Carbon capture integrated equipment for coupling multistage membrane separation with chemical adsorption

Abstract

The utility model relates to the technical field of carbon capture, and discloses a multistage membrane separation coupled chemical adsorption carbon capture integrated device, which comprises a pretreatment device, a membrane separation device, an adsorption tower and an auxiliary device, an inner frame is arranged in the adsorption tower, and the upper side and the lower side of the outer part of the inner frame in the adsorption tower are respectively provided with a building frame; the first servo motor is arranged in the adsorption tower and located on the left side of the lower end of the inner frame, a driving rod is installed at the output end of the first servo motor, and two steam nozzles are arranged at the upper end of the driving rod; the second servo motor is arranged at the end, away from the first servo motor, of the upper end of the driving rod, a driving gear is installed at the output end of the second servo motor, a transmission gear ring is arranged in the lower end of the inner frame, and the driving gear is connected with the transmission gear ring in a meshed mode; and the chemical adsorbent is arranged in the inner frame. According to the utility model, the chemical adsorbent is regenerated by using high-temperature steam in the adsorption tower, so that the cost is reduced.

Description

Technical Field

[0001] This utility model relates to the field of carbon capture technology, specifically to an integrated carbon capture device that combines multi-stage membrane separation with chemical adsorption. Background Technology

[0002] The multi-stage membrane separation coupled with chemisorption carbon capture integrated equipment is an advanced carbon capture technology device. It combines multi-stage membrane separation technology with chemisorption method to efficiently capture carbon dioxide (CO2) from industrial waste gas (such as flue gas from coal-fired power plants, steel plants, cement plants, etc.).

[0003] A multi-stage membrane separation coupled with chemisorption carbon capture integrated equipment typically consists of a pretreatment unit, a membrane separation unit, a chemisorption unit, auxiliary equipment, and a control system.

[0004] The chemical adsorption device is filled with chemical adsorbents, which can react chemically or physically with carbon dioxide to separate it from the gas. Over time, the adsorbents become saturated and need to be processed. Replacing the chemical adsorbents requires the regular purchase of new adsorbents, which increases the operating cost of the equipment. At the same time, the waste disposal costs generated during the replacement of the adsorbents also increase the operating cost. Therefore, a multi-stage membrane separation coupled with chemical adsorption carbon capture integrated equipment is proposed. Utility Model Content

[0005] (a) Technical problems to be solved

[0006] To address the shortcomings of existing technologies, this invention provides an integrated carbon capture device that combines multi-stage membrane separation with chemical adsorption, thereby solving the problems mentioned in the background section.

[0007] (II) Technical Solution

[0008] To achieve the above objectives, this utility model provides the following technical solution: a multi-stage membrane separation coupled with chemical adsorption carbon capture integrated device, comprising:

[0009] The device includes a pretreatment unit, a membrane separation unit, an adsorption tower, and auxiliary equipment. The adsorption tower has an inner frame inside, and the adsorption tower has supports on both the upper and lower sides outside the inner frame. The inner frame and the supports are movably connected.

[0010] The first servo motor is located inside the adsorption tower, on the lower left side of the inner frame. A drive rod is installed at the output end of the first servo motor, and two steam nozzles are provided at the upper end of the drive rod.

[0011] The second servo motor is located at the upper end of the drive rod, away from the end of the first servo motor. A drive gear is installed at the output end of the second servo motor. A transmission gear ring is provided inside the lower end of the inner frame. The drive gear meshes with the transmission gear ring.

[0012] The chemical adsorbent is placed inside the inner frame.

[0013] Preferably, a return spring is provided on one side of the upper end of the drive rod, and a bracket is provided on the upper end of the return spring, and the bracket is fixed to the return spring. The return spring is used to lift the bracket.

[0014] Preferably, a rotating roller is rotatably installed inside the upper end of the bracket, and a vibrator is provided at the lower end of the bracket. The vibrator is fixed to the bracket, and the vibration generated by the vibrator is transmitted to the bracket. The bracket then transmits the vibration to the chemical adsorbent through the rotating roller.

[0015] Preferably, the adsorption tower has a side door located on the right side of the inner frame, and the side door is rotatably connected to the adsorption tower.

[0016] Preferably, the adsorption tower is provided with a second side block and a first side block at the lower end of the side door on the outside. The second side block is fitted with an adjusting bolt through a threaded connection. The adjusting bolt is used to control the lifting and lowering of the limit plate.

[0017] Preferably, the upper end of the adjusting bolt is rotatably connected to a limiting plate, and the limiting plate is slidably connected to the second side block. The limiting plate is used to limit the side door.

[0018] (III) Beneficial Effects

[0019] Compared with the prior art, this utility model provides a multi-stage membrane separation coupled with chemical adsorption carbon capture integrated device, which has the following beneficial effects:

[0020] This invention uses a steam nozzle to spray high-temperature steam toward the chemical adsorbent. During the heating process, the adsorbate molecules gradually desorb from the surface of the adsorbent, forming gas or steam. This allows the chemical adsorbent to be regenerated inside the adsorption tower, eliminating the cost and complex process of replacing the chemical adsorbent and solving the problems mentioned in the background art. Attached Figure Description

[0021] Figure 1 This is a three-dimensional view of the overall structure of this utility model;

[0022] Figure 2 This is a cross-sectional view of the adsorption tower structure of this utility model;

[0023] Figure 3 For the present utility model Figure 2 Enlarged view of a portion of region A in the middle;

[0024] Figure 4 For the present utility model Figure 2 Enlarged view of a portion of region B in the middle.

[0025] In the diagram: 1. Pretreatment device; 2. Membrane separation device; 3. Adsorption tower; 4. Auxiliary equipment; 5. Inner frame; 6. Chemical adsorbent; 7. First servo motor; 8. Drive rod; 9. Steam nozzle; 10. Second servo motor; 11. Drive gear; 12. Transmission gear ring; 13. Return spring; 14. Vibrator; 15. Bracket; 16. Rotary roller; 17. Side door; 18. First side block; 19. Adjusting bolt; 20. Second side block; 21. Limiting plate; 22. Frame. Detailed Implementation

[0026] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.

[0027] This utility model provides a technical solution: a multi-stage membrane separation coupled with chemical adsorption integrated carbon capture device. Please refer to [link to relevant documentation]. Figure 1 , Figure 2 , Figure 3 and Figure 4 ,include:

[0028] The pretreatment device 1, membrane separation device 2, adsorption tower 3 and auxiliary equipment 4 are provided. The adsorption tower 3 is provided with an inner frame 5. The adsorption tower 3 is provided with supports 22 on the upper and lower sides outside the inner frame 5. The inner frame 5 and the supports 22 are movably connected.

[0029] The first servo motor 7 is located inside the adsorption tower 3 at the lower left of the inner frame 5. The output end of the first servo motor 7 is equipped with a drive rod 8, and the upper end of the drive rod 8 is equipped with two steam nozzles 9.

[0030] The second servo motor 10 is located at the upper end of the drive rod 8, away from the end of the first servo motor 7. The output end of the second servo motor 10 is equipped with a drive gear 11, and the lower end of the inner frame 5 is provided with a transmission gear ring 12. The drive gear 11 and the transmission gear ring 12 are meshed and connected.

[0031] Chemical adsorbent 6 is placed inside the inner frame 5.

[0032] Please see Figure 2 , Figure 3 and Figure 4A return spring 13 is provided on one side of the upper end of the drive rod 8. A bracket 15 is provided on the upper end of the return spring 13, and the bracket 15 is fixed to the return spring 13. The return spring 13 is used to lift the bracket 15.

[0033] Please see Figure 2 , Figure 3 and Figure 4 A rotating roller 16 is rotatably mounted inside the upper end of the bracket 15, and a vibrator 14 is provided at the lower end of the bracket 15. The vibrator 14 is fixed to the bracket 15. The vibration generated by the vibrator 14 is transmitted to the bracket 15, and the bracket 15 transmits the vibration to the chemical adsorbent 6 through the rotating roller 16.

[0034] Please see Figure 2 and Figure 4 The adsorption tower 3 is provided with a side door 17 on the right side of the inner frame 5, and the side door 17 is rotatably connected to the adsorption tower 3.

[0035] Please see Figure 2 and Figure 4 The adsorption tower 3 is provided with a second side block 20 and a first side block 18 at the lower end of the side door 17. The second side block 20 is fitted with an adjusting bolt 19 through a threaded connection. The adjusting bolt 19 is used to control the lifting and lowering of the limit plate 21.

[0036] Please see Figure 2 and Figure 4 The upper end of the adjusting bolt 19 is rotatably connected to the limiting plate 21, and the limiting plate 21 is slidably connected to the second side block 20. The limiting plate 21 is used to limit the side door 17.

[0037] This scheme involves connecting and turning on the input end of the steam source and steam nozzle 9. The first servo motor 7 is activated to control the drive rod 8 to rotate towards the chemical adsorbent 6 until it reaches a horizontal parallel position. At this point, the drive gear 11 meshes with the transmission gear ring 12, and the steam nozzle 9 heats the chemical adsorbent 6, causing the adsorbed organic matter to carbonize or volatilize. The second servo motor 10 is activated, causing the drive gear 11 to rotate. The transmission gear ring 12 and the drive gear 11 drive the inner frame 5 to rotate, ensuring sufficient contact between the steam and the chemical adsorbent 6 at different positions. Simultaneously, the vibrator 14 is activated to generate vibration, which is transmitted to the chemical adsorbent 6 through the bracket 15 and the rotating roller 16. The vibration disrupts the agglomeration on the adsorbent surface, making it easier for adsorbate molecules to desorb from the adsorbent surface. The adsorbate molecules gain sufficient energy to desorb from the adsorbent surface, forming gas or vapor. This gas or vapor can be discharged through the outlet of the adsorption tower 3 and subjected to appropriate treatment (such as condensation, absorption, etc.) to recover or process the adsorbate. After heating and regeneration, the adsorption tower 3 needs to be cooled to restore the adsorbent to a suitable operating temperature.

[0038] It should be noted that, in this document, relational terms such as "first" and "second" are used only to distinguish one entity or operation from another, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Furthermore, the terms "comprising," "including," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements includes not only those elements but also other elements not expressly listed, or elements inherent to such process, method, article, or apparatus.

[0039] Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made to these embodiments without departing from the principles and spirit of the present invention, the scope of which is defined by the appended claims and their equivalents.

Claims

1. A multi-stage membrane separation coupled with chemical adsorption integrated carbon capture plant, characterized in that, Include: Preprocessing device (1), membrane separation device (2), adsorption tower (3) and auxiliary equipment (4), the inside of the adsorption tower (3) is provided with inner frame (5), the inside of the adsorption tower (3) is located on the outside of the inner frame (5) upper and lower sides are provided with the frame (22), and the inner frame (5) is movably connected with the frame (22); The first servo motor (7) is arranged in the lower left side of the inner frame (5) in the inside of the adsorption tower (3), the output end of the first servo motor (7) is provided with a driving rod (8), the upper end of the driving rod (8) is provided with two steam nozzles (9); The second servo motor (10) is arranged on the end of the upper end of the driving rod (8) away from the first servo motor (7), the output end of the second servo motor (10) is provided with a driving gear (11), the lower end of the inner frame (5) is provided with a transmission gear ring (12), the driving gear (11) is movably connected with the transmission gear ring (12); Chemisorption agent (6) is arranged in the inside of the inner frame (5).

2. The integrated carbon capture device of claim 1, wherein: The upper end of the driving rod (8) is provided with a reset spring (13) on one side, the upper end of the reset spring (13) is provided with a bracket (15), and the bracket (15) is fixed with the reset spring (13).

3. The integrated carbon capture device of claim 2, wherein: The upper end of the bracket (15) is rotatably installed with a rotating roller (16), the lower end of the bracket (15) is provided with a vibrator (14), and the vibrator (14) is fixed with the bracket (15).

4. The multi-stage membrane separation coupled with chemisorption integrated carbon capture device of claim 1, wherein: The outside of the adsorption tower (3) is provided with a side door (17) on the right side of the inner frame (5), and the side door (17) is rotatably connected with the adsorption tower (3).

5. The multi-stage membrane separation coupled with chemisorption integrated carbon capture device of claim 4, wherein: The outside of the adsorption tower (3) is provided with a second side block (20) and a first side block (18) on the lower end of the side door (17), the inside of the second side block (20) is provided with an adjusting bolt (19) through threaded cooperation.

6. The multi-stage membrane separation coupled with chemisorption integrated carbon capture device of claim 5, wherein: The upper end of the adjusting bolt (19) is rotatably connected with a limiting plate (21), and the limiting plate (21) is slidably connected with the second side block (20).

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