Chemical reaction kettle waste gas treatment device

Abstract

The invention relates to the technical field of waste gas treatment, and provides a chemical reaction kettle waste gas treatment device which comprises a base, a liquid adsorption assembly is arranged on one side of the top end of the base and comprises a spraying adsorption treatment tank, and a heating assembly is arranged on the side, located on the spraying adsorption treatment tank, of the top end of the base; according to the device, waste gas enters the gas distribution plate and is sprayed out through small holes in the gas distribution plate, small bubbles are formed in liquid, the rising speed of the small bubbles is low, components in the gas can be adsorbed by the liquid, the motor is started, the motor drives the rotating rod to rotate, the rotating rod drives the stirring blades and the bubble dispersion plate to work, and the stirring blades stir the liquid; according to the gas-liquid separator, the gas-liquid separator is arranged, so that fine bubbles stay in liquid for a longer time and are fully mixed, the bubble dispersion plate reciprocates up and down through the reciprocating groove to extrude the liquid and the fine bubbles, gas fusion is increased, and the gas dispersion plate is provided with a plurality of fine holes, so that the gas rising speed can be limited, and the adsorption effect can be improved.

Description

Technical Field

[0001] The invention relates to the technical field of waste gas treatment, and in particular to a waste gas treatment device for a chemical reactor. Background Art

[0002] Chemical reactor waste gas usually contains a variety of harmful substances, such as volatile organic compounds (VOCs), acidic gases, alkaline gases, dust, etc. If these waste gases are directly discharged without effective treatment, they will cause serious harm to the environment and human health. Therefore, the application of chemical reactor waste gas treatment equipment is of great significance to achieving sustainable development and protecting the environment.

[0003] As disclosed in the publication number CN111228947A, the embodiment of the invention discloses a waste gas treatment device for a chemical reactor, which specifically relates to the field of waste gas treatment technology, including a device bracket, a reactor is fixedly arranged on one side of the device bracket, a mounting bracket is fixedly arranged on the top of the other side of the device bracket, a spray treatment tank is fixedly arranged in the middle of the mounting bracket, a vacuum pump is fixedly arranged on the top of the device bracket, the input end of the vacuum pump is fixedly connected to the exhaust port of the reactor, an air pipe is fixedly arranged on the output end of the vacuum pump, and an air inlet is fixedly arranged at the bottom of the spray treatment tank. The invention filters and purifies the gas by spraying and filtering the waste gas, and the installation page installs the filter purification core on the fixed shaft, which is convenient for removing the filter purification core from the air purification filter cartridge. Various types of filter purification cores improve the purification effect, and the filter purification core is convenient for maintenance and replacement, which is convenient for maintenance and use of the treatment device.

[0004] In the above-mentioned prior art, the staff adds the waste gas into the treatment barrel through the air inlet pipe, and the gas emerges from the solution at the bottom of the interior. While passing through the solution, the harmful substances in the liquid are adsorbed, and then the spray component sprays and adsorbs the gas again. Then the gas enters the activated carbon adsorption component through the delivery pipeline to complete the final treatment and is then discharged. However, the waste gas continuously enters the treatment barrel, so when passing through the solution, the speed is too fast, resulting in poor solution adsorption effect, and the activated carbon group needs to be cleaned regularly for long-term adsorption, otherwise it will affect the adsorption effect. During the cleaning of the activated carbon group, the equipment needs to be stopped, which will waste a lot of time. Summary of the invention

[0005] The purpose of the present invention is to solve the problem in the prior art that waste gas continuously enters the treatment barrel, so when passing through the solution, the speed is too fast, resulting in poor solution adsorption effect, and the activated carbon group needs to be cleaned regularly after long-term adsorption, otherwise it will affect the adsorption effect, and during the cleaning of the activated carbon group, the equipment needs to be stopped, which will waste a lot of time.

[0006] In order to achieve the above-mentioned objectives, the present invention adopts the following technical scheme: a chemical reactor waste gas treatment device, comprising a base, a liquid adsorption component is arranged on one side of the top of the base, the liquid adsorption component comprises a spray adsorption treatment tank, the top of the base is located at a side of the spray adsorption treatment tank and a heating component is arranged, the heating component comprises a heating box, the top of the heating box is provided with an activated carbon adsorption component, the activated carbon adsorption component comprises an adsorption box, a plurality of adsorption boxes are arranged and are stacked on the top of the heating box, a cooling component is arranged on the top of the base at a side of the heating box away from the spray adsorption treatment tank, the cooling component comprises a cooling box, the spray adsorption treatment tank, the heating box and the cooling box are all fixedly connected to the base, a first air inlet pipe is fixedly connected to the middle of the bottom end of the spray adsorption treatment tank, the first air inlet pipe passes through the spray adsorption treatment tank, and one end of the first air inlet pipe located inside the spray adsorption treatment tank is fixedly connected to a gas separator, and the gas separator is fixedly connected to the spray adsorption treatment tank.

[0007] As a preferred embodiment, a motor is fixedly connected to the middle part of the top of the spray adsorption treatment tank, and a rotating rod is transmission-connected to the bottom end of the motor, the rotating rod penetrates the spray adsorption treatment tank and is rotationally connected to the spray adsorption treatment tank, and reciprocating grooves are arranged equidistantly at the bottom end of the rotating rod, and the rotating rod is threadedly connected to a bubble dispersion plate through the reciprocating grooves, and the two radial sides of the bubble dispersion plate are fixedly connected to limit sliders, and the rotating rod is fixedly connected to a stirring blade on the side opposite to the bubble dispersion plate, and limit slide grooves are provided on both sides of the interior of the spray adsorption treatment tank, and the limit slide grooves are slidably connected to the limit slide The exhaust gas enters the gas separator and is ejected through the tiny holes on the gas separator to form tiny bubbles in the liquid. The tiny bubbles rise slowly, which helps the components in the gas to be adsorbed by the liquid. The motor is started, and the motor drives the rotating rod to rotate. The rotating rod drives the stirring blades and the bubble dispersion plate to work. The stirring blades stir the liquid, so that the tiny bubbles stay in the liquid for a longer time and are fully mixed. The bubble dispersion plate reciprocates up and down through the reciprocating groove, which squeezes the liquid and small bubbles, thereby increasing gas fusion. In addition, a number of tiny holes are arranged on the bubble dispersion plate to limit the rising speed of the gas and improve the adsorption effect.

[0008] As a preferred embodiment, the rotating rod is located in the top annular array inside the spray adsorption treatment tank and is fixedly connected to a fixed rod, the fixed rod is fixedly connected to a rotating water ring at one end away from the rotating rod, the inner annular array of the rotating water ring is fixedly connected to an atomizing nozzle, the top of the rotating water ring is rotatably connected to a supporting water ring, the top of one side of the supporting water ring is fixedly connected to the spray adsorption treatment tank, the rising gas enters the top of the blocking plate through the gas buffer plate, the rotation of the rotating rod drives the fixed rod to rotate, the fixed rod drives the supporting water ring to rotate, the supporting water ring rotates to spray water mist through the atomizing nozzle, and works on the exhaust gas.

[0009] As a preferred embodiment, a first circulation pipe is fixedly connected to the top of one side of the supporting water ring, both ends of the first circulation pipe penetrate the spray adsorption treatment tank and are fixedly connected to the spray adsorption treatment tank, the first circulation pipe is located at the top of the spray adsorption treatment tank and is fixedly connected to a water pump, the rotating rod is located at the bottom end of the rotating water ring and is fixedly connected to a baffle plate, gas buffer plates are provided on both sides of the baffle plate, and the water pump is started to allow the liquid inside the spray adsorption treatment tank to enter the first circulation pipe, and then enter the supporting water ring and the rotating water ring, and finally be sprayed out through the atomizing nozzle.

[0010] As a preferred embodiment, an activated carbon plate is provided inside the adsorption box, and a first branch air inlet pipe is fixedly connected to one radial side of the adsorption box, and the end of the first branch air inlet pipe away from the adsorption box is fixedly connected to the top of the spray adsorption treatment tank, and the two ports of the first branch air inlet pipe close to the adsorption box are provided with a first solenoid valve, and the gas enters the corresponding adsorption box through a branch port of the first branch air inlet pipe, and the activated carbon plate adsorbs the incoming gas, thereby adsorbing organic matter.

[0011] As a preferred embodiment, the adsorption box is fixedly connected to a second branch air intake pipe on the side away from the first branch air intake pipe, the end of the second branch air intake pipe away from the adsorption box is fixedly connected to the heating box, two ports of the second branch air intake pipe close to the adsorption box are provided with second solenoid valves, and the end of the second branch air intake pipe close to the heating box is fixedly connected to the first fan, the adsorbed gas enters the heating box through the corresponding second branch air intake pipe, and the incoming exhaust gas is heated by the heating pipe. When an activated carbon plate is adsorbed to a saturated state, the corresponding first solenoid valve and second solenoid valve are closed, and the other first solenoid valve and second solenoid valve are opened for alternating adsorption.

[0012] As a preferred embodiment, a heating pipe is fixedly connected to the interior of the heating box, a high-temperature chamber is opened in the wall of the heating box, a heat sink is fixedly connected to the central annular array of the heating box located inside the high-temperature chamber, a third branch air intake pipe is fixedly connected to one side of the heating box, the top of the third branch air intake pipe is respectively fixedly connected to the adsorption box, the exhaust gas is converted into carbon dioxide and water vapor under the action of the catalyst, and the high temperature generated during this period causes the temperature inside the high-temperature chamber to rise, and the high-temperature gas in the high-temperature chamber enters the third branch air intake pipe through the operation of the second fan.

[0013] As a preferred embodiment, the two ports at the top of the third branch air intake pipe are fixedly connected to the third solenoid valve, the bottom of the third branch air intake pipe is fixedly connected to the second fan, and an exhaust assembly is provided on the side of the top of the heating box away from the third branch air intake pipe, which enters into the adsorption box of the activated carbon plate in a saturated state, thereby desorbing the organic matter on the activated carbon plate, and the desorbed organic matter enters the heating pipe again through the second branch air intake pipe for catalytic combustion, thereby completely treating the exhaust gas.

[0014] As a preferred embodiment, the exhaust assembly includes an air connecting pipe, both ends of the air connecting pipe are fixedly connected to the heating box and the cooling box, a fixed cylinder is fixedly connected to the side of the connecting pipe away from the heating box, a push rod is slidably connected to the end of the fixed cylinder close to the heating box, the push rod passes through the fixed cylinder, a spring is fixedly connected to the end of the push rod located inside the fixed cylinder, the spring is fixedly connected to the fixed cylinder, a piston is fixedly connected to the end of the push rod away from the fixed cylinder, the piston is slidably connected to the air connecting pipe, the bottom end of the air connecting pipe is fixedly connected to an exhaust pipe, and the exhaust pipe is fixedly connected to the cooling box at one end away from the connecting pipe. When the heating box burns for a long time, there are more water vapor and carbon dioxide inside, and the pressure generated pushes the piston. After the piston is under pressure, it slides to one side of the cooling box and squeezes the push rod. The push rod moves to push the spring, and the spring is gradually compressed. The spring will continue to apply pressure to the piston, so that the piston is always in a pushed state, and the carbon dioxide and water vapor are discharged into the cooling box through the exhaust pipe. Therefore, the continuous squeezing and sealing of the piston effectively prevents the internal gas of the heating box from being discharged, so that the gas combustion is more complete.

[0015] As a preferred embodiment, a controller is fixedly connected to the top of the cooling box, and staggered baffles are fixedly connected to the inside of the cooling box at equal intervals, and the staggered baffles are staggered up and down. A cooling pipe is fixedly connected to the inside of the cooling box, and the cooling pipe is fixedly connected to the staggered baffles. The staggered baffles buffer the incoming carbon dioxide and water vapor, and the cooling pipe cools the carbon dioxide and water vapor, and the cooled water is discharged and collected.

[0016] The beneficial effects of the present invention are as follows:

[0017] 1. In the present invention, the exhaust gas enters the gas separator plate and is ejected through the tiny holes on the gas separator plate to form tiny bubbles in the liquid. The tiny bubbles rise slowly, which helps the components in the gas to be adsorbed by the liquid. The motor is started, and the motor drives the rotating rod to rotate. The rotating rod drives the stirring blades and the bubble dispersion plate to work. The stirring blades stir the liquid, so that the tiny bubbles stay in the liquid for a longer time and are fully mixed. The bubble dispersion plate reciprocates up and down through the reciprocating groove, so that the liquid and the small bubbles are squeezed, thereby increasing gas fusion. In addition, a number of tiny holes are arranged on the bubble dispersion plate to limit the rising speed of the gas and improve the adsorption effect.

[0018] 2. In the present invention, the gas treated by the spray adsorption treatment tank enters the corresponding adsorption box through a branch port of the first branch air inlet pipe, the activated carbon plate adsorbs the incoming gas, thereby adsorbing organic matter, and the adsorbed gas enters the heating box through the corresponding second branch air inlet pipe, and the incoming exhaust gas is heated by the heating pipe. When one activated carbon plate is adsorbed to a saturated state, the corresponding first solenoid valve and second solenoid valve are closed, and the other first solenoid valve and second solenoid valve are opened to perform alternating adsorption, and the exhaust gas is converted into carbon dioxide and water vapor under the action of the catalyst, and the high temperature generated during this period increases the temperature inside the high-temperature bin, and through the operation of the second fan, the high-temperature gas in the high-temperature bin enters the third branch air inlet pipe and enters the adsorption box in the activated carbon plate in a saturated state, thereby desorbing the organic matter on the activated carbon plate, and the desorbed organic matter enters the heating pipe through the second branch air inlet pipe again for catalytic combustion, thereby completely treating the exhaust gas, and the activated carbon plate can perform adsorption again.

[0019] 3. In the present invention, when the combustion is carried out for a long time in the heating box, there are more water vapor and carbon dioxide inside, and the pressure generated pushes the piston. After the piston is under pressure, it slides to one side of the cooling box and squeezes the push rod. The push rod moves to push the spring, and the spring is gradually compressed. The spring will continue to pressurize the piston, so that the piston is always in a pushing state, and the carbon dioxide and water vapor are discharged into the cooling box through the exhaust pipe. Therefore, the continuous squeezing and sealing of the piston effectively prevents the internal gas of the heating box from being discharged, so that the gas burns more completely, and the staggered baffles have a buffering effect on the incoming carbon dioxide and water vapor, and the cooling pipe cools the carbon dioxide and water vapor, and the cooled water is discharged and collected. BRIEF DESCRIPTION OF THE DRAWINGS

[0020] Figure 1 A schematic diagram of the structure of a chemical reactor waste gas treatment device provided by the present invention;

[0021] Figure 2 A schematic cross-sectional structure diagram of a chemical reactor waste gas treatment device provided by the present invention;

[0022] Figure 3 A schematic diagram of the structure of a liquid adsorption component of a chemical reactor waste gas treatment device provided by the present invention;

[0023] Figure 4 A schematic diagram of the explosion structure of a liquid adsorption component of a chemical reactor waste gas treatment device provided by the present invention;

[0024] Figure 5 A schematic diagram of the structure of a baffle plate of a chemical reactor waste gas treatment device provided by the present invention;

[0025] Figure 6 A schematic diagram of the structure of a heating component of a chemical reactor waste gas treatment device provided by the present invention;

[0026] Figure 7 A schematic diagram of the exhaust assembly structure of a chemical reactor waste gas treatment device provided by the present invention;

[0027] Figure 8 A schematic diagram of the cooling assembly structure of a chemical reactor waste gas treatment device provided by the present invention;

[0028] Legend:

[0029] 1. Base; 21. Spray adsorption treatment tank; 22. First air inlet pipe; 23. Air distributor plate; 24. Motor; 25. Rotating rod; 251. Reciprocating groove; 26. Bubble dispersion plate; 261. Limiting slider; 27. Stirring blade; 28. First circulation pipe; 29. ​​Water pump; 210. Support water ring; 211. Rotating water ring; 2111. Atomizing nozzle; 2112. Fixed rod; 212. Blocking plate; 2121. Gas buffer plate; 213. Limiting slide; 31. Adsorption box; 32. Activated carbon plate; 33. The first branch air intake pipe; 34, the first solenoid valve; 35, the second branch air intake pipe; 36, the second solenoid valve; 37, the first fan; 41, the heating box; 42, the high-temperature chamber; 43, the heat sink; 44, the heating pipe; 45, the third branch air intake pipe; 46, the second fan; 47, the third solenoid valve; 48, the connecting air pipe; 481, the fixing cylinder; 482, the spring; 483, the push rod; 484, the piston; 485, the exhaust pipe; 51, the cooling box; 52, the controller; 53, the cooling pipe; 54, the staggered baffle. DETAILED DESCRIPTION

[0030] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0031] See also Figure 1 - Figure 8 The present invention provides a technical solution: a chemical reactor waste gas treatment device, comprising a base 1, a liquid adsorption component is arranged on one side of the top of the base 1, the liquid adsorption component comprises a spray adsorption treatment tank 21, a heating component is arranged on the top of the base 1 located on one side of the spray adsorption treatment tank 21, the heating component comprises a heating box 41, an activated carbon adsorption component is arranged on the top of the heating box 41, the activated carbon adsorption component comprises an adsorption box 31, a plurality of adsorption boxes 31 are arranged, and they are superimposed on the top of the heating box 41, a cooling component is arranged on the top of the base 1 located on the side of the heating box 41 away from the spray adsorption treatment tank 21, the cooling component comprises a cooling box 51, the spray adsorption treatment tank 21, the heating box 41 and the cooling box 51 are all fixedly connected to the base 1, a first air inlet pipe 22 is fixedly connected to the middle of the bottom end of the spray adsorption treatment tank 21, the first air inlet pipe 22 penetrates the spray adsorption treatment tank 21, and an end of the first air inlet pipe 22 located inside the spray adsorption treatment tank 21 is fixedly connected to a gas distributor 23, and the gas distributor 23 is fixedly connected to the spray adsorption treatment tank 21.

[0032] like Figure 1 - Figure 8 As shown, a motor 24 is fixedly connected to the middle of the top of the spray adsorption treatment tank 21, and a rotating rod 25 is transmission-connected to the bottom of the motor 24. The rotating rod 25 penetrates the spray adsorption treatment tank 21 and is rotatably connected to the spray adsorption treatment tank 21. Reciprocating grooves 251 are arranged equidistantly at the bottom of the rotating rod 25. The rotating rod 25 is threadedly connected to a bubble dispersion plate 26 through the reciprocating grooves 251. The two radial sides of the bubble dispersion plate 26 are fixedly connected to a limiting slider 261. The rotating rod 25 is located on the side opposite to the bubble dispersion plate 26 and is fixedly connected to a stirring blade 27. Limiting slide grooves 213 are provided on both sides of the interior of the spray adsorption treatment tank 21. The limiting slide grooves 213 are slidably connected to the limiting slider 261. The rotating rod 25 is located at the top of the spray adsorption treatment tank 21. The circular array is fixedly connected to the fixed rod 21 12. The end of the fixed rod 2112 away from the rotating rod 25 is fixedly connected to the rotating water ring 211, the internal annular array of the rotating water ring 211 is fixedly connected to the atomizing nozzle 2111, the top of the rotating water ring 211 is rotatably connected to the supporting water ring 210, the top of one side of the supporting water ring 210 is fixedly connected to the spray adsorption treatment tank 21, the top of one side of the supporting water ring 210 is fixedly connected to the first circulation pipe 28, both ends of the first circulation pipe 28 pass through the spray adsorption treatment tank 21 and are fixedly connected to the spray adsorption treatment tank 21, the first circulation pipe 28 is located at the top of the spray adsorption treatment tank 21 and is fixedly connected to the water pump 29, the rotating rod 25 is located at the bottom of the rotating water ring 211 and is fixedly connected to the blocking plate 212, and gas buffer plates 2121 are provided on both sides of the blocking plate 212.

[0033] In this embodiment, the exhaust gas enters the gas separator 23 and is ejected through the tiny holes on the gas separator 23 to form tiny bubbles in the liquid. The tiny bubbles rise slowly, which helps the components in the gas to be adsorbed by the liquid. The motor 24 is started, and the motor 24 drives the rotating rod 25 to rotate. The rotating rod 25 drives the stirring blade 27 and the bubble dispersion plate 26 to work. The stirring blade 27 stirs the liquid, so that the tiny bubbles stay in the liquid for a longer time and are fully mixed. The bubble dispersion plate 26 reciprocates up and down through the reciprocating groove 251, so that the liquid and the small bubbles are squeezed, thereby increasing gas fusion. In addition, a number of tiny holes are provided on the bubble dispersion plate 26 to limit the rising speed of the gas and improve the adsorption effect. The rising gas enters the top of the blocking plate 212 through the gas buffer plate 2121. The rotating rod 25 rotates to drive the fixed rod 2112 to rotate, and the fixed rod 2112 drives the supporting water ring 210 to rotate. The supporting water ring 210 rotates through the atomizing nozzle 2111 to spray water mist to spray the exhaust gas.

[0034] like Figure 1 - Figure 8 As shown, an activated carbon plate 32 is arranged inside the adsorption box 31, a first branch air intake pipe 33 is fixedly connected to one radial side of the adsorption box 31, one end of the first branch air intake pipe 33 away from the adsorption box 31 is fixedly connected to the top of the spray adsorption treatment tank 21, and two ports of the first branch air intake pipe 33 close to the adsorption box 31 are both provided with a first solenoid valve 34, a second branch air intake pipe 35 is fixedly connected to one side of the adsorption box 31 away from the first branch air intake pipe 33, one end of the second branch air intake pipe 35 away from the adsorption box 31 is fixedly connected to the heating box 41, and two ports of the second branch air intake pipe 35 close to the adsorption box 31 are both provided with a second solenoid valve 36, and the second branch air intake pipe 35 is fixedly connected to the heating box 41. The first fan 37 is fixedly connected to one end close to the heating box 41, a heating pipe 44 is fixedly connected to the inside of the heating box 41, a high-temperature chamber 42 is provided in the wall of the heating box 41, a heat sink 43 is fixedly connected to the central ring array of the heating box 41 located inside the high-temperature chamber 42, a third directional air inlet pipe 45 is fixedly connected to one side of the heating box 41, the top of the third directional air inlet pipe 45 is respectively fixedly connected to the adsorption box 31, two ports at the top of the third directional air inlet pipe 45 are fixedly connected to the third solenoid valve 47, the bottom of the third directional air inlet pipe 45 is fixedly connected to the second fan 46, and an exhaust assembly is provided on the side of the top of the heating box 41 away from the third directional air inlet pipe 45.

[0035] In this embodiment, the gas enters the corresponding adsorption box 31 through a branch port of the first branch air inlet pipe 33, and the activated carbon plate 32 adsorbs the incoming gas, thereby adsorbing the organic matter. The adsorbed gas enters the heating box 41 through the corresponding second branch air inlet pipe 35, and the incoming exhaust gas is heated by the heating pipe 44. When one activated carbon plate 32 is adsorbed to a saturated state, the corresponding first solenoid valve 34 and second solenoid valve 36 are closed, and the other first solenoid valve 34 and second solenoid valve 36 are opened to perform alternating adsorption. Under the action of the catalyst, the exhaust gas is converted into carbon dioxide and water vapor, and the high temperature generated during this period increases the temperature inside the high-temperature chamber 42. Through the operation of the second fan 46, the high-temperature gas in the high-temperature chamber 42 enters the third branch air inlet pipe 45 and enters the adsorption box 31 in the activated carbon plate 32 in a saturated state, thereby desorbing the organic matter on the activated carbon plate 32. The desorbed organic matter enters the heating pipe 44 through the second branch air inlet pipe 35 again for catalytic combustion, thereby completely treating the exhaust gas.

[0036] like Figure 1 - Figure 8 As shown, the exhaust assembly includes a connecting air pipe 48, both ends of which are fixedly connected to the heating box 41 and the cooling box 51, a fixed cylinder 481 is fixedly connected to the side of the connecting air pipe 48 away from the heating box 41, and a push rod 483 is slidably connected to the end of the fixed cylinder 481 close to the heating box 41, and the push rod 483 passes through the fixed cylinder 481, and a spring 482 is fixedly connected to the end of the push rod 483 located inside the fixed cylinder 481, and the spring 482 is fixedly connected to the fixed cylinder 481, and the push rod 483 is away from the fixed cylinder 4 One end of 81 is fixedly connected to a piston 484, which is slidably connected to the connecting air pipe 48, the bottom end of the connecting air pipe 48 is fixedly connected to an exhaust pipe 485, the end of the exhaust pipe 485 away from the connecting air pipe 48 is fixedly connected to a cooling box 51, the top of the cooling box 51 is fixedly connected to a controller 52, the interior of the cooling box 51 is fixedly connected to staggered baffles 54 arranged equidistantly, the staggered baffles 54 are staggered up and down, the interior of the cooling box 51 is fixedly connected to a cooling pipe 53, and the cooling pipe 53 is fixedly connected to the staggered baffles 54.

[0037] In this embodiment, when the heating box 41 is burned for a long time, there are more water vapor and carbon dioxide inside, and the pressure generated pushes the piston 484. After being pressurized, the piston 484 slides to one side of the cooling box 51 and squeezes the push rod 483. The push rod 483 moves to push the spring 482, and the spring 482 is gradually compressed. The spring 482 will continue to pressurize the piston 484, so that the piston 484 is always in a pushed state, and the carbon dioxide and water vapor are discharged into the cooling box 51 through the exhaust pipe 485. Therefore, the continuous squeezing and sealing of the piston 484 effectively prevents the internal gas of the heating box 41 from being discharged, so that the gas burns more completely, and the staggered baffle 54 has a buffering effect on the incoming carbon dioxide and water vapor, and the cooling pipe 53 cools the carbon dioxide and water vapor, and discharges and collects the cooled water.

[0038] Working principle: First, the exhaust gas enters the gas separator 23 and is ejected through the tiny holes on the gas separator 23 to form tiny bubbles in the liquid. The tiny bubbles rise slowly, which helps the components in the gas to be adsorbed by the liquid. The motor 24 is started, and the motor 24 drives the rotating rod 25 to rotate. The rotating rod 25 drives the stirring blade 27 and the bubble dispersion plate 26 to work. The stirring blade 27 stirs the liquid, so that the tiny bubbles stay in the liquid for a longer time and are fully mixed. The bubble dispersion plate 26 reciprocates up and down through the reciprocating groove 251, so that the liquid and the small bubbles are squeezed, thereby increasing gas fusion. In addition, a number of tiny holes are provided on the bubble dispersion plate 26 to limit the rising speed of the gas and improve the adsorption effect. After rising, The gas enters the top of the blocking plate 212 through the gas buffer plate 2121, the rotating rod 25 rotates to drive the fixed rod 2112 to rotate, the fixed rod 2112 drives the supporting water ring 210 to rotate, and the supporting water ring 210 rotates to spray water mist through the atomizing nozzle 2111 to spray the exhaust gas, and then the gas enters the corresponding adsorption box 31 through a branch port of the first branch air inlet pipe 33, and the activated carbon plate 32 adsorbs the incoming gas, thereby adsorbing the organic matter. The adsorbed gas enters the heating box 41 through the corresponding second branch air inlet pipe 35, and the incoming exhaust gas is heated by the heating pipe 44. When an activated carbon plate 32 is adsorbed to a saturated state, the corresponding first solenoid valve 34 and the second solenoid valve are closed. The valve 36 opens another first solenoid valve 34 and a second solenoid valve 36 for alternate adsorption, and the exhaust gas is converted into carbon dioxide and water vapor under the action of the catalyst, and the high temperature generated during this period increases the temperature inside the high-temperature chamber 42, and the high-temperature gas in the high-temperature chamber 42 enters the third branch air inlet pipe 45 through the operation of the second fan 46, and enters the adsorption box 31 in the activated carbon plate 32 in a saturated state, thereby desorbing the organic matter on the activated carbon plate 32, and the desorbed organic matter enters the heating pipe 44 through the second branch air inlet pipe 35 again for catalytic combustion, thereby completely treating the exhaust gas, and when it burns for a long time in the heating box 41, the internal water vapor and carbon dioxide are There is a lot of carbon, and the pressure generated pushes the piston 484. After the piston 484 is under pressure, it slides to one side of the cooling box 51 and squeezes the push rod 483. The push rod 483 moves to push the spring 482, and the spring 482 is gradually compressed. The spring 482 will continue to pressurize the piston 484, so that the piston 484 is always in a pushed state, and the carbon dioxide and water vapor are discharged into the cooling box 51 through the exhaust pipe 485. Therefore, the continuous squeezing and sealing of the piston 484 effectively prevents the internal gas of the heating box 41 from being discharged, so that the gas burns more completely, and the staggered baffle 54 has a buffering effect on the incoming carbon dioxide and water vapor, and the cooling pipe 53 cools the carbon dioxide and water vapor, and discharges and collects the cooled water.

[0039] The above description is only a preferred embodiment of the present invention and does not limit the present invention in other forms. Any technician familiar with the profession may use the technical content disclosed above to change or modify it into an equivalent embodiment with equivalent changes and apply it to other fields. However, any simple modification, equivalent change and modification made to the above embodiment based on the technical essence of the present invention without departing from the content of the technical solution of the present invention still falls within the protection scope of the technical solution of the present invention.

Claims

1. A chemical reactor waste gas treatment device, comprising a base (1), characterized in that: A liquid adsorption component is arranged on one side of the top of the base (1), and the liquid adsorption component includes a spray adsorption treatment tank (21). A heating component is arranged on the top of the base (1) and located on one side of the spray adsorption treatment tank (21). The heating component includes a heating box (41). An activated carbon adsorption component is arranged on the top of the heating box (41). The activated carbon adsorption component includes an adsorption box (31). A plurality of adsorption boxes (31) are arranged and are stacked on the top of the heating box (41). The top of the base (1) is located on the heating box (41) away from the spray adsorption treatment tank (21). ) is provided with a cooling assembly on one side, the cooling assembly comprising a cooling box (51), the spray adsorption treatment tank (21), the heating box (41) and the cooling box (51) are all fixedly connected to the base (1), a first air inlet pipe (22) is fixedly connected to the middle of the bottom end of the spray adsorption treatment tank (21), the first air inlet pipe (22) passes through the spray adsorption treatment tank (21), one end of the first air inlet pipe (22) located inside the spray adsorption treatment tank (21) is fixedly connected to an air separation plate (23), and the air separation plate (23) is fixedly connected to the spray adsorption treatment tank (21).

2. A chemical reactor waste gas treatment device according to claim 1, characterized in that: A motor (24) is fixedly connected to the middle of the top of the spray adsorption treatment tank (21), and a rotating rod (25) is drivingly connected to the bottom of the motor (24). The rotating rod (25) penetrates the spray adsorption treatment tank (21) and is rotatably connected to the spray adsorption treatment tank (21). Reciprocating grooves (251) are arranged equidistantly at the bottom of the rotating rod (25). The rotating rod (25) is threadedly connected to a bubble dispersion plate (26) through the reciprocating grooves (251). The bubble dispersion plate (26) is fixedly connected to limiting sliders (261) on both radial sides. A stirring blade (27) is fixedly connected to the rotating rod (25) on the side opposite to the bubble dispersion plate (26). Limiting slide grooves (213) are provided on both sides of the interior of the spray adsorption treatment tank (21), and the limiting slide grooves (213) are slidably connected to the limiting slider (261).

3. A chemical reactor waste gas treatment device according to claim 2, characterized in that: The top annular array of the rotating rod (25) located inside the spray adsorption treatment tank (21) is fixedly connected to a fixed rod (2112); one end of the fixed rod (2112) away from the rotating rod (25) is fixedly connected to a rotating water ring (211); the inner annular array of the rotating water ring (211) is fixedly connected to an atomizing nozzle (2111); the top of the rotating water ring (211) is rotatably connected to a supporting water ring (210); and the top of one side of the supporting water ring (210) is fixedly connected to the spray adsorption treatment tank (21).

4. A chemical reactor waste gas treatment device according to claim 3, characterized in that: A first circulation pipe (28) is fixedly connected to the top end of one side of the supporting water ring (210); both ends of the first circulation pipe (28) penetrate the spray adsorption treatment tank (21) and are fixedly connected to the spray adsorption treatment tank (21); the first circulation pipe (28) is located at the top end of the spray adsorption treatment tank (21) and is fixedly connected to a water pump (29); the rotating rod (25) is located at the bottom end of the rotating water ring (211) and is fixedly connected to a blocking plate (212); gas buffer plates (2121) are provided on both sides of the blocking plate (212).

5. The chemical reactor waste gas treatment device according to claim 1, characterized in that: An activated carbon plate (32) is arranged inside the adsorption box (31), a first directional air intake pipe (33) is fixedly connected to one radial side of the adsorption box (31), an end of the first directional air intake pipe (33) away from the adsorption box (31) is fixedly connected to the top of the spray adsorption treatment tank (21), and two ports of the first directional air intake pipe (33) close to the adsorption box (31) are both provided with a first solenoid valve (34).

6. A chemical reactor waste gas treatment device according to claim 5, characterized in that: A second directional air intake pipe (35) is fixedly connected to a side of the adsorption box (31) away from the first directional air intake pipe (33); an end of the second directional air intake pipe (35) away from the adsorption box (31) is fixedly connected to a heating box (41); two ports of the second directional air intake pipe (35) close to the adsorption box (31) are both provided with a second solenoid valve (36); and an end of the second directional air intake pipe (35) close to the heating box (41) is fixedly connected to a first fan (37).

7. A chemical reactor waste gas treatment device according to claim 1, characterized in that: A heating tube (44) is fixedly connected to the interior of the heating box (41), a high-temperature chamber (42) is provided in the wall of the heating box (41), a heat sink (43) is fixedly connected to the central annular array of the heating box (41) located inside the high-temperature chamber (42), a third branch air intake pipe (45) is fixedly connected to one side of the heating box (41), and the top end of the third branch air intake pipe (45) is fixedly connected to the adsorption box (31).

8. A chemical reactor waste gas treatment device according to claim 7, characterized in that: The two ports at the top end of the third branch air inlet pipe (45) are both fixedly connected to a third solenoid valve (47), the bottom end of the third branch air inlet pipe (45) is fixedly connected to a second fan (46), and an exhaust assembly is provided on the side of the top end of the heating box (41) away from the third branch air inlet pipe (45).

9. A chemical reactor waste gas treatment device according to claim 8, characterized in that: The exhaust assembly comprises a connecting air pipe (48), both ends of which are fixedly connected to the heating box (41) and the cooling box (51), a fixed cylinder (481) is fixedly connected to the side of the connecting air pipe (48) away from the heating box (41), and a push rod (483) is slidably connected to the end of the fixing cylinder (481) close to the heating box (41), the push rod (483) passes through the fixing cylinder (481), and the push rod (483) is located in the fixing cylinder (481). 1) A spring (482) is fixedly connected to one end of the interior, and the spring (482) is fixedly connected to the fixed cylinder (481); an end of the push rod (483) away from the fixed cylinder (481) is fixedly connected to a piston (484); the piston (484) is slidably connected to the connecting air pipe (48); an exhaust pipe (485) is fixedly connected to the bottom end of the connecting air pipe (48); and an end of the exhaust pipe (485) away from the connecting air pipe (48) is fixedly connected to the cooling box (51).

10. The chemical reactor waste gas treatment device according to claim 1, characterized in that: The top of the cooling box (51) is fixedly connected to a controller (52), the interior of the cooling box (51) is equidistantly arranged and fixedly connected to staggered baffles (54), the staggered baffles (54) are staggered up and down, the interior of the cooling box (51) is fixedly connected to a cooling pipe (53), and the cooling pipe (53) is fixedly connected to the staggered baffles (54).

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