Carbon capture multistage cyclonic separation device

Abstract

The utility model discloses a kind of carbon capture multilayer cyclone separation devices, it is related to carbon capture device technical field.The utility model includes separation cylinder, carbon capture structure, including fixed in the inside of the lower end of separation cylinder and the open upper end of net cylinder, fill in the granular amido modified activated carbon of net cylinder inside, the partition that is equidistant distribution in the inner wall of net cylinder, the hole that is distributed in the partition inside, rotationally installed in the partition inside of shaft, the rotating plate that is annular array distribution between partition and is connected with shaft;Maintenance structure, including the closure cap in the upper end of net cylinder, nut, slider in the one end of nut and closure cap, guide rail in the inner wall of net cylinder, motor one in the upper end of separation cylinder, screw rod in the lower end of motor one.The utility model sets up carbon capture structure, to solve the problem that amido modified activated carbon of granular accumulation makes gas pass through when being blocked, and then lead to the efficiency reduction of activated carbon capture.

Description

Technical Field

[0001] This utility model relates to the field of carbon capture device technology, and in particular to a carbon capture multilayer cyclone separation device. Background Technology

[0002] Flue gas is treated by electrostatic precipitators or bag filters to remove particulate matter and prevent adsorbent pore blockage. Wet or dry desulfurization is used to avoid SO2 and CO2 competing for adsorption sites. Selective catalytic reduction technology is used to reduce the poisoning effect of nitrogen oxides on the adsorbent. Flue gas temperature and humidity are controlled to optimize the working conditions of the adsorbent.

[0003] The treated flue gas is captured using amine-modified activated carbon. Under normal or slightly positive pressure, the treated flue gas is adsorbed by the amine-modified activated carbon. Carbon capture directly reduces greenhouse gas emissions, contributing to carbon neutrality. However, the particle-accumulated amine-modified activated carbon obstructs gas flow, reducing the efficiency of activated carbon capture. Therefore, those skilled in the art have provided a multi-layer cyclone separator for carbon capture to address the problems mentioned in the background section. Utility Model Content

[0004] 1. Technical Solution

[0005] To solve the above-mentioned technical problems, this utility model is achieved through the following technical solution:

[0006] This utility model relates to a multi-layer cyclone separation device for carbon capture, including a separation cylinder.

[0007] The carbon capture structure includes a mesh cylinder fixed inside the lower end of the separation cylinder and open at the upper end, granular amine-modified activated carbon filled inside the mesh cylinder, partitions evenly distributed on the inner wall of the mesh cylinder, holes staggered inside the partitions, a rotating shaft rotatably installed inside the partitions, and rotating plates arranged in a ring array between the partitions and connected to the rotating shaft.

[0008] as well as;

[0009] The maintenance structure includes a closed cover at the upper end of the mesh cylinder, a nut at one end of the closed cover, a slider at one end of the nut and the closed cover, a guide rail located on the inner wall of the mesh cylinder and slidably mounted with the slider, a motor at the upper end of the separating cylinder, a bearing embedded in the upper end of the separating cylinder, and a screw located at the lower end of the motor, rotatably mounted inside the bearing and threadedly connected to the nut.

[0010] Furthermore, a flow guide shroud is provided at the upper end of the separation cylinder, a conveying pipe is provided at the upper end of the flow guide shroud, and a gas detector is provided inside the conveying pipe;

[0011] Specifically, the flow guide hood transports the gas after it has been adsorbed by amine-modified activated carbon, and the carbon dioxide content in the gas is detected by a gas detector during the emission process.

[0012] Furthermore, an inspection port is provided at one end of the separation cylinder, and an inspection door is provided on the outer wall of the separation cylinder to cover the inspection port and to be fixed by bolts. A support frame is provided on the outer wall of the separation cylinder.

[0013] Specifically, the inside of the separator is inspected through the inspection port, the inspection port is closed through the inspection door, and the separator is supported by the support frame.

[0014] Furthermore, the lower end of the closed cover is provided with an annular plug located in the upper opening of the mesh cylinder, the upper end of the closed cover is provided with a second motor whose output end is rotatably mounted on the closed cover, the lower end of the second motor is provided with a rotating ring, the lower end of the rotating ring is provided with rotating rods arranged in an annular array, the upper end of the rotating shaft is provided with a support ring, and the upper end of the support ring is provided with side rods arranged in an annular array and located between the rotating rods;

[0015] Specifically, the ring plug closes the upper end of the mesh cylinder. When the rotating rod connects with the side rod, the rotational force of the rotating ring is applied to the side rod through the rotating rod, causing the support ring and the rotating shaft to rotate.

[0016] Furthermore, a travel channel is provided between the separating cylinder and the mesh cylinder, the upper end of the separating cylinder is connected to the travel channel, and the lower end of the separating cylinder is provided with a discharge pipe that is connected to the lower end of the mesh cylinder and controlled by a valve;

[0017] Specifically, the gas adsorbed by the amine-modified activated carbon is transported upward through the flow channel, and the saturated amine-modified activated carbon is transported to the outside through the discharge pipe. The opening and closing of the discharge pipe is controlled by a valve.

[0018] Furthermore, the lower end of the separation cylinder is provided with a diffusion shroud whose radius decreases sequentially from top to bottom, and the lower end of the diffusion shroud is connected to an input pipe;

[0019] Specifically, the treated flue gas is input through the input pipe and then transported into the inside of the mesh cylinder through the diffuser.

[0020] 2. Beneficial effects

[0021] Compared with existing technologies, the advantages of this utility model are:

[0022] This invention guides the treated flue gas into the interior of a mesh cylinder. The mesh cylinder contains amine-modified activated carbon in its interlayer. As the treated flue gas passes through the mesh cylinder, it comes into contact with the amine-modified activated carbon. Carbon dioxide in the flue gas also contacts the amine-modified activated carbon, while the flue gas flows out through the gaps between the amine-modified activated carbon particles. Upon entering the mesh cylinder, a rotating plate causes the flue gas to rotate, dividing the interior of the mesh cylinder into multiple spaces connected by holes. When the flue gas throughput is low, the compressed flue gas automatically rises and enters different positions within the mesh cylinder, contacting the amine-modified activated carbon inside. The rotating plate slaps the treated flue gas into the mesh cylinder, aiding in its flow. The flue gas vortexes as it contacts the mesh cylinder and flows upwards, further improving the flow and efficiency of the treated flue gas through the mesh cylinder, thus enhancing carbon capture efficiency.

[0023] Of course, any product implementing this utility model does not necessarily need to achieve all of the advantages described above at the same time. Attached Figure Description

[0024] To more clearly illustrate the technical solutions of the embodiments of this utility model, the accompanying drawings used in the description of the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of this utility model. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0025] Figure 1 This is a side view of the three-dimensional structure of the present invention;

[0026] Figure 2 This is a front-view three-dimensional structural diagram of the present invention;

[0027] Figure 3 This is a schematic diagram of the main sectional three-dimensional structure of this utility model;

[0028] Figure 4 This is a schematic diagram of the three-dimensional structure of the mesh cylinder of this utility model in front section.

[0029] Figure 5 This is a front-view three-dimensional structural diagram of the motor of this utility model.

[0030] The attached diagram lists the components represented by each number as follows:

[0031] 100. Separation cylinder; 101. Support frame;

[0032] 200. Maintenance structure; 201. Closing cover; 202. Flow deflector; 203. Gas detector; 204. Delivery pipe; 205. Motor 1; 206. Bearing; 207. Guide rail; 208. Screw; 209. Slider; 210. Inspection port; 211. Inspection door; 212. Nut; 213. Plug;

[0033] 300. Carbon capture structure; 301. Discharge pipe; 302. Mesh cylinder; 303. Stroke channel; 304. Motor II; 305. Rotating shaft; 306. Partition plate; 307. Rotating plate; 308. Hole; 309. Diffuser hood; 310. Input pipe; 311. Support ring; 312. Side rod; 313. Rotating ring; 314. Rotating rod. Detailed Implementation

[0034] To make the above-mentioned objectives, features and advantages of this utility model more apparent and understandable, the specific embodiments of this utility model will be described in detail below with reference to the accompanying drawings.

[0035] Many specific details are set forth in the following description in order to provide a full understanding of the present invention. However, the present invention may also be implemented in other ways different from those described herein. Those skilled in the art can make similar extensions without departing from the spirit of the present invention. Therefore, the present invention is not limited to the specific embodiments disclosed below.

[0036] Secondly, this utility model is described in detail with reference to the schematic diagrams. When describing the embodiments of this utility model, for ease of explanation, the cross-sectional views illustrating the device structure may be partially enlarged, not adhering to the usual scale. Furthermore, the schematic diagrams are merely examples and should not limit the scope of protection of this utility model. In addition, actual manufacturing should include the three-dimensional spatial dimensions of length, width, and depth.

[0037] To make the objectives, technical solutions, and advantages of this utility model clearer, the embodiments of this utility model will be described in further detail below with reference to the accompanying drawings.

[0038] Example 1

[0039] Please see Figures 1-5 As shown, this embodiment is a carbon capture multilayer cyclone separator, including a separation cylinder 100.

[0040] The carbon capture structure 300 includes a mesh cylinder 302 fixed inside the lower end of the separation cylinder 100 and open at the upper end, granular amine-modified activated carbon filled inside the mesh cylinder 302, partitions 306 evenly distributed on the inner wall of the mesh cylinder 302, holes 308 staggeredly distributed inside the partitions 306, a rotating shaft 305 rotatably installed inside the partitions 306, and rotating plates 307 arranged in a ring array between the partitions 306 and connected to the rotating shaft 305.

[0041] as well as;

[0042] The maintenance structure 200 includes a closed cover 201 located at the upper end of the mesh cylinder 302, a nut 212 located at one end of the closed cover 201, a slider 209 located at one end of the nut 212 and the closed cover 201, a guide rail 207 located on the inner wall of the mesh cylinder 302 and slidably mounted with the slider 209, a motor 205 located at the upper end of the separation cylinder 100, a bearing 206 embedded and mounted inside the upper end of the separation cylinder 100, and a screw 208 located at the lower end of the motor 205, rotatably mounted inside the bearing 206, and threadedly connected to the nut 212; a flow guide 202 is provided at the upper end of the separation cylinder 100, a conveying pipe 204 is provided at the upper end of the flow guide 202, and a gas detector 203 is provided inside the conveying pipe 204;

[0043] The separator 100 has an inspection port 210 at one end, and an inspection door 211 that covers the inspection port 210 and is fixed by bolts is provided on the outer wall of the separator 100. A support frame 101 is provided on the outer wall of the separator 100.

[0044] The lower end of the closed cover 201 is provided with a ring plug 213 in the upper opening of the mesh cylinder 302. The upper end of the closed cover 201 is provided with a motor 304 whose output end is rotatably mounted on the closed cover 201. The lower end of the motor 304 is provided with a rotating ring 313. The lower end of the rotating ring 313 is provided with rotating rods 314 arranged in a ring array. The upper end of the rotating shaft 305 is provided with a support ring 311. The upper end of the support ring 311 is provided with side rods 312 arranged in a ring array and located between the rotating rods 314.

[0045] A travel channel 303 is provided between the separation cylinder 100 and the mesh cylinder 302. The upper end of the separation cylinder 100 is connected to the travel channel 303. The lower end of the separation cylinder 100 is provided with a discharge pipe 301 that is connected to the lower end of the mesh cylinder 302 and is controlled by a valve.

[0046] The lower end of the separator 100 is provided with a diffuser 309 whose radius decreases from top to bottom, and the lower end of the diffuser 309 is connected to an input pipe 310;

[0047] The maintenance structure 200 and the carbon capture structure 300 are used;

[0048] When the device is powered on, the treated flue gas enters the diffuser hood 309 through the input pipe 310. After being evenly distributed by the diffuser hood 309, it enters the bottom of the mesh cylinder 302. The motor 304 drives the rotating ring 313 to rotate, which in turn drives the rotating rod 314 to periodically move the side rod 312, so that the rotating shaft 305 and the rotating plate 307 rotate synchronously. The flue gas forms a vortex airflow under the push of the rotating plate 307, spirals up along the inner wall of the mesh cylinder 302, and passes through the holes 308 of the partition 306 in sequence to enter the multi-layer space. The amine-modified activated carbon particles come into full contact with the flue gas and adsorb carbon dioxide.

[0049] The purified gas enters the guide hood 202 through the stroke channel 303 and is discharged through the delivery pipe 204. The gas detector 203 monitors the carbon dioxide concentration in real time. If the concentration exceeds the standard, the amine-modified activated carbon particles need to be replaced. When the adsorption is saturated, the valve is closed, the motor 205 is started to drive the screw 208 to rotate, and the nut 212 cooperates with the slider 209 to lift the closed cover 201, exposing the opening of the mesh cylinder 302. The closed cover 201 is then reset and the device is restarted.

[0050] By optimizing gas-solid contact efficiency through multi-layer swirling design, in traditional fixed beds, flue gas tends to flow along the path of least resistance, resulting in uneven utilization of activated carbon. This device uses a rotating plate 307 to force flue gas to form a vortex, extending the gas residence time. At the same time, the baffle plate 306 and the holes 308 divide the mesh cylinder 302 into multiple spaces, and the centrifugal force generated by the swirling helps the flue gas to penetrate the activated carbon layer evenly. The amine-modified activated carbon particles capture carbon dioxide. The maintenance structure 200 uses a motor-driven screw 208 to automatically lift and lower the closing cover 201, simplifying the activated carbon replacement process and avoiding the risk of sealing failure caused by manual operation.

[0051] The swirling design increases the contact area between flue gas and activated carbon, improving collection efficiency compared to traditional fixed beds. The vortex airflow continuously washes the surface of the activated carbon, and the tapping action of the rotating plate 307 effectively prevents particle accumulation. The gas detector 203 provides real-time feedback on emission data to ensure compliance with emission standards. When it is necessary to replace the amine-modified activated carbon particles, the motor 205 drives the screw 208 to rotate. Through the threaded engagement of the nut 212 and the screw 208, the closing cover 201 is lifted, and the ring plug 213 disengages from the upper part of the screen cylinder 302. New activated carbon is then transported into the screen cylinder 302 through the inspection port 210. Subsequently, the upper part of the screen cylinder 302 is closed. The electric maintenance structure 200 achieves automated operation, with short replacement time, significantly improving carbon collection efficiency and operational stability.

[0052] In the description of this utility model, it should also be noted that, unless otherwise explicitly specified and limited, the terms "set," "install," "connect," and "link" should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral connection; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; and they can refer to the internal connection of two components. Those skilled in the art can understand the specific meaning of the above terms in this utility model according to the specific circumstances.

[0053] Finally, it should be noted that the above description is merely a preferred embodiment of this utility model and is not intended to limit the utility model. Although the utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art can still modify the technical solutions described in the foregoing embodiments or make equivalent substitutions for some of the technical features. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of this utility model should be included within the protection scope of this utility model.

Claims

1. A multi-layer cyclone separator for carbon capture, characterized in that: Includes a separator (100), The carbon capture structure (300) includes a mesh cylinder (302) fixed inside the lower end of the separation cylinder (100) and open at the upper end, granular amine-modified activated carbon filled inside the mesh cylinder (302), partitions (306) evenly distributed on the inner wall of the mesh cylinder (302), holes (308) staggeredly distributed inside the partitions (306), a rotating shaft (305) rotatably installed inside the partitions (306), and rotating plates (307) arranged in a ring array between the partitions (306) and connected to the rotating shaft (305). as well as; The maintenance structure (200) includes a closed cover (201) located at the upper end of the mesh cylinder (302), a nut (212) located at one end of the closed cover (201), a slider (209) located at one end of the nut (212) and the closed cover (201), a guide rail (207) located on the inner wall of the mesh cylinder (302) and slidably mounted with the slider (209), a motor (205) located at the upper end of the separation cylinder (100), a bearing (206) embedded and mounted inside the upper end of the separation cylinder (100), and a screw (208) located at the lower end of the motor (205) and rotatably mounted inside the bearing (206) and threadedly connected to the nut (212).

2. The carbon capture multilayer cyclone separator according to claim 1, characterized in that: The upper end of the separation cylinder (100) is provided with a flow guide hood (202), the upper end of the flow guide hood (202) is provided with a conveying pipe (204), and a gas detector (203) is provided inside the conveying pipe (204).

3. The carbon capture multilayer cyclone separator according to claim 1, characterized in that: The separation cylinder (100) has an inspection port (210) at one end, and the outer wall of the separation cylinder (100) is provided with an inspection door (211) that covers the inspection port (210) and is fixed by bolts. The outer wall of the separation cylinder (100) is provided with a support frame (101).

4. The carbon capture multilayer cyclone separator according to claim 1, characterized in that: The lower end of the closed cover (201) is provided with a ring plug (213) that is annular and located in the upper opening of the mesh cylinder (302). The upper end of the closed cover (201) is provided with a motor (304) whose output end is rotatably mounted on the closed cover (201). The lower end of the motor (304) is provided with a rotating ring (313). The lower end of the rotating ring (313) is provided with rotating rods (314) arranged in a ring array. The upper end of the rotating shaft (305) is provided with a support ring (311). The upper end of the support ring (311) is provided with side rods (312) arranged in a ring array and located between the rotating rods (314).

5. The carbon capture multilayer cyclone separator according to claim 1, characterized in that: A travel channel (303) is provided between the separation cylinder (100) and the mesh cylinder (302). The upper end of the separation cylinder (100) is connected to the travel channel (303). The lower end of the separation cylinder (100) is provided with a discharge pipe (301) that is connected to the lower end of the mesh cylinder (302) and controlled by a valve.

6. The carbon capture multilayer cyclone separator according to claim 1, characterized in that: The lower end of the separation cylinder (100) is provided with a diffusion hood (309) whose radius decreases sequentially from top to bottom, and the lower end of the diffusion hood (309) is connected to an input pipe (310).

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