A carbon dioxide capture and catalytic recycling device

Abstract

The present invention discloses a carbon dioxide capture and catalytic recycling device, belonging to the technical field of carbon dioxide capture. The carbon dioxide capture and catalytic recycling device includes a first reactor and a second reactor, which are connected through a feeding channel. A circulating feed channel is arranged on the side wall of the first reactor, and a circulating discharge channel is arranged on the side wall of the second reactor. The circulating feed channel and the circulating discharge channel are connected through a transportation component, and a first driving component and a second driving component are respectively fixedly connected to the transportation component. The present invention uses hot steam as the power source instead of an electric motor as the power source, achieving the purpose of saving electric energy. The first reactor is assisted in heating by high-temperature carbon dioxide gas, reducing the operating power of the electric heater and achieving the purpose of energy conservation.

Description

Technical Field

[0001] The present invention relates to the technical field of carbon dioxide capture, and specifically provides a carbon dioxide capture and catalytic recycling device. Background Art

[0002] Carbon dioxide is a greenhouse gas. With the continuous increase in carbon dioxide emissions globally, the global greenhouse effect shows an upward trend. Therefore, the country actively advocates energy conservation and emission reduction. Since carbon dioxide has high utilization value in industry and agriculture, currently, carbon capture means are used to reduce the carbon dioxide content in the air, which can not only alleviate the greenhouse effect but also apply carbon dioxide in industry. Common carbon dioxide capture methods include chemical adsorption method, physical separation method, membrane separation method, calcium ion cycle method, etc. Among them, the calcium ion cycle method has the advantages of strong absorption capacity, high decarbonization efficiency, high recycled carbon concentration, cheap absorbent, and recyclable absorbent. Therefore, it has good market prospects.

[0003] In the calcium ion cycle method, calcium oxide is used as an adsorbent in the first reactor to adsorb carbon dioxide in the air at an appropriate temperature. During the adsorption process, calcium oxide reacts with carbon dioxide and moisture in the air to form calcium carbonate. The calcium carbonate is transported to the second reactor for high-temperature calcination. At high temperatures, calcium carbonate will produce calcium oxide and pure carbon dioxide. The pure carbon dioxide is collected or transported to the next process for use, and the calcium oxide formed after calcination is transported to the first reactor as an adsorbent through a transport device to achieve the purpose of recycling. However, currently, the general calcium oxide transport device is driven by an electric motor, which consumes a certain amount of electric energy. During the high-temperature calcination process in the second reactor, the temperature of the pure carbon dioxide produced is relatively high. The current calcium oxide transport device cannot use the high temperature of carbon dioxide as a driving form. When calcium oxide adsorbs carbon dioxide in the first reactor, a heating device is also required for heating, which also consumes electric energy. In the prior art, the high temperature of carbon dioxide is not used to assist in heating the first reactor, resulting in waste of thermal energy.

[0004] In view of the above problems, a carbon dioxide capture and catalytic recycling device is proposed. Summary of the Invention

[0005] The purpose of the present invention is to provide a carbon dioxide capture and catalytic recycling device. By using this device for operation, the problems in the above background that the calcium oxide transport device cannot use the high temperature of carbon dioxide as a driving form and that the high temperature of carbon dioxide is not used to assist in heating the first reactor are solved.

[0006] To achieve the above object, the present invention provides the following technical solution: A carbon dioxide capture and catalytic recycling device, comprising a first reactor and a second reactor, both of which are provided with electric heaters. The first reactor and the second reactor are connected through a material transfer channel. A circulating feed channel is provided on the side wall of the first reactor, and a buffer is provided at the connection of the circulating feed channel and the side wall of the first reactor. A circulating discharge channel is provided on the side wall of the second reactor, and a buffer is provided at the connection of the circulating discharge channel and the side wall of the second reactor. The circulating feed channel and the circulating discharge channel are connected through a transportation component. A first driving component and a second driving component are respectively fixedly connected to the transportation component. A water storage tank is fixedly installed on the side wall of the second reactor. A vibration component is provided in the inner cavity of the water storage tank. A condenser is fixedly installed on the top surface of the water storage tank. A pressurization chamber is fixedly installed on the side wall of the water storage tank. The pressurization chamber and the first driving component and the second driving component are respectively connected through steam pipelines. The condenser and the first driving component and the second driving component are respectively connected through steam pipelines. The first reactor and the second reactor are connected through a carbon dioxide pipeline, and the carbon dioxide pipeline penetrates through the inner cavity of the water storage tank and is connected to the vibration component;

[0007] The material transfer channel includes a slideway, and a through hole is provided on the slideway. The transportation component penetrates through the through hole. Connecting rods are respectively fixedly installed on the inner side walls of both sides of the inner cavity of the through hole, and both of the two connecting rods are fixedly connected to the transportation component;

[0008] The water storage tank includes a box body fixedly installed on the side wall of the second reactor and a water injection port fixedly connected and communicated on the side wall of the box body. A liquid level tube is also embedded on the side wall of the box body;

[0009] The vibration component includes a shell provided in the inner cavity of the box body. A plurality of vibration plates are respectively inserted through the top surface and the bottom surface of the shell. The shell is connected to the carbon dioxide pipeline;

[0010] The vibration plate includes a plurality of main vibration plates respectively inserted through the top surface and the bottom surface of the shell, and a plurality of auxiliary vibration plates are provided on each of the plurality of main vibration plates.

[0011] Furthermore, the transportation component includes a housing and a plurality of rollers rotatably installed on the inner wall of the inner cavity of the housing. The plurality of rollers are linearly arranged on the housing. The plurality of rollers are movably connected through a belt. A plurality of scraping plates are fixedly installed on the outer wall of the belt. The two ends of the roller at the lower end of the housing are respectively fixedly connected to the first driving component and the second driving component.

[0012] Further, the rotating roll includes a rotating roll body, and connecting shafts are fixedly connected to the side walls at both ends of the rotating roll body. The two connecting shafts are respectively fixedly connected to a first driving assembly and a second driving assembly.

[0013] Further, the first driving assembly includes an air chamber fixedly installed on the side wall of the housing. An air inlet channel and an air outlet channel are respectively formed on the air chamber, and the air inlet channel and the air outlet channel are respectively communicated with a steam pipeline. One end of the connecting shaft away from the rotating roll body penetrates and is rotatably arranged in the inner cavity of the air chamber, and a runner is fixedly connected to the end of the connecting shaft away from the rotating roll body. The runner is arranged in the inner cavity of the air chamber. The composition structure and connection mode of the first driving assembly and the second driving assembly are the same.

[0014] Further, the carbon dioxide pipeline includes a pipe body, and a plurality of bending parts are arranged on the pipe body. The plurality of bending parts are all arranged in the inner cavity of the box body.

[0015] Further, the first reactor includes a tank body and a gas valve fixedly installed on the top surface of the tank body in a communicating manner. The upper end of the gas valve is communicated with another carbon dioxide pipeline. A sandwich layer is arranged inside the tank body, and the sandwich layer is communicated with the second reactor through the carbon dioxide pipeline. A feeding port and a discharging port are respectively arranged on the outer side walls of both sides of the tank body. The feeding port is arranged above the discharging port, and the discharging port is communicated with a slideway. An air outlet is fixedly installed on the top surface of the tank body in a communicating manner, and an air inlet is formed on the bottom surface of the tank body.

[0016] Compared with the prior art, the beneficial effects of the present invention are as follows:

[0017] The present invention can use high-temperature carbon dioxide gas to heat water and generate hot steam, and then use the hot steam as a power source to drive the first driving assembly and the second driving assembly to operate, so as to realize the transportation of materials; using the hot steam as a power source instead of an electric motor as a power source not only achieves the purpose of saving electric energy, but also reduces the capital investment of the equipment. In addition, the recycling of water resources is realized; the hot steam is generated by using the waste heat of carbon dioxide. Such a setting improves the utilization rate of heat energy and reduces energy waste; when the carbon dioxide gas flows rapidly inside the housing, the main vibration plate vibrates, and the vibration is transmitted to the water through a plurality of auxiliary vibration plates, which is beneficial to the emission of hot steam in the water, provides a sufficient power source for the first driving assembly and the second driving assembly, and is also beneficial to uniformly heating the water; the high-temperature carbon dioxide gas generated in the second reactor will enter the sandwich layer through the carbon dioxide pipeline to assist in heating the tank body. On the premise of meeting the temperature requirements, the operating power of the electric heater can be reduced to achieve the purpose of energy saving. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] Figure 1 is the overall structural schematic diagram of the present invention;

[0019] Figure 2 Another perspective schematic diagram of the overall structure of the present invention;

[0020] Figure 3 Schematic cross-sectional view of the material transfer channel and the transportation component of the present invention;

[0021] Figure 4 Exploded schematic diagram of the transportation component of the present invention;

[0022] Figure 5 For the present invention Figure 4 Enlarged view of part A;

[0023] Figure 6 Schematic cross-sectional view of the first driving component of the present invention;

[0024] Figure 7 Schematic diagram of the installation positions among the water storage tank, the vibration component and the carbon dioxide pipeline of the present invention;

[0025] Figure 8 Schematic cross-sectional view of the vibration component and the carbon dioxide pipeline of the present invention;

[0026] Figure 9 Schematic cross-sectional view of the first reactor of the present invention.

[0027] In the figure: 1, the first reactor; 11, the tank body; 12, the interlayer; 13, the feeding port; 14, the discharging port; 15, the gas outlet; 16, the gas valve; 17, the gas inlet; 2, the second reactor; 3, the electric heater; 4, the material transfer channel; 41, the slideway; 42, the through hole; 43, the connecting rod; 5, the circulating feeding channel; 6, the circulating discharging channel; 7, the transportation component; 71, the outer shell; 72, the roller; 721, the roller body; 722, the connecting shaft; 73, the belt; 74, the scraper; 8, the first driving component; 81, the air chamber; 82, the air inlet channel; 83, the air outlet channel; 84, the runner; 9, the second driving component; 10, the water storage tank; 101, the box body; 102, the water injection port; 103, the liquid level tube; 20, the condenser; 30, the pressurizing chamber; 40, the vibration component; 401, the housing; 402, the vibration plate; 4021, the main vibration plate; 4022, the auxiliary vibration plate; 50, the steam pipeline; 60, the carbon dioxide pipeline; 601, the pipe body; 602, the bending part. Detailed implementation manners

[0028] 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. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

[0029] In order to solve the technical problem that the transportation component 7 cannot utilize the high temperature of carbon dioxide as a driving form and cannot achieve energy conservation, such as Figure 1-8 shown, the following preferred technical solutions are provided:

[0030] A carbon dioxide capture and catalytic recycling device includes a first reactor 1 and a second reactor 2. In the first reactor 1, calcium oxide is used as an adsorbent to adsorb carbon dioxide in the air at an appropriate temperature. During the adsorption process, calcium oxide reacts with carbon dioxide and moisture in the air to form calcium carbonate. The calcium carbonate is transported to the second reactor 2 for high-temperature calcination. At high temperatures, calcium carbonate will produce calcium oxide and pure carbon dioxide. Electric heaters 3 are provided on both the first reactor 1 and the second reactor 2. Through the setting of the electric heaters 3, the first reactor 1 and the second reactor 2 can be heated respectively to reach the appropriate reaction temperature and calcination temperature. The first reactor 1 and the second reactor 2 are connected through a feeding channel 4. The calcium carbonate generated in the first reactor 1 will slide into the second reactor 2 through the feeding channel 4 and then be calcined. A circulating feeding channel 5 is provided on the side wall of the first reactor 1, and a buffer is provided at the connection of the circulating feeding channel 5 and the side wall of the first reactor 1. A circulating discharging channel 6 is provided on the side wall of the second reactor 2, and a buffer is provided at the connection of the circulating discharging channel 6 and the side wall of the second reactor 2. The circulating feeding channel 5 and the circulating discharging channel 6 are connected through a transportation component 7. After the calcium carbonate in the second reactor 2 is calcined, it will produce calcium oxide and pure carbon dioxide, and the calcium oxide will fall into the circulating discharging channel 6, and then the transportation component 7 will transport the calcium oxide in the circulating discharging channel 6 to the circulating feeding channel 5 and finally slide into the first reactor 1 as an adsorbent for recycling.

[0031] A first driving component 8 and a second driving component 9 are respectively fixedly connected to the transportation component 7 to drive the transportation component 7 to operate and achieve the transportation effect. A water storage tank 10 is fixedly installed on the side wall of the second reactor 2 for storing water. A vibration component 40 is provided in the inner cavity of the water storage tank 10. When carbon dioxide passes through the vibration component 40, the vibration component 40 will produce a vibration effect. A condenser 20 is fixedly installed on the top surface of the water storage tank 10. A pressurizing chamber 30 is fixedly installed on the side wall of the water storage tank 10 for increasing the pressure of the hot steam. The pressurizing chamber 30 and the first driving component 8 and the second driving component 9 are respectively connected through a steam pipe 50. The condenser 20 and the first driving component 8 and the second driving component 9 are respectively connected through a steam pipe 50. The first reactor 1 and the second reactor 2 are connected through a carbon dioxide pipe 60. The carbon dioxide pipe 60 passes through the inner cavity of the water storage tank 10 and is connected to the vibration component 40.

[0032] The material conveying channel 4 includes a slideway 41, and a through hole 42 is provided on the slideway 41. The transportation component 7 is penetrated and arranged in the through hole 42. Connecting rods 43 are fixedly installed on the inner walls of both sides of the inner cavity of the through hole 42, and both of the two connecting rods 43 are fixedly connected to the transportation component 7. The calcium carbonate generated in the first reactor 1 will slide down through the slideway 41 into the second reactor 2 for calcination. The calcium oxide generated after calcination will be transported to the first reactor 1 through the transportation component 7 for recycling. During the operation of the transportation component 7, vibrations will be generated. The vibrations are conducted to the slideway 41 through the connecting rods 43, causing the slideway 41 to vibrate. Also, since the slideway 41 is inclined, it is beneficial for the calcium carbonate in the first reactor 1 to slide down through the slideway 41 into the second reactor 2, which can reduce the probability of blockage of the slideway 41. Since buffer members are provided at the connection between the circulating feed channel 5 and the side wall of the first reactor 1, and buffer members are provided at the connection between the circulating discharge channel 6 and the side wall of the second reactor 2, the vibrations on the slideway 41 will not be conducted to the first reactor 1 and the second reactor 2, and will not cause the first reactor 1 and the second reactor 2 to shake. Therefore, the carbon dioxide capture effect will not be affected.

[0033] The transportation component 7 includes a housing 71 and a plurality of rollers 72 rotatably installed on the inner wall of the inner cavity of the housing 71. The plurality of rollers 72 are linearly arranged on the housing 71. The plurality of rollers 72 are movably connected by a belt 73. A plurality of scraping plates 74 are fixedly installed on the outer wall of the belt 73. The two ends of the roller 72 at the lower end of the housing 71 are respectively fixedly connected to a first driving component 8 and a second driving component 9. The first driving component 8 and the second driving component 9 are driven to operate by hot steam. The first driving component 8 and the second driving component 9 will synchronously drive the roller 72 at the lower end of the housing 71 to rotate. The roller 72 drives the belt 73 and other rollers 72 to rotate. During the rotation of the belt 73, the calcium oxide in the circulating discharge channel 6 will be transported to the circulating feed channel 5 through the scraping plates 74. The calcium oxide then slides down from the circulating feed channel 5 into the first reactor 1. By repeating the above operations, the circulating transportation can be realized.

[0034] The roller 72 includes a roller body 721. Connecting shafts 722 are respectively fixedly connected to the side walls at both ends of the roller body 721. The two connecting shafts 722 are respectively fixedly connected to a first driving component 8 and a second driving component 9.

[0035] The first driving assembly 8 includes an air chamber 81 fixedly installed on the side wall of the housing 71. An air inlet channel 82 and an air outlet channel 83 are respectively formed on the air chamber 81. The air inlet channel 82 and the air outlet channel 83 are respectively communicated with the steam pipeline 50. One end of the connecting shaft 722 far away from the roller body 721 penetrates and is rotatably arranged in the inner cavity of the air chamber 81, and a runner 84 is fixedly connected to the end of the connecting shaft 722 far away from the roller body 721. The runner 84 is arranged in the inner cavity of the air chamber 81. The composition structure and connection mode of the first driving assembly 8 and the second driving assembly 9 are the same. The hot steam in the water storage tank 10 first enters the pressurizing chamber 30 for pressurization, and then enters the inner cavity of the air chamber 81 through the steam pipeline 50 and the air inlet channel 82, and blows the runner 84 to rotate. During the rotation of the runner 84, the roller body 721 will be driven to rotate through the connecting shaft 722, and then the whole conveying assembly 7 will be driven to operate. By adjusting the flow rate of the hot steam in the air inlet channel 82, the rotation speed of the runner 84 can be adjusted, and then the running speed of the conveying assembly 7 can be adjusted. It is relatively flexible to use. The hot steam flowing through the air chamber 81 will enter the condenser 20 through the air outlet channel 83 and the steam pipeline 50 for condensation. The condensed water after condensation enters the water storage tank 10 for recycling, saving water resources.

[0036] The water storage tank 10 includes a box body 101 fixedly installed on the side wall of the second reactor 2 and a water injection port 102 fixedly installed and communicated on the side wall of the box body 101. A liquid level pipe 103 is also embedded on the side wall of the box body 101, which is convenient for the operator to observe the water volume inside the box body 101 to confirm whether water needs to be replenished. When the operator adds water, it can be injected from the water injection port 102.

[0037] The carbon dioxide pipeline 60 includes a pipe body 601. A plurality of bending parts 602 are arranged on the pipe body 601. The plurality of bending parts 602 are all arranged in the inner cavity of the box body 101. The arrangement of the bending parts 602 can extend the residence time of carbon dioxide in the inner cavity of the box body 101 to obtain a good heating effect, which is beneficial to the generation of hot steam.

[0038] Specifically, during the process of carbon dioxide capture, first start the electric heater 3 to heat the first reactor 1 to an appropriate reaction temperature. At this time, introduce the gas flow into the first reactor 1, use calcium oxide as the adsorbent to adsorb carbon dioxide in the gas flow. During the adsorption process, calcium carbonate will be generated, and the calcium carbonate will slide down through the material transfer channel 4 into the second reactor 2 for calcination. After the calcium carbonate in the second reactor 2 is calcined, calcium oxide and pure carbon dioxide will be generated. At this time, the gas temperature of carbon dioxide is higher than the boiling point of water. Since the carbon dioxide pipeline 60 is arranged through the water storage tank 10, it can heat the water in the water storage tank 10 and generate hot steam. The hot steam enters the first driving component 8 and the second driving component 9 through the steam pipeline 50 respectively, driving the first driving component 8 and the second driving component 9 to rotate synchronously, and then driving the transportation component 7 to rotate. Finally, the calcium oxide generated in the second reactor 2 is transported to the first reactor 1 through the transportation component 7 for recycling. The hot steam flowing through the first driving component 8 and the second driving component 9 will enter the condenser 20 through the steam pipeline 50 respectively for condensation. The condensed water after condensation will enter the water storage tank 10, also realizing the recycling of water resources.

[0039] The present invention can use high-temperature carbon dioxide gas to heat water and generate hot steam, and then use the hot steam as the power source to drive the first driving component 8 and the second driving component 9 to operate, realizing the transportation of materials. Using the hot steam as the power source instead of the motor as the power source achieves the purpose of saving electric energy, reduces the capital investment of the equipment, and the hot steam is generated by using the waste heat of carbon dioxide. Such a setting improves the utilization rate of thermal energy and reduces energy waste.

[0040] To solve the technical problems of slow divergence of hot steam resulting in insufficient power of the first driving component 8 and the second driving component 9, and uneven heating of water, as Figure 7-8 shown, the following preferred technical solutions are provided:

[0041] The vibration component 40 includes a housing 401 arranged in the inner cavity of the box body 101. A plurality of vibration plates 402 are respectively inserted through the top surface and the bottom surface of the housing 401, and the housing 401 is communicated with the carbon dioxide pipeline 60.

[0042] The vibration plate 402 includes a plurality of main vibration plates 4021 respectively inserted through the top surface and the bottom surface of the housing 401, and a plurality of auxiliary vibration plates 4022 are arranged on the plurality of main vibration plates 4021.

[0043] Specifically, the carbon dioxide gas generated in the second reactor 2 will flow through the interior of the housing 401 via the carbon dioxide pipeline 60. When the carbon dioxide gas rapidly flows through the interior of the housing 401, it will exert a force on the main vibration plate 4021, thereby causing the main vibration plate 4021 to vibrate. The vibration generated by the main vibration plate 4021 is conducted to the water through a number of auxiliary vibration plates 4022, which not only helps the thermal steam in the water to dissipate, providing a sufficient power source for the first drive assembly 8 and the second drive assembly 9, but also helps to uniformly heat the water.

[0044] To solve the technical problem of the continuous high-power operation of the electric heater 3 and the consumption of electric energy, as Figure 1-Figure 9 shown, the following preferred technical solutions are provided:

[0045] The first reactor 1 includes a tank body 11 and a gas valve 16 fixedly installed on the top surface of the tank body 11 in a communicating manner. The upper end of the gas valve 16 is communicatively provided with another carbon dioxide pipeline 60. An interlayer 12 is provided inside the tank body 11. The interlayer 12 and the second reactor 2 are communicatively provided through the carbon dioxide pipeline 60. The carbon dioxide gas generated in the second reactor 2 will enter the interlayer 12 through the carbon dioxide pipeline 60 to heat the tank body 11. A feeding port 13 and a discharging port 14 are respectively provided on the outer walls of both sides of the tank body 11. The feeding port 13 is provided above the discharging port 14. When the dosage of calcium oxide adsorbent inside the tank body 11 is insufficient, feeding can be carried out through the feeding port 13. The discharging port 14 is communicatively provided with the slideway 41. The calcium oxide generated in the tank body 11 enters the slideway 41 from the discharging port 14 and finally enters the second reactor 2 for calcination. An air outlet 15 is fixedly installed on the top surface of the tank body 11 in a communicating manner. The air flow after adsorption will be discharged outward from the air outlet 15. An air inlet 17 is provided on the bottom surface of the tank body 11. The air flow that has not been adsorbed will enter the interior of the tank body 11 through the air inlet 17 for adsorption.

[0046] Specifically, the carbon dioxide gas generated in the second reactor 2 will enter the interlayer 12 through the carbon dioxide pipeline 60 to assist in heating the tank body 11. The carbon dioxide gas that has circulated in the interlayer 12 will flow into the next process for use or into a storage tank for storage and standby through the gas valve 16 and another carbon dioxide pipeline 60. Through such a setting, on the premise of meeting the temperature requirements, the operating power of the electric heater 3 can be reduced, achieving the purpose of energy conservation.

[0047] It should be noted that in this text, relational terms such as first and second are only used to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any actual relationship or order between these entities or operations. Moreover, the terms "comprising", "including" or any other variant thereof are intended to cover non-exclusive inclusion, so that a process, method, article or device comprising a series of elements not only includes those elements, but also includes other elements not expressly listed, or elements inherent to such process, method, article or device.

[0048] Although the embodiments of the present invention have been shown and described, those of ordinary skill in the art can understand that various changes, modifications, substitutions and variations can be made to these embodiments without departing from the principles and spirit of the present invention. The scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A carbon dioxide capture and catalytic recycling device, comprising a first reactor (1) and a second reactor (2), and electric heaters (3) are arranged on both the first reactor (1) and the second reactor (2), characterized in that: The first reactor (1) and the second reactor (2) are connected through a material transfer channel (4). A circulating feed channel (5) is provided on the side wall of the first reactor (1). A buffer is provided at the connection of the circulating feed channel (5) and the side wall of the first reactor (1). A circulating discharge channel (6) is provided on the side wall of the second reactor (2). A buffer is provided at the connection of the circulating discharge channel (6) and the side wall of the second reactor (2). The circulating feed channel (5) and the circulating discharge channel (6) are connected through a transportation component (7). A first driving component (8) and a second driving component (9) are respectively and fixedly connected to the transportation component (7). A water storage tank (10) is fixedly installed on the side wall of the second reactor (2). A vibration component (40) is provided in the inner cavity of the water storage tank (10). A condenser (20) is fixedly installed on the top surface of the water storage tank (10). A pressurizing chamber (30) is fixedly installed on the side wall of the water storage tank (10). The pressurizing chamber (30) and the first driving component (8) and the second driving component (9) are respectively connected through steam pipes (50). The condenser (20) and the first driving component (8) and the second driving component (9) are respectively connected through steam pipes (50). The first reactor (1) and the second reactor (2) are connected through a carbon dioxide pipe (60). The carbon dioxide pipe (60) is arranged through the inner cavity of the water storage tank (10), and the carbon dioxide pipe (60) is connected to the vibration component (40). The material transfer channel (4) includes a slideway (41). A through hole (42) is provided on the slideway (41). The transportation component (7) is arranged through the through hole (42). Connecting rods (43) are respectively and fixedly installed on the inner side walls of both sides of the inner cavity of the through hole (42), and both of the two connecting rods (43) are fixedly connected to the transportation component (7). The water storage tank (10) includes a box body (101) fixedly installed on the side wall of the second reactor (2) and a water injection port (102) connected and fixedly installed on the side wall of the box body (101). A liquid level pipe (103) is also embedded on the side wall of the box body (101). The vibration component (40) includes a shell (401) arranged in the inner cavity of the box body (101). A plurality of vibration plates (402) are respectively inserted through the top surface and the bottom surface of the shell (401). The shell (401) is connected to the carbon dioxide pipe (60). The vibration plate (402) includes a plurality of main vibration plates (4021) respectively inserted through the top surface and the bottom surface of the shell (401). A plurality of secondary vibration plates (4022) are provided on each of the plurality of main vibration plates (4021).

2. The carbon dioxide capture and catalytic recycling device according to claim 1, characterized in that: The transport component (7) includes a housing (71) and a plurality of rollers (72) rotatably mounted on the inner wall of the inner cavity of the housing (71). The plurality of rollers (72) are linearly arranged on the housing (71). The plurality of rollers (72) are movably connected by a belt (73). A plurality of scraping plates (74) are fixedly mounted on the outer wall of the belt (73). The two ends of the roller (72) at the lower end of the housing (71) are respectively fixedly connected to a first drive component (8) and a second drive component (9).

3. A carbon dioxide capture and catalytic recycling device according to claim 2, characterized in that: The roller (72) includes a roller body (721). Connecting shafts (722) are respectively fixedly connected to the side walls at both ends of the roller body (721). The two connecting shafts (722) are respectively fixedly connected to a first drive component (8) and a second drive component (9).

4. A carbon dioxide capture and catalytic recycling device according to claim 3, characterized in that: The first drive component (8) includes an air chamber (81) fixedly mounted on the side wall of the housing (71). An air inlet channel (82) and an air outlet channel (83) are respectively formed in the air chamber (81). The air inlet channel (82) and the air outlet channel (83) are respectively communicated with a steam pipe (50). One end of the connecting shaft (722) far from the roller body (721) penetrates and is rotatably arranged in the inner cavity of the air chamber (81). And a runner (84) is fixedly connected to one end of the connecting shaft (722) far from the roller body (721). The runner (84) is arranged in the inner cavity of the air chamber (81). The composition structure and connection mode of the first drive component (8) and the second drive component (9) are the same.

5. A carbon dioxide capture and catalytic recycling device according to claim 1, characterized in that: The carbon dioxide pipe (60) includes a pipe body (601). A plurality of bending parts (602) are arranged on the pipe body (601). The plurality of bending parts (602) are all arranged in the inner cavity of the box body (101).

6. A carbon dioxide capture and catalytic recycling device according to claim 1, characterized in that: The first reactor (1) includes a tank body (11) and a gas valve (16) fixedly connected and communicated on the top surface of the tank body (11). Another carbon dioxide pipe (60) is communicated and arranged at the upper end of the gas valve (16). A sandwich layer (12) is arranged inside the tank body (11). The sandwich layer (12) and the second reactor (2) are communicated through a carbon dioxide pipe (60). Feeding ports (13) and discharging ports (14) are respectively arranged on the outer walls on both sides of the tank body (11). The feeding port (13) is arranged above the discharging port (14). The discharging port (14) is communicated with a slideway (41). An air outlet (15) is fixedly connected and communicated on the top surface of the tank body (11). An air inlet (17) is formed in the bottom surface of the tank body (11).

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