the cylinder above the ear-type support.

5. The receiving tank according to claim 3, characterized in that: The limiting plate is located in the straight cylinder in the middle of the drainage inner cylinder. The limiting plate is provided with a through hole, and the diameter of the through hole is much larger than the diameter of the solid in the impurity-containing gas.

6. The receiving tank according to claim 1, characterized in that: The top and bottom of the cylinder are respectively a head and a lower cylinder. The lower cylinder as a whole presents a cone with a larger top and a smaller bottom. The angle of the cone is 30-50°. The bottom of the lower cylinder is connected by a discharge pipe and a connecting flange. The connecting flange is connected to an external impurity solid collection bucket. A safety valve port and a lifting lug are provided on the head. The head is wrapped with a head insulation ring. A thermometer port pipe is provided on the side of the lower cylinder.

7. The receiving tank according to claim 1, characterized in that: The filter element is located on the connecting plate at the top of the upper cylinder, an upper head cover is provided on the top of the upper cylinder, the upper cylinder and the upper head cover are connected by a flange, a stud and a nut, and a positioning pin is provided on the stud.

8. The receiving tank according to claim 7, characterized in that: A back-blowing distributor is arranged above the filter element in the upper head cover, a gas outlet is arranged on the top of the upper head cover, a back-blowing gas storage tank is connected to the gas outlet, and a pressure difference port is arranged on the side of the gas outlet.

Citation Information

Patent Citations

  • Gas-solid separator and gas-solid separation system

    CN212314926U