An activated carbon production equipment for absorbing malodorous gases in high humidity environments

Abstract

The present invention provides an activated carbon production equipment for absorbing malodorous gases in a high-humidity environment, comprising a tetraethyl orthosilicate solution tank, a silane solution tank, a production tank, a vacuum tube, a protective air pipe, a heat conduction pipe, a first discharge pipe and a second discharge pipe. A containing box is placed in the production tank, a plurality of first through holes are opened on the containing box, a power motor is arranged on the production tank, the vacuum tube, the protective air pipe, the first discharge pipe and the second discharge pipe are all connected with the production tank, the tetraethyl orthosilicate solution tank is connected with the production tank through a first feed pipe, the first feed pipe, the second feed pipe, the vacuum tube, the protective air pipe, the first discharge pipe and the second discharge pipe are all provided with a first valve, the heat conduction pipe is connected to the production tank, and finally the purpose of heating, activating and modifying the activated carbon is achieved, and the modified activated carbon is not easy to adsorb water vapor, thereby improving the adsorption capacity of the malodorous gas, and at the same time, the activated carbon with low water content is less likely to be bacteria-producing and mildewed.

Description

Technical Field

[0001] The invention relates to an activated carbon production equipment for absorbing malodorous gases in a high-humidity environment. Background Art

[0002] The sources of malodorous gases are quite extensive, such as the collection and treatment of domestic waste, wastewater treatment, livestock and poultry breeding and excrement treatment, biological product processing, microbial fermentation pharmaceuticals, synthetic pharmaceuticals, etc. The malodorous gases in these industries not only have complex compositions, but also often contain a large amount of water vapor.

[0003] Activated carbon is widely used to absorb malodorous gases because of its advantages such as low price, wide sources, simple process for absorbing waste gas, and low operating costs. However, if the malodorous gas to be absorbed contains a large amount of water vapor, due to the hydrophilic groups contained in ordinary activated carbon, the water vapor will occupy a large amount of adsorption space of the activated carbon, which will greatly shorten the adsorption saturation time of the activated carbon and greatly reduce the adsorption capacity. When the activated carbon is saturated with adsorption, it will no longer have the adsorption function and has to be regenerated. This not only increases the operational complexity and operating costs of activated carbon adsorption, but is also not conducive to energy saving and emission reduction.

[0004] At present, a Chinese patent with authorization announcement number CN222153158U discloses a waste activated carbon cleaning device, including a support frame, a cleaning box, a stirring assembly and a screen vibration screen plate. Rotating shafts are provided on both sides of the cleaning box. The cleaning box is rotatable through the rotating shaft and is arranged in the middle of the support frame. The stirring assembly is slidably arranged in the support frame and is located above the cleaning box. Slide grooves are provided on both sides of the lower end of the support frame. The screen vibration screen plate is slidably arranged in the support frame and is located below the cleaning box. The stirring assembly includes a top cover, a drive motor, a stirring shaft and a stirring tube that are compatible with the cleaning box.

[0005] This waste activated carbon cleaning device uses water to clean the activated carbon. The water will occupy the adsorption space of the activated carbon, greatly shortening the adsorption saturation time of the activated carbon, so it is not very practical. Summary of the invention

[0006] In view of this, the purpose of the present invention is to provide an activated carbon production equipment for absorbing malodorous gases in high humidity environments, so as to achieve the purpose of enabling the activated carbon to adsorb malodorous gases but not easily adsorb water vapor.

[0007] In order to solve the above technical problems, the technical solution of the present invention is: an activated carbon production equipment for absorbing malodorous gases in a high-humidity environment, comprising a tetraethyl orthosilicate solution tank, a silane solution tank, a production tank, a vacuum tube, a protective air pipe, a heat pipe, a first discharge pipe and a second discharge pipe, a containing box for storing activated carbon is placed in the production tank, a plurality of first through holes are opened on the containing box, a power motor for driving the containing box to rotate is provided on the production tank, the vacuum tube, the protective air pipe, the first discharge pipe and the second discharge pipe are all connected to the production tank, the tetraethyl orthosilicate solution tank is connected to the production tank through a first feed pipe, the silane solution tank is connected to the production tank through a second feed pipe, the first feed pipe, the second feed pipe, the vacuum tube, the protective air pipe, the first discharge pipe and the second discharge pipe are all provided with a first valve, and the heat pipe is connected to the production tank.

[0008] To implement the above technical scheme, the ethyl orthosilicate ethanol solution in the ethyl orthosilicate solution tank is injected into the production tank and does not pass through the containing box, the power motor is turned on, the containing box is rotated, so that the activated carbon in the containing box is fully in contact with the ethyl orthosilicate solution, and after rotating for 2-4 hours, the power motor stops working, the first valve on the first discharge pipe is opened, the ethyl orthosilicate solution is discharged from the production tank, the power motor is turned on, the liquid on the activated carbon is recovered by centrifugal separation, the power motor is turned off, the vacuum equipment is turned on, the ethanol gas in the production tank is extracted from the production tank through the vacuum pipe, and then nitrogen is injected into the production tank through the protective gas pipe. The heat transfer pipe is connected to the heat transfer medium to heat the production tank, and the power motor is turned on at the same time to allow the gas in the production tank to flow so that the temperature in the production tank is uniform, and the activated carbon in the production tank is maintained at 90-115°C for 4-5 hours. After the production tank is cooled, the silane ethanol solution is injected into the production tank through the second feed pipe and covers the containing box, and the power motor is turned on to make the activated carbon in the containing box fully contact with the silane. After 8 hours of starting the power motor, the second discharge pipe is opened to discharge the silane ethanol solution from the production tank. After repeating the centrifugation, vacuuming and nitrogen addition processes, the production tank is heated to 100-120°C and kept warm for 6-8 hours. After cooling, the containing box is taken out of the production tank. The activated carbon processed by this equipment is modified so that water vapor is not easily adsorbed on the activated carbon, thereby greatly extending the adsorption saturation time of the activated carbon and improving the adsorption capacity of malodorous gases.

[0009] As a preferred embodiment of the present invention, it also includes an ethyl orthosilicate tank, an anhydrous ethanol tank, a silane tank, a first tee and a second tee, wherein the first port of the first tee is connected to the ethyl orthosilicate tank, the second port of the first tee is connected to the anhydrous ethanol tank, the third port of the first tee is connected to the ethyl orthosilicate solution tank, the first port of the second tee is connected to the silane tank, the second port of the second tee is connected to the anhydrous ethanol tank, the third port of the second tee is connected to the silane solution tank, and the first port of the first tee, the second port of the first tee, the first port of the second tee and the second port of the second tee are all provided with a second valve.

[0010] To implement the above technical solution, the second valve is opened, and the anhydrous ethanol in the anhydrous ethanol tank and the ethyl orthosilicate in the ethyl orthosilicate tank are injected into the ethyl orthosilicate solution tank along the first three-way pipe, so that the ratio of ethyl orthosilicate and anhydrous ethanol in the ethyl orthosilicate solution tank is adjusted to a suitable concentration; similarly, the ratio of silane and anhydrous ethanol in the silane solution tank is adjusted.

[0011] As a preferred embodiment of the present invention, the first discharge pipe is connected to a ethyl orthosilicate recovery tank, the ethyl orthosilicate recovery tank is connected to the ethyl orthosilicate solution tank through a first recovery pipe, and the first recovery pipe is connected to a first water pump.

[0012] By implementing the above technical solution, ethyl orthosilicate can be reused and production costs can be reduced.

[0013] As a preferred solution of the present invention, the second discharge pipe is connected to a silane recovery tank, the silane recovery tank is connected to the silane solution tank through a second recovery pipe, and the second recovery pipe is connected to a second water pump.

[0014] By implementing the above technical solution, silane can be reused and production costs can be reduced.

[0015] As a preferred solution of the present invention, a fixing rod is fixedly connected inside the production tank, a supporting tube is arranged on the fixing rod, a supporting plate for supporting a containing box is fixedly connected to the supporting tube, the power motor is started and causes the supporting tube to reciprocate along the length direction of the fixing rod and rotate along the axis of the fixing rod through a conducting component, a second through hole is opened on the supporting tube, and a plurality of containing boxes are stacked in the supporting tube.

[0016] To implement the above technical solution, multiple containing boxes are placed on a support plate and stacked, and then the power motor is turned on. Through the conduction component, the support tube is reciprocated along the length direction of the fixed rod and rotated along the axis of the fixed rod, so that the ethyl orthosilicate and silane can be more fully in contact with the activated carbon, thereby improving efficiency.

[0017] As a preferred solution of the present invention, the transmission component includes a first gear, a second gear, a power tube, a third gear, a fourth gear, a retaining ring, and a push rod. The first gear is connected to the power shaft of the power motor and is coaxially arranged. The second gear is rotatably connected to the production tank and meshes with the first gear. The power tube is fixed to the second gear and is coaxially arranged. A guide rod is fixedly connected to the outer wall of the power tube, and the length direction of the guide rod is parallel to the length direction of the power tube. A guide groove is provided on the support tube, and the guide rod is slidably connected to the guide groove. The fixed rod passes through the power tube and the second gear. The third gear is fixed to the fixed rod and is coaxially arranged. The fourth gear is rotatably connected to the outer wall of the power tube and meshes with the third gear. The push rod is fixed to the fourth gear and is non-coaxially arranged with the fourth gear. The retaining ring is fixed to the inner wall of the support tube, and the push rod supports the retaining ring.

[0018] To implement the above technical solution, the power motor is turned on, the power shaft drives the first gear to rotate, the first gear drives the second gear to rotate, the second gear and the power tube rotate synchronously, the guide rod contacts the inner wall of the guide groove, so that the support tube rotates synchronously with the power tube, at the same time, the fourth gear rotates around the axis of the power tube while the fourth gear rotates, the push rod contacts the retaining ring, so that the push rod pushes the support tube to move upward along the length direction of the power tube through the retaining ring, and then the support tube moves downward through the action of gravity, the push rod and the retaining ring always maintain contact, thereby realizing the movement state of the support tube rotating and moving up and down at the same time.

[0019] As a preferred solution of the present invention, an anti-dropout cover is threadedly connected to the support tube, the fixing rod passes through the anti-dropout cover, and the anti-dropout cover is in conflict with the containing box.

[0020] By implementing the above technical solution, the containing box is not easy to fall out of the supporting tube.

[0021] As a preferred solution of the present invention, a first vibration rod is connected to the outer wall of the power shaft, and the first vibration rod is used to beat the outer wall of the support tube.

[0022] To implement the above technical solution, the power shaft rotates, and the containing box in the support tube moves synchronously with the support tube. The first vibration rod hits the outer wall of the support tube, and the generated vibration is transmitted to the containing box, making it difficult for the activated carbon to adhere to the inner wall of the containing box. At the same time, the activated carbon can produce slight vibrations to enable the activated carbon to contact more fully with tetraethyl orthosilicate and silane.

[0023] As a preferred solution of the present invention, a sleeve is rotatably connected to the power shaft, and a second vibration rod for beating the outer wall of the support tube is fixedly connected to the sleeve. The power shaft rotates and drives the sleeve to rotate through a linkage assembly, and the directions of the sleeve and the power shaft are opposite.

[0024] To implement the above technical solution, the power shaft drives the first vibration rod to rotate while the second vibration rod is rotated through the linkage assembly. The first vibration rod and the second vibration rod both hit the outer wall of the support tube, and the directions of the first vibration rod and the second vibration rod are opposite, so that the opposite forces caused by the first vibration rod and the second vibration rod on the support tube can offset each other, reducing the impact on the support tube, thereby making the rotation of the support tube more stable.

[0025] As a preferred solution of the present invention, the linkage assembly includes a ring gear, a fifth gear, a sixth gear, and a seventh gear. The fifth gear is fixed on the sleeve, the sixth gear is fixed on the power shaft, and the seventh gear is rotatably connected to the production tank. The sixth gear and the seventh gear are located inside the ring gear, and the sixth gear and the seventh gear are both meshed with the ring gear, and the seventh gear is meshed with the fifth gear.

[0026] To implement the above technical solution, the power shaft drives the sixth gear to rotate, the sixth gear drives the seventh gear to rotate through the ring gear, the seventh gear drives the fifth gear to rotate, the fifth gear drives the sleeve to rotate, so that the sleeve drives the second vibration rod to rotate, so that the direction of rotation between the sleeve and the power shaft is opposite.

[0027] In summary, the present invention has the following beneficial effects:

[0028] 1. Silane is on the surface of activated carbon, making it difficult for water vapor to adsorb on the activated carbon, thereby greatly extending the adsorption saturation time of the activated carbon;

[0029] 2. The ethyl orthosilicate and silane in the ethyl orthosilicate recovery tank and the silane recovery tank can be reused to reduce production costs;

[0030] 3. Stack multiple containing boxes in the support tube. When the power shaft rotates, the support tube moves up and down and rotates at the same time, so that the activated carbon can fully contact with the tetraethyl orthosilicate and silane;

[0031] 4. During the process of the support tube moving up and down and rotating, the first vibration rod and the second vibration rod hit the outer wall of the support tube, and the vibration generated is transmitted to the activated carbon, so that the activated carbon is not easy to adhere to the inner wall of the containing box in large quantities;

[0032] 5. The first vibration rod and the second vibration rod have opposite directions of rotation, which has little impact on the support tube, so that the support tube can rotate smoothly. BRIEF DESCRIPTION OF THE DRAWINGS

[0033] Figure 1 It is a schematic diagram of the overall structure of the present invention;

[0034] Figure 2 A schematic diagram showing the location of the heat pipe;

[0035] Figure 3 A schematic diagram showing the position of the first vibration rod;

[0036] Figure 4 A schematic diagram showing the structure of the conduction component;

[0037] Figure 5 To illustrate the structural diagram of the linkage components;

[0038] Figure 6 A schematic diagram showing the position of the first gear;

[0039] Figure 7 To show the structural diagram of the power shaft;

[0040] Figure 8 A schematic diagram showing the structure of the containing box;

[0041] Fig. 9 To show the position diagram of the cylinder;

[0042] Fig.10 To show the structural diagram of the retaining ring;

[0043] Fig.11 It is a cross-sectional schematic diagram showing the seventh gear.

[0044] Figure numerals: 11, tetraethyl orthosilicate solution tank; 12, silane solution tank; 13, production tank; 131, cover plate; 132, power motor; 133, power shaft; 134, anti-drop cover; 14, vacuum tube; 15, protective air pipe; 16, heat conduction pipe; 17, first discharge pipe; 18, second discharge pipe; 19, first valve; 21, first three-way pipe; 22, tetraethyl orthosilicate tank; 23, anhydrous ethanol tank; 24, second three-way pipe; 25, silane tank; 26, second valve; 3, containing box; 31, first through hole; 41, tetraethyl orthosilicate recovery tank; 42, first recovery pipe; 43, first water pump; 44, second recovery pipe; 45. Silane recovery tank; 46. Second water pump; 51. Fixed rod; 52. Support tube; 53. Support plate; 54. Second through hole; 6. Conducting assembly; 61. First gear; 62. Second gear; 63. Power tube; 64. Third gear; 65. Fourth gear; 66. Retaining ring; 67. Push rod; 68. Guide rod; 69. Guide groove; 71. First vibration rod; 72. Sleeve; 73. Second vibration rod; 8. Linkage assembly; 81. Gear ring; 82. Fifth gear; 83. Sixth gear; 84. Seventh gear; 85. Baffle; 91. Upper connecting section; 92. Lower connecting section; 93. Groove; 94. Protrusion; 95. Cylinder. DETAILED DESCRIPTION

[0045] The specific implementation modes of the present invention are further described below in conjunction with the accompanying drawings to make the technical solutions of the present invention easier to understand and grasp.

[0046] An activated carbon production equipment for absorbing malodorous gases in a high-humidity environment includes a ethyl orthosilicate solution tank 11, a silane solution tank 12, a production tank 13, a vacuum pipe 14, a protective gas pipe 15, a heat conduction pipe 16, a first discharge pipe 17 and a second discharge pipe 18.

[0047] A container box 3 for storing activated carbon is placed in the production tank 13; a plurality of first through holes 31 are provided on the container box 3. A power motor 132 for driving the container box 3 to rotate is fixed on the cover plate 131 of the production tank 13, and the power motor 132 and the production tube are both arranged vertically.

[0048] The vacuum pipe 14, the protective gas pipe 15, the first discharge pipe 17 and the second discharge pipe 18 are all connected to the production tank 13. The first discharge pipe 17 and the second discharge pipe 18 are located at the lower end of the production tank 13. The ethyl orthosilicate solution tank 11 is connected to the production tank 13 through the first feed pipe; the silane solution tank 12 is connected to the production tank 13 through the second feed pipe, and the first feed pipe and the second feed pipe are close to the upper edge of the production tank 13. The first feed pipe, the second feed pipe, the vacuum pipe 14, the protective gas pipe 15, the first discharge pipe 17 and the second discharge pipe 18 are all provided with a first valve 19.

[0049] The first port of the first three-way pipe 21 is connected to the ethyl orthosilicate tank 22 , the second port of the first three-way pipe 21 is connected to the anhydrous ethanol tank 23 , and the third port of the first three-way pipe 21 is connected to the ethyl orthosilicate solution tank 11 .

[0050] The first port of the second three-way pipe 24 is connected to the silane tank 25 , the second port of the second three-way pipe 24 is connected to the anhydrous ethanol tank 23 , and the third port of the second three-way pipe 24 is connected to the silane solution tank 12 .

[0051] The first port of the first three-way pipe 21 , the second port of the first three-way pipe 21 , the first port of the second three-way pipe 24 , and the second port of the second three-way pipe 24 are all provided with a second valve 26 .

[0052] The second valve 26 is opened, and the ethyl orthosilicate in the ethyl orthosilicate tank 22 and the anhydrous ethanol in the anhydrous ethanol tank 23 are injected into the ethyl orthosilicate solution tank 11 along the first three-way pipe 21, so that the ethyl orthosilicate is diluted to obtain a suitable concentration ratio. Similarly, the silane in the silane tank 25 and the anhydrous ethanol in the anhydrous ethanol tank 23 are injected into the silane solution tank 12 along the second three-way pipe 24, so that the silane is diluted to obtain a suitable concentration ratio.

[0053] The mixture of ethyl orthosilicate and anhydrous ethanol in the ethyl orthosilicate solution tank 11 is injected into the production tank 13 and does not pass through the receiving box 3. The mixture contacts the activated carbon through the first through hole 31. The power motor 132 is turned on, and the receiving box 3 rotates. After rotating for 2-4 hours, the power motor 132 stops, and the first valve 19 on the first discharge pipe 17 is opened, and the ethyl orthosilicate is discharged from the production tank 13 and then centrifuged.

[0054] The vacuum equipment is turned on, and the anhydrous ethanol in the production tank 13 is extracted from the production tank 13 through the vacuum pipe 14, and then nitrogen is injected into the production tank 13 through the protective gas pipe 15. The heat conducting pipe 16 heats the production tank 13 after passing the heat conducting medium, and the power motor 132 is turned on at the same time, so that the gas in the production tank 13 can flow to make the temperature in the production tank 13 uniform, and the activated carbon is kept at 90-115℃ for 4-5h.

[0055] After the production tank 13 is cooled, the silane solution is injected into the production tank 13 through the second feed pipe and covers the containing box 3, and the power motor 132 is turned on to make the activated carbon in the containing box 3 fully contact with the silane solution. After 8 hours of starting the power motor 132, the second discharge pipe 18 is opened to discharge the silane solution from the production tank 13, and the centrifugation, vacuuming, nitrogen protection and heating to 100-120°C are repeated and kept warm for 6-8 hours. After cooling, the containing box 3 is taken out from the production tank 13. At this time, the activated carbon has been modified, and water vapor will not be easily adsorbed on the activated carbon, thereby greatly extending the adsorption saturation time of the activated carbon.

[0056] The first discharge pipe 17 is connected to the ethyl orthosilicate recovery tank 41, which is connected to the ethyl orthosilicate solution tank 11 through a first recovery pipe 42, and the first recovery pipe 42 is connected to a first water pump 43; the second discharge pipe 18 is connected to the silane recovery tank 45, which is connected to the silane solution tank 12 through a second recovery pipe 44, and the second recovery pipe 44 is connected to a second water pump 46.

[0057] The first water pump 43 is turned on, and the mixed liquid of anhydrous ethanol and ethyl orthosilicate in the ethyl orthosilicate recovery tank 41 is injected into the ethyl orthosilicate solution tank 11 for reuse. By injecting anhydrous ethanol and ethyl orthosilicate, a suitable ratio between anhydrous ethanol and ethyl orthosilicate in the ethyl orthosilicate solution tank 11 is achieved.

[0058] Similarly, by injecting anhydrous ethanol and silane, an appropriate ratio of anhydrous ethanol to silane is achieved in the silane solution tank 12 .

[0059] A vertically arranged fixing rod 51 is fixedly connected in the production tank 13. A supporting tube 52 is arranged on the fixing rod 51, and the supporting tube 52 is arranged coaxially with the fixing rod 51. A supporting plate 53 for supporting the containing box 3 is fixedly connected to the inner wall of the supporting tube 52, and the supporting plate 53 is arranged coaxially with the supporting tube 52. The fixing rod 51 passes through the supporting plate 53. A plurality of containing boxes 3 are stacked in the supporting tube 52, and the bottom containing box 3 is supported by the supporting plate 53.

[0060] The power motor 132 is started and causes the support tube 52 to reciprocate along the length direction of the fixing rod 51 and rotate along the axis of the fixing rod 51 through the transmission assembly 6. A second through hole 54 is formed in the support tube 52.

[0061] The transmission assembly 6 includes a first gear 61, a second gear 62, a power tube 63, a third gear 64, a fourth gear 65, a retaining ring 66, and a push rod 67. The first gear 61 is connected to the power shaft 133 of the power motor 132 and is coaxially arranged. The first gear 61 is rotatably connected to the production tank 13. The second gear 62 is rotatably connected to the production tank 13 and meshes with the first gear 61. The first gear 61 and the second gear 62 are both spur gears, and the third gear 64 and the fourth gear 65 are both bevel gears.

[0062] The power tube 63 is fixed on the second gear 62 and is coaxially arranged. A guide rod 68 is fixedly connected to the outer wall of the power tube 63, and the length direction of the guide rod 68 is parallel to the length direction of the power tube 63. A guide groove 69 is opened on the inner wall of the support tube 52, and the guide rod 68 is slidably connected in the guide groove 69.

[0063] The fixed rod 51 passes through the power tube 63 and the second gear 62. The fixed rod 51 is coaxially arranged with the power tube 63. The second gear 62 is rotatably connected to the fixed rod 51 through a bearing. The third gear 64 is fixed to the fixed rod 51 and coaxially arranged; the fourth gear 65 is rotatably connected to the outer wall of the power tube 63 and meshes with the third gear 64. The push rod 67 is fixed to the fourth gear 65 and non-coaxially arranged with the fourth gear 65. The length direction of the push rod 67 is parallel to the axial direction of the fourth gear 65. The retaining ring 66 is fixed to the inner wall of the support tube 52. The retaining ring 66 is coaxially arranged with the support tube 52. The push rod 67 supports the retaining ring 66.

[0064] The inner wall of the upper end of the support tube 52 is threadedly connected with an anti-drop cover 134. The anti-drop cover 134 abuts against the receiving box 3.

[0065] A first vibration rod 71 is connected to the outer wall of the power shaft 133, and the first vibration rod 71 is used to beat the outer wall of the support tube 52. A sleeve 72 is rotatably connected to the power shaft 133 through a bearing. A second vibration rod 73 is fixedly connected to the outer wall of the sleeve 72 for beating the outer wall of the support tube 52. The power shaft 133 rotates and drives the sleeve 72 to rotate through the linkage assembly 8; the sleeve 72 and the power shaft 133 have opposite directions of rotation.

[0066] The first vibration rod 71 and the second vibration rod 73 are both made of rubber.

[0067] The linkage assembly 8 includes a gear ring 81, a fifth gear 82, a sixth gear 83, and a seventh gear 84. The fifth gear 82, the sixth gear 83, and the seventh gear 84 are all spur gears. The fifth gear 82 is fixed to the sleeve 72 and is coaxially arranged, and the sixth gear 83 is fixed to the power shaft 133. The seventh gear 84 is rotatably connected to the production tank 13, and the sixth gear 83 and the seventh gear 84 are located inside the gear ring 81. The sixth gear 83 and the seventh gear 84 are both meshed with the gear ring 81, and the sixth gear 83 and the seventh gear 84 are distributed along the diameter direction of the gear ring 81. The seventh gear 84 is meshed with the fifth gear 82.

[0068] A baffle 85 is fixedly connected to the lower surfaces of the sixth gear 83 and the seventh gear 84. The lower surface of the gear ring 81 is supported by the baffle 85, and the upper surface of the gear ring 81 is limited by the sleeve 72.

[0069] The power shaft 133 includes an upper connecting section 91 and a lower connecting section 92. The lower end of the upper connecting section 91 has a groove 93 with a square cross section, and the upper end of the lower connecting section 92 has a protrusion 94 with a square cross section. The protrusion 94 is used to be embedded in the groove 93. Among them, the upper connecting section 91 is fixedly connected to the main machine of the power motor 132, and the lower connecting section 92 is fixedly connected to the sixth gear 83 and the first gear 61. A cylinder 95 is fixedly connected to the outer wall of the production tank 13, and the cover plate 131 is pushed up and down by the cylinder 95. When the cylinder 95 pushes the cover plate 131 to move up, the upper connecting section 91 is separated from the lower connecting section 92, so as to facilitate the placement of the container box 3 in the support tube 52 or the removal of the container box 3 from the support tube 52.

[0070] When the cylinder 95 drives the cover plate 131 to move downward, the upper connecting section 91 and the lower connecting section 92 are plugged into each other, and the upper connecting section 91 can drive the lower connecting section 92 to rotate.

[0071] Of course, the above are only typical examples of the present invention. In addition, the present invention may also have many other specific implementations. All technical solutions formed by equivalent replacement or equivalent transformation fall within the scope of protection required by the present invention.

Claims

1. An activated carbon production equipment for absorbing malodorous gases in high humidity environments, characterized by: It includes an ethyl orthosilicate solution tank, a silane solution tank, a production tank, a vacuum tube, a protective air pipe, a heat-conducting pipe, a first discharge pipe and a second discharge pipe. A containing box for storing activated carbon is placed in the production tank. A plurality of first through holes are provided on the containing box. A power motor for driving the containing box to rotate is provided on the production tank. The vacuum tube, the protective air pipe, the first discharge pipe and the second discharge pipe are all connected to the production tank. The ethyl orthosilicate solution tank is connected to the production tank through a first feed pipe. The silane solution tank is connected to the production tank through a second feed pipe. The first feed pipe, the second feed pipe, the vacuum tube, the protective air pipe, the first discharge pipe and the second discharge pipe are all provided with a first valve. The heat-conducting pipe is connected to the production tank. A fixing rod is fixedly connected to the production tank. A supporting pipe is provided on the fixing rod. A fixing rod is fixedly connected to the supporting pipe. A support plate is provided for supporting a containing box. The power motor is started and the transmission component is used to reciprocate the support tube along the length direction of the fixed rod while rotating the support tube along the axis of the fixed rod. A second through hole is provided on the support tube. A plurality of containing boxes are stacked in the support tube. The transmission component includes a first gear, a second gear, a power tube, a third gear, a fourth gear, a retaining ring, and a push rod. The first gear is connected to the power shaft of the power motor and is coaxially arranged. The second gear is rotatably connected to the production tank and meshes with the first gear. The power tube is fixed to the second gear and is coaxially arranged. The fixed rod passes through the power tube and the second gear. The third gear is fixed to the fixed rod and is coaxially arranged. The fourth gear is rotatably connected to the outer wall of the power tube and meshes with the third gear. The push rod is fixed to the fourth gear and is non-coaxially arranged with the fourth gear. The retaining ring is fixed to the inner wall of the support tube, and the push rod supports the retaining ring.

2. The activated carbon production equipment for absorbing malodorous gases in high humidity environments according to claim 1 is characterized by: It also includes an tetraethyl orthosilicate tank, an anhydrous ethanol tank, a silane tank, a first tee, and a second tee. The first port of the first tee is connected to the tetraethyl orthosilicate tank, the second port of the first tee is connected to the anhydrous ethanol tank, and the third port of the first tee is connected to the tetraethyl orthosilicate solution tank; the first port of the second tee is connected to the silane tank, the second port of the second tee is connected to the anhydrous ethanol tank, and the third port of the second tee is connected to the silane solution tank. The first port of the first tee, the second port of the first tee, the first port of the second tee, and the second port of the second tee are all provided with a second valve.

3. The activated carbon production equipment for absorbing malodorous gases in high humidity environments according to claim 2 is characterized by: The first discharge pipe is connected to a ethyl orthosilicate recovery tank, and the ethyl orthosilicate recovery tank is connected to a ethyl orthosilicate solution tank through a first recovery pipe, and the first recovery pipe is connected to a first water pump.

4. The activated carbon production equipment for absorbing malodorous gases in high humidity environments according to claim 3 is characterized by: The second discharge pipe is connected to a silane recovery tank, and the silane recovery tank is connected to a silane solution tank through a second recovery pipe, and the second recovery pipe is connected to a second water pump.

5. The activated carbon production equipment for absorbing malodorous gases in high humidity environments according to claim 1 is characterized by: A guide rod is fixedly connected to the outer wall of the power tube, and the length direction of the guide rod is parallel to the length direction of the power tube. A guide groove is opened on the support tube, and the guide rod is slidably connected in the guide groove.

6. The activated carbon production equipment for absorbing malodorous gases in high humidity environments according to claim 5 is characterized by: An anti-dropout cover is threadedly connected to the support tube, the fixing rod passes through the anti-dropout cover, and the anti-dropout cover is in conflict with the containing box.

7. The activated carbon production equipment for absorbing malodorous gases in high humidity environments according to claim 6 is characterized by: A first vibration rod is connected to the outer wall of the power shaft, and the first vibration rod is used to beat the outer wall of the support tube.

8. The activated carbon production equipment for absorbing malodorous gases in high humidity environments according to claim 7 is characterized by: The power shaft is rotatably connected with a sleeve, and the sleeve is fixedly connected with a second vibration rod for beating the outer wall of the support tube. The power shaft rotates and drives the sleeve to rotate through a linkage assembly, and the sleeve and the power shaft have opposite directions.

9. The activated carbon production equipment for absorbing malodorous gases in high humidity environments according to claim 8 is characterized by: The linkage assembly includes a ring gear, a fifth gear, a sixth gear, and a seventh gear. The fifth gear is fixed on the sleeve, the sixth gear is fixed on the power shaft, and the seventh gear is rotatably connected to the production tank. The sixth gear and the seventh gear are located inside the ring gear. The sixth gear and the seventh gear are both meshed with the ring gear, and the seventh gear is meshed with the fifth gear.

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