Separation assembly for gas-liquid separation

Abstract

The utility model relates to the technical field of biological aviation kerosene raw material production, and discloses a separation assembly for gas-liquid separation, which comprises a cylindrical separation tank; the flow guide structure comprises a first flow guide part and a second flow guide part, the first flow guide part comprises a heat preservation sleeve arranged in the separation tank, a first fixed circular plate is fixedly mounted on the inner wall of the heat preservation sleeve, a first protective ring plate is fixedly mounted at the top of the first fixed circular plate, and two groups of first flow guide grooves are formed in the bottom of the first fixed circular plate; a conical guide plate is fixedly mounted at the top of the first fixed circular plate; the second flow guide part comprises two groups of first arc-shaped fixing plates arranged at the bottom of the heat preservation sleeve, and the outer walls of the first arc-shaped fixing plates are fixedly connected with the inner wall of the heat preservation sleeve, so that the purposes of guiding and conveying the distillate are achieved, the gas-liquid separation efficiency of the device is improved, and the distillate attached to the flow guide plates is collected and conveyed; and the use flexibility of the device is improved.

Description

TECHNICAL FIELD

[0001] The utility model belongs to biological aviation coal raw material production technical field, concretely relates to a separation assembly for gas-liquid separation. BACKGROUND

[0002] In the biological aviation coal raw material production process, gas-liquid separation technology plays a vital role. The raw materials of biological aviation coal mainly include crop residues, forestry wastes, algae, animal fats, industrial waste gas and energy crops, etc. Among them, food waste oil becomes one of the main raw materials due to its low cost, stable supply and high technical maturity. The production process of biological aviation coal is complex and strict, including filtering and removing impurities, hydrogenation reaction to improve oil performance, and rectification separation to output biological aviation coal.

[0003] In the rectification separation process, efficient gas-liquid separation assembly is the key to ensure product quality and stability. Traditional gas-liquid separation technologies such as gravity settling, inertial collision and centrifugal separation have limitations in the production process of biological aviation coal, such as low separation efficiency, high energy consumption and easy clogging. Therefore, developing a high-efficiency, low-resistance and non-clogging gas-liquid separation assembly is of great significance to improve the production efficiency and product quality of biological aviation coal.

[0004] The utility model discloses a kind of gas-liquid separation equipment, including tank body, the inside of the tank body is provided with the separation mechanism for separating gas-liquid mixture, the top of the tank body is provided with the acceleration component for improving gas flow speed, by being provided with separation mechanism, gas-liquid mixture is guided into the inside of separation mechanism when using, gas-liquid mixture moves in the inside of separation mechanism, will play the effect of making gas-liquid mixture accelerate movement, can also improve the contact area of gas-liquid mixture with separation mechanism simultaneously, so that liquid is attached in the inside of separation mechanism and then discharged, improve the efficiency of gas-liquid separation, by being provided with acceleration component, after gas-liquid mixture enters the inside of separation mechanism, acceleration component can make the gas separated out accelerate discharge, improve the efficiency of gas-liquid separation again.

[0005] But the above patent still has the following problems: in the gas-liquid separation process, part of distillation liquid is easy to adhere to the inner wall of the guide plate, which leads to insufficient collection of distillation liquid. This not only causes waste of resources, but also affects the convenience and practicality of the device, and the use of the device is inconvenient.

[0006] Therefore, the utility model is proposed. UTILITY MODEL CONTENT

[0007] To solve the technical problem of insufficient collection of distillation liquid, the basic idea of the technical solution of the utility model is:

[0008] A separation assembly for gas-liquid separation, comprising:

[0009] A separation tank, the separation tank being cylindrical;

[0010] A flow guide structure, the flow guide structure comprising a first flow guide part and a second flow guide part, the first flow guide part comprising a heat preservation sleeve arranged inside the separation tank, a first fixed circular plate being fixedly installed on an inner wall of the heat preservation sleeve, a first protective ring plate being fixedly installed on a top of the first fixed circular plate, two groups of first flow guide grooves being formed in a bottom of the first fixed circular plate, and a conical material guide plate being fixedly installed on the top of the first fixed circular plate; the second flow guide part comprising two groups of first arc-shaped fixed plates arranged at a bottom of the heat preservation sleeve, outer walls of the two groups of first arc-shaped fixed plates being fixedly connected with an inner wall of the heat preservation sleeve, two groups of first fixed plates being fixedly installed between the two groups of first arc-shaped fixed plates, and a rotating rod being rotatably installed between the two groups of first fixed plates.

[0011] As a preferred embodiment of the present application, the second flow guide part further comprises a turnover circular plate arranged between the two groups of first arc-shaped fixed plates, a first limiting hole being formed in an inner portion of the turnover circular plate, an outer wall of the first fixed plate being fixedly connected with an inner wall of the first limiting hole, and a group of water storage grooves being formed in outer walls of two sides of the turnover circular plate.

[0012] As a preferred embodiment of the present application, the second flow guide part further comprises a second fixed circular plate fixedly installed on an inner wall of the heat preservation sleeve, an electric rotating rod being rotatably installed on a top of the second fixed circular plate, a water scraping plate being fixedly installed on an outer wall of the electric rotating rod, an electric control box being fixedly installed on a bottom of the second fixed circular plate, and the electric control box being electrically connected with the electric rotating rod.

[0013] As a preferred embodiment of the present application, the second flow guide part further comprises eight groups of second flow guide grooves formed in a bottom of the second fixed circular plate, a third fixed circular plate being fixedly installed on an inner wall of the heat preservation sleeve, nine groups of second limiting holes being formed in a bottom of the third fixed circular plate, a mesh being fixedly installed in an inner portion of the second limiting hole, a second protective ring plate being fixedly installed on a top of the third fixed circular plate, and the third fixed circular plate being arranged below the second fixed circular plate.

[0014] As a preferred embodiment of the present application, a sealing bottom cover is fixedly installed on a bottom of the separation tank, a hole is formed in an outer wall of the sealing bottom cover, an output pipe is fixedly installed in the hole, a sealing top cover is fixedly installed on a top of the separation tank, a hole is formed in an outer wall of the sealing top cover, and an input pipe is fixedly installed in the hole.

[0015] As a preferred embodiment of the present application, a hole is formed in an outer wall of the separation tank, a pressure adjusting pipe is fixedly installed in the hole, a group of pressure gauges and a group of adjusting knobs are arranged on an outer wall of the pressure adjusting pipe.

[0016] As an optimal implementation form of the utility model, the support is fixedly installed on the outer wall of the separation tank.

[0017] Compared with the prior art, the utility model has the following beneficial effects:

[0018] 1. The purpose of guiding and conveying the distillation liquid is achieved, the gas-liquid separation efficiency of the device is improved, the distillation liquid attached to the guide plate is collected and conveyed, and the flexibility of the device is improved.

[0019] 2. The purpose of conveying steam and outputting distillation liquid is achieved, the use experience of the device is simplified, the convenience of the device is improved, and the use pressure of the device is reduced.

[0020] 3. The purpose of supporting and fixing the device and adjusting the pressure is achieved, the work pressure of the worker is reduced, the stability of the device is improved, and the use experience of the device is optimized.

[0021] The specific implementation of the utility model will be described in further detail below in combination with the drawings. BRIEF DESCRIPTION OF DRAWINGS

[0022] In the drawings:

[0023] Figure 1 It is a front view of the utility model;

[0024] Figure 2 It is a structural schematic view of the utility model;

[0025] Figure 3 It is a heat preservation sleeve structural schematic view of the utility model;

[0026] Figure 4 It is a first fixed circular plate, input pipe, second fixed circular plate and third fixed circular plate split schematic view of the utility model;

[0027] Figure 5 It is a rotating rod and overturning circular plate split schematic view of the utility model;

[0028] Figure 6 It is a bag net structural schematic view of the utility model;

[0029] Figure 7 It is an electric control box structural schematic view of the utility model.

[0030] In the figure: 10, separation tank; 11, sealing bottom cover; 12, output pipe; 13, sealing top cover; 14, input pipe; 15, pressure regulating pipe; 16, pressure gauge; 17, adjusting knob; 18, support; 19, heat preservation sleeve; 20, first fixed circular plate; 21, first protective ring plate; 22, first flow guide groove; 23, conical guide plate; 24, first arc-shaped fixed plate; 25, first fixed plate; 26, rotating rod; 27, overturning circular plate; 28, first limiting hole; 29, water storage groove; 30, second fixed circular plate; 31, electric rotating rod; 32, wiper plate; 33, second flow guide groove; 34, electric control box; 35, third fixed circular plate; 36, second protective ring plate; 37, second limiting hole; 38, mesh net. DETAILED DESCRIPTION

[0031] In order to make the purpose, technical scheme and advantages of the embodiments of the utility model clearer, the technical scheme in the embodiments will be clearly and completely described below in combination with the drawings in the embodiments of the utility model, and the following embodiments are used to illustrate the utility model.

[0032] Embodiment one: a separation assembly for gas-liquid separation, specifically as shown in Figure 1 , Figure 3 and Figure 4 , comprising a separation tank 10, the separation tank 10 is cylindrical; a flow guide structure, the flow guide structure comprises a first flow guide part and a second flow guide part, the first flow guide part comprises a heat preservation sleeve 19 arranged inside the separation tank 10, a first fixed circular plate 20 is fixedly installed on the inner wall of the heat preservation sleeve 19, a first protective ring plate 21 is fixedly installed on the top of the first fixed circular plate 20, two groups of first flow guide grooves 22 are arranged on the bottom of the first fixed circular plate 20, and a conical guide plate 23 is fixedly installed on the top of the first fixed circular plate 20; the second flow guide part comprises two groups of first arc-shaped fixed plates 24 arranged at the bottom of the heat preservation sleeve 19, the outer wall of the first arc-shaped fixed plate 24 is fixedly connected with the inner wall of the heat preservation sleeve 19, two groups of first fixed plates 25 are fixedly installed between the two groups of first arc-shaped fixed plates 24, and a rotating rod 26 is rotatably installed between the two groups of first fixed plates 25. The flow guide structure is used for guiding and outputting the distillation liquid. The first protective ring plate 21 is used for shielding the edge of the first fixed circular plate 20, and the first flow guide groove 22 and the conical guide plate 23 are used for accumulating the steam into the distillation liquid and guiding the distillation liquid to the first arc-shaped fixed plate 24.

[0033] Specifically as shown in Figure 4 and Figure 5As shown in the drawings, the second flow guide part further comprises a turnover circular plate 27 arranged between the two groups of first arc-shaped fixed plates 24, the inside of the turnover circular plate 27 is provided with a first limiting hole 28, the outer wall of the first fixed plate 25 is fixedly connected with the inner wall of the first limiting hole 28, and a group of water storage grooves 29 are arranged on the outer walls of the two sides of the turnover circular plate 27. When the distillate liquid accumulates on the water storage grooves 29, the weight of the distillate liquid drives the rotating rod 26 to rotate, so that the water storage grooves 29 are turned over, and the distillate liquid is transported to the top of the second fixed circular plate 30.

[0034] As shown in the drawings, Figure 4 and Figure 7 As shown in the drawings, the second flow guide part further comprises a second fixed circular plate 30 fixedly arranged on the inner wall of the heat preservation sleeve 19, the top of the second fixed circular plate 30 is rotatably arranged with an electric rotating rod 31, the outer wall of the electric rotating rod 31 is fixedly arranged with a water scraping plate 32, the bottom of the second fixed circular plate 30 is fixedly arranged with an electric control box 34, and the electric control box 34 is electrically connected with the electric rotating rod 31. Starting the electric control box 34 drives the electric rotating rod 31 to rotate, and drives the water scraping plate 32 to push the distillate liquid falling on the second fixed circular plate 30 to the inside of the second flow guide groove 33 and to the top of the third fixed circular plate 35.

[0035] As shown in the drawings, Figure 4 and Figure 6 As shown in the drawings, the second flow guide part further comprises eight groups of second flow guide grooves 33 arranged on the bottom of the second fixed circular plate 30, the inner wall of the heat preservation sleeve 19 is fixedly arranged with a third fixed circular plate 35, the bottom of the third fixed circular plate 35 is arranged with nine groups of second limiting holes 37, the inside of the second limiting hole 37 is fixedly arranged with a bag net 38, the top of the third fixed circular plate 35 is fixedly arranged with a second protective ring plate 36, and the third fixed circular plate 35 is arranged below the second fixed circular plate 30. The edge of the third fixed circular plate 35 is shielded by the second protective ring plate 36, the bag net 38 is limited by the second limiting hole 37, the distillate liquid is filtered by the bag net 38, and is output.

[0036] According to the above, through the structure of the separation tank 10, the heat preservation sleeve 19, the first fixed circular plate 20, the first protective ring plate 21, the first flow guide groove 22, the conical guide plate 23, the first arc-shaped fixed plate 24, the first fixed plate 25, the rotating rod 26, the turnover circular plate 27, the first limiting hole 28, the water storage groove 29, the second fixed circular plate 30, the electric rotating rod 31, the water scraping plate 32, the second flow guide groove 33, the electric control box 34, the third fixed circular plate 35, the second protective ring plate 36, the second limiting hole 37 and the bag net 38, the purpose of guiding and transporting the distillate liquid is achieved, the gas-liquid separation efficiency of the device is improved, the distillate liquid adhering to the guide plate is collected and transported, and the flexibility of the device is improved.

[0037] Example Two: Based on example one, as shown in the drawings,Figure 1 And Figure 2 As shown in The bottom of the separation tank 10 is fixedly installed with a sealing bottom cover 11, a hole is formed in the outer wall of the sealing bottom cover 11, and an output pipe 12 is fixedly installed in the hole. The top of the separation tank 10 is fixedly installed with a sealing top cover 13, a hole is formed in the outer wall of the sealing top cover 13, and an input pipe 14 is fixedly installed in the hole. The distillate is output through the output pipe 12, and the steam is transported into the separation tank 10 through the input pipe 14.

[0038] According to the above, through the structure of the separation tank 10, the sealing bottom cover 11, the output pipe 12, the sealing top cover 13 and the input pipe 14, the purpose of transporting steam and outputting distillate is achieved, the use experience of the device is simplified, the convenience of using the device is improved, and the use pressure of the device is reduced.

[0039] Figure 1 And Figure 2 As shown in The outer wall of the separation tank 10 is fixedly installed with a pressure regulating pipe 15, and a group of pressure gauges 16 and a group of adjusting knobs 17 are arranged on the outer wall of the pressure regulating pipe 15. Rotate the adjusting knob 17 to adjust the pressure in the separation tank 10, and observe the pressure through the pressure gauge 16.

[0040] Figure 1 And Figure 2 As shown in The outer wall of the separation tank 10 is fixedly installed with a support 18. The device is supported by the support 18. The device in the heat preservation sleeve 19 is coated with a water-resistant coating.

[0041] As described above, through the structure of the separation tank 10, the pressure regulating pipe 15, the pressure gauge 16, the adjusting knob 17 and the support 18, the purpose of supporting and fixing the device and adjusting the pressure is achieved, the work pressure of the worker is reduced, the stability of using the device is improved, and the use experience of the device is optimized.

[0042] Working principle: steam enters the inside of the separation tank 10 through the input pipe 14. In the separation tank 10, the steam encounters the flow guide structure for flow guiding and separation. The flow guide structure mainly consists of a first flow guide part and a second flow guide part, the first flow guide part including a heat preservation sleeve 19, a first fixed circular plate 20, a first protective ring plate 21, a first flow guide groove 22 and a conical material guide plate 23. The steam rises in the heat preservation sleeve 19, is guided by the conical material guide plate 23 and accumulates on the first fixed circular plate 20. When the steam accumulates into distillate, it flows to the first arc-shaped fixed plate 24 through the first flow guide groove 22, and the second flow guide part further processes the distillate. The distillate first accumulates in the water storage groove 29 of the overturned circular plate 27. When the distillate accumulates to a certain weight, it drives the rotating rod 26 to rotate, so that the water storage groove 29 is overturned, and the distillate is transported to the top of the second fixed circular plate 30. On the second fixed circular plate 30, the electric rotating rod 31 rotates through the start of the electric control box 34, drives the water scraping plate 32 to move the top of the second flow guide groove 33, pushes the distillate into the second flow guide groove 33, and finally transports the distillate to the top of the third fixed circular plate 35. At the third fixed circular plate 35, the distillate is filtered by the mesh net 38, and after removing impurities, the distillate is output. The mesh net 38 is fixed at the bottom of the third fixed circular plate 35 through the second limiting hole 37, and the second protective ring plate 36 shields the edge of the third fixed circular plate 35. The bottom of the separation tank 10 outputs the processed distillate through the sealing bottom cover 11 and the output pipe 12. At the same time, the top of the separation tank 10 receives new steam input through the sealing top cover 13 and the input pipe 14. The outer wall of the separation tank 10 is provided with the pressure adjusting pipe 15, the pressure in the separation tank 10 can be adjusted by rotating the adjusting knob 17, and the current pressure value can be observed through the pressure gauge 16. The support 18 is used for supporting the whole device.

[0043] It can be understood that the utility model is described through some embodiments, and the person skilled in the art knows that various changes or equivalent replacements can be made to these features and embodiments without departing from the spirit and scope of the utility model. In addition, under the guidance of the utility model, these features and embodiments can be modified to adapt to specific conditions and materials without departing from the spirit and scope of the utility model. Therefore, the utility model is not limited by the specific embodiments disclosed herein, and all embodiments falling within the scope of the claims of the present application belong to the scope protected by the utility model.

Claims

1. A separation assembly for gas-liquid separation, characterized by The utility model relates to a kind of separation tank and its guide structure. The utility model provides a kind of separation tank and its guide structure, including: separation tank (10), separation tank (10) is cylindrical; The guide structure includes first guide part and second guide part, first guide material part includes the heat preservation sleeve (19) being arranged in the inside of separation tank (10), the inner wall of heat preservation sleeve (19) is fixedly installed with first fixed circular plate (20), the top of first fixed circular plate (20) is fixedly installed with first protection ring plate (21), the bottom of first fixed circular plate (20) is provided with two groups of first guide groove (22), the top of first fixed circular plate (20) is fixedly installed with conical guide plate (23);Second guide part includes two groups of first arc-shaped fixed plate (24) being arranged in the bottom of heat preservation sleeve (19), the outer wall of first arc-shaped fixed plate (24) is fixedly connected with the inner wall of heat preservation sleeve (19), two groups of first arc-shaped fixed plate (24) between fixedly installed with two groups of first fixed plate (25), two groups of first fixed plate (25) between rotatably installed with rotating rod (26).

2. The separation assembly for gas-liquid separation according to claim 1, characterized in that The second guide part further includes a turnover circular plate (27) arranged between the two groups of first arc-shaped fixed plates (24), a first limiting hole (28) is formed in the inside of the turnover circular plate (27), the outer wall of the first fixed plate (25) is fixedly connected with the inner wall of the first limiting hole (28), a group of water storage grooves (29) are formed in the outer walls of the two sides of the turnover circular plate (27).

3. The separation assembly for gas-liquid separation according to claim 1, characterized in that, The second guide part further includes a second fixed circular plate (30) fixedly installed on the inner wall of the heat preservation sleeve (19), an electric rotating rod (31) is rotatably installed on the top of the second fixed circular plate (30), a water scraping plate (32) is fixedly installed on the outer wall of the electric rotating rod (31), an electric control box (34) is fixedly installed on the bottom of the second fixed circular plate (30), and the electric control box (34) is electrically connected with the electric rotating rod (31).

4. The separation assembly for gas-liquid separation according to claim 1, characterized in that, The second guide part further includes eight groups of second guide grooves (33) formed in the bottom of the second fixed circular plate (30), a third fixed circular plate (35) is fixedly installed on the inner wall of the heat preservation sleeve (19), nine groups of second limiting holes (37) are formed in the bottom of the third fixed circular plate (35), a mesh net (38) is fixedly installed in the inside of each second limiting hole (37), a second protection ring plate (36) is fixedly installed on the top of the third fixed circular plate (35), and the third fixed circular plate (35) is arranged below the second fixed circular plate (30).

5. The separation assembly for gas-liquid separation according to claim 1, characterized in that, A sealing bottom cover (11) is fixedly installed on the bottom of the separation tank (10), a hole is formed in the outer wall of the sealing bottom cover (11), and an output pipe (12) is fixedly installed in the hole, a sealing top cover (13) is fixedly installed on the top of the separation tank (10), a hole is formed in the outer wall of the sealing top cover (13), and an input pipe (14) is fixedly installed in the hole.

6. The separation assembly for gas-liquid separation according to claim 1, wherein A hole is formed in the outer wall of the separation tank (10), a pressure adjusting pipe (15) is fixedly installed in the hole, a group of pressure gauges (16) and a group of adjusting knobs (17) are arranged on the outer wall of the pressure adjusting pipe (15).

7. The separation assembly for gas-liquid separation according to claim 1, wherein A support (18) is fixedly installed on the outer wall of the separation tank (10).

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