A gas recovery and purification device for the production experiment of ethoxy pentafluorocyclotriphosphazene

By designing the liquid piston-driven filler shaking mechanism in the gas recovery and purification device, the problems of degradation of purification efficiency and equipment instability caused by fixed filler are solved, and more efficient gas purification and long-term stable operation of the equipment are achieved.

CN119857367BActive Publication Date: 2025-06-27LONGYAN UNIV
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Patent Information

Application Number
CN202510357532.9
Authority / Receiving Office
CN · China
Patent Type
Patents(China)
Current Assignee / Owner
Filing Date
2025-03-25
Publication Date
2025-06-27
Estimated Expiration
2045-03-25

AI Technical Summary

Technical Problem

In the existing gas recovery and purification device, after a long time of use, the fixed filler may easily reduce the gas-liquid contact area due to the coverage of pollutants and sediments, reduce the purification efficiency, and may form a local airflow dead zone, affecting the stability of the equipment.

Method used

A gas recovery and purification device for the production of ethoxy pentafluorocyclic triphosphazene was designed. The back and forth displacement of the liquid piston drove the movement of the curved push rod and the top rod, causing the filling material in the bottom mesh plate, closed ring and top mesh plate to shake, increasing the contact area between the gas and the purified liquid.

Benefits of technology

By shaking the filler, the contact area between the gas and the purified liquid is increased, the gas absorption and purification efficiency is improved, the filling material agglomeration and dead zone formation is avoided, and the long-term stability and efficient operation of the equipment are ensured.

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Abstract

The present invention relates to the technical field of gas recovery and purification, and discloses a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments, including: a support frame and a purification tank arranged on the support frame, and a recovery box is fixed above the support frame; it also includes: a power ring fixed inside the purification tank; a closing block fixed inside the power ring for dividing the internal area of the power ring; a liquid piston sliding inside the power ring; a spring socket fixed inside the power ring; in the present invention, the reciprocating displacement of the liquid piston drives the displacement of the curved push rod and the top rod, and the top rod drives the bottom net plate, the closing ring and the top net plate to shake back and forth. The filling material in the bottom net plate, the closing ring and the top net plate can be turned over by the shaking of the filling material, which can increase the contact area between the gas and the purification liquid, thereby improving the absorption and purification efficiency of the gas; when the filling material remains stationary for a long time, caking or accumulation will occur, thus affecting the uniform flow of the fluid.
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Description

Technical Field

[0001] The present invention relates to the technical field of gas recovery and purification, and particularly relates to a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments. Background Art

[0002] Existing gas recovery and purification devices achieve gas purification through multiple contacts and interactions between the gas, the purification liquid, and the packing material; the gas to be purified enters the tower body through the air inlet, and during the upward flow of the gas in the tower, it will come into contact with the purification liquid sprayed from top to bottom; the purification liquid is evenly distributed in the tower through the spraying system to form fine liquid droplets, increasing the contact area between the liquid and the gas, and purifying the gas.

[0003] In the field of gas recovery and purification, packing materials are often used to enhance the contact area between the gas and the purification liquid and improve the removal efficiency of pollutants. The role of the packing material is to provide a porous structure for gas flow to increase the surface of gas-liquid contact, thereby improving the adsorption, dissolution, and reaction efficiency of pollutants in the gas. However, in the prior art, the packing material has a fixed design, and this structure gradually exposes the problem of decreased efficiency during use. With the long-term use of the packing material, its surface is easily covered by pollutants, sediments, or scaling substances, resulting in a gradual reduction in the gas-liquid contact area. The gas flow is no longer uniform, the contact effect between the purification liquid and the pollutants decreases, and thus the gas purification efficiency is significantly reduced.

[0004] During the long-term use of the fixed packing material, local gas flow dead zones may also be formed due to uneven gas flow velocity, further exacerbating the decline in purification efficiency. The surface of the fixed packing material is easily blocked or wrapped by certain pollutants, which will affect its original adsorption performance and catalytic effect, making the device unable to maintain a stable purification effect. Therefore, a new technical solution is needed to overcome the deficiencies of the existing fixed structure of the packing material to improve the overall efficiency and long-term stability of the gas purification device. Summary of the Invention

[0005] The present invention provides a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments. The liquid piston squeezes the return coil spring, the displacement of the liquid piston drives the displacement of the curved push rod, the displacement of the curved push rod drives the ejector rod to move along the stroke curved groove, and the movement of the ejector rod drives the bottom mesh plate, the sealing ring, and the top mesh plate to move back and forth, so that the packing material inside the bottom mesh plate, the sealing ring, and the top mesh plate can shake.

[0006] To solve the above technical problems, the technical solution of the present invention is as follows:

[0007] In a first aspect, a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments includes: a support frame and a purification tank arranged on the support frame, and a recovery box is fixed above the support frame; it further includes:

[0008] The power ring is fixed inside the purification tank; the sealing block is fixed inside the power ring and is used to divide the internal area of the power ring; the liquid piston slides inside the power ring; the spring sleeve seat is fixed inside the power ring; the curved push rod has one end fixed on the liquid piston and the other end sliding through the spring sleeve seat; the return curved spring is sleeved on the curved push rod, with one end fixed on the liquid piston and the other end fixed on the spring sleeve seat, and is used to reset the liquid piston; the ejector rod is fixed below the end of the curved push rod away from the liquid piston and is used to connect the filler layer and drive the filler layer, gas and purification liquid to perform dynamic contact and adsorption movement.

[0009] The liquid supply assembly is fixed below the purification tank; the filling assembly rotates inside the purification tank; the gas-liquid separation assembly is fixed inside the purification tank.

[0010] The rotating air pipe has one end fixed above the purification tank and the other end extending into the recovery box; the activated carbon assembly is fixed inside the recovery box and is used to remove harmful substances in the gas.

[0011] The blower is fixed below the purification tank; the first air inlet pipe is fixed on the blower; the second air inlet pipe has one end fixed on the blower and the other end fixed below the purification tank.

[0012] The controller is fixed on the support frame.

[0013] Furthermore, it also includes:

[0014] The liquid inlet ring pipe is located inside the filling tank; the ring inlet pipe has one end extending out of the filling tank and the other end fixed on the liquid inlet ring pipe; the liquid outlet ring pipe is located inside the filling tank; the ring outlet pipe has one end extending out of the filling tank and the other end fixed on the liquid outlet ring pipe; the opening and closing inlet pipe has one end fixed on the power ring and the other end fixed on the liquid inlet ring pipe; the opening and closing outlet pipe has one end fixed on the power ring and the other end fixed on the liquid outlet ring pipe; the opening and closing valve body is fixed on the opening and closing inlet pipe and the opening and closing outlet pipe; the opening and closing valve core slides inside the opening and closing valve body and is used to move up and down in the opening and closing valve body to switch the flow channel. The opening and closing valve body is provided with a liquid channel and an installation hole.

[0015] Furthermore, it also includes:

[0016] The first hydraulic sleeve ring is fixed inside the power ring; the first hydraulic push ring is slidably arranged inside the first hydraulic sleeve ring and is located inside the power ring; the first hydraulic telescopic rod has its fixed end fixed inside the opening and closing valve body and its telescopic end fixed inside the installation hole; the first hydraulic pipe has one end fixed on the first hydraulic sleeve ring and the other end fixed on the first hydraulic telescopic rod.

[0017] A second hydraulic collar, fixed inside the power ring; a second hydraulic push ring, slidably disposed inside the second hydraulic collar and located inside the power ring; a second hydraulic telescopic rod, with the fixed end fixed inside the opening and closing valve body and the telescopic end fixed inside the mounting hole; a second hydraulic pipe, with one end fixed on the second hydraulic collar and the other end fixed on the second hydraulic telescopic rod;

[0018] A stroke cam groove, opened above the power ring and sleeved above the cam push rod.

[0019] Furthermore, the liquid supply assembly includes:

[0020] A circulation pump, fixed on the bottom liquid tank; a liquid suction pipe, with one end fixed on the circulation pump and the other end extending into the bottom liquid tank; a filter element pipe, fixed below the liquid suction pipe above and located inside the bottom liquid tank; a liquid supply pipe, with one end fixed on the circulation pump and the other end extending into the filling tank.

[0021] Furthermore, the liquid supply assembly further includes:

[0022] A first branch pipe, with one end fixed on the liquid supply pipe and the other end fixed on the ring inlet pipe; a second branch pipe, with one end fixed on the liquid supply pipe and the other end extending into the filling tank; an electromagnetic valve, fixed on the first branch pipe and the second branch pipe and located outside the filling tank, for controlling the opening and closing of the two branch pipes; a spraying ring, located inside the filling tank, with one side fixed on the second branch pipe and the other side fixed on the ring outlet pipe; spraying nozzles, fixed on the spraying ring.

[0023] Furthermore, the purification tank includes a bottom liquid tank, a filling tank and a gas-liquid tank;

[0024] The bottom liquid tank is fixed below on the support frame, there are three filling tanks, the three filling tanks are arranged from bottom to top, the bottom liquid tank is fixed above below the filling tanks, and the gas-liquid tank is fixed below above the filling tanks.

[0025] Furthermore, an inlet pipe is fixed above the bottom liquid tank, a conical cylinder is fixed below the bottom liquid tank, a drain pipe is fixed below the conical cylinder, an electric switch valve is fixed on the drain pipe, and a limiting plate is fixed inside the bottom liquid tank.

[0026] Furthermore, the filling assembly includes:

[0027] A bottom net plate, fixed below above the cam push rod and located inside the filling tank; a sealing ring, fixed below above the bottom net plate and located inside the filling tank; a top net plate, fixed below above the sealing ring and located inside the filling tank. The bottom net plate, the sealing ring and the top net plate together form a filling material area.

[0028] Furthermore, the gas-liquid separation assembly includes:

[0029] The gas-liquid ring is fixed inside the gas-liquid tank; the lower folding plate is fixed inside the gas-liquid ring; the upper folding plate is fixed inside the gas-liquid ring and is located above the lower folding plate; the inclined surfaces of the lower folding plate and the upper folding plate are used to intercept small liquid droplets in the gas.

[0030] Furthermore, the activated carbon assembly includes:

[0031] The purification sleeve box is located inside the recovery box; the air vents are opened on both sides of the purification sleeve box; the fixing plate is fixed inside the recovery box and is fixed to the purification sleeve box below; the activated carbon box slides inside the purification sleeve box; the air-permeable net tube is fixed inside the activated carbon box; the activated carbon net plates are fixed on both sides of the activated carbon box; the closing plate is fixed to the activated carbon box; the handle is fixed to the closing plate; the recovery gas pipe is fixed below the recovery box.

[0032] The above scheme of the present invention has at least the following beneficial effects:

[0033] In the present invention, the liquid piston moves back and forth, driving the displacement of the curved push rod and the ejector rod. The ejector rod drives the bottom net plate, the closing ring and the top net plate to shake. The filling materials inside the bottom net plate, the closing ring and the top net plate can be turned over by the shaking of the filling materials, which can increase the contact area between the gas and the purification liquid, thereby improving the absorption and purification efficiency of the gas; when the filling materials remain stationary for a long time, caking or accumulation will occur, which will affect the uniform flow of the fluid and reduce the dead zone, that is, the area where the fluid flow is blocked, ensuring a more uniform flow of the gas and the liquid; the turned-over filling materials can help maintain the stability of the liquid film, making the coverage of the liquid film more uniform, thereby improving the adsorption and chemical reaction efficiency; for the purification process relying on chemical reactions, the shaking filling materials can make the contact between the reactants and the catalyst in the purification liquid more sufficient, improving the reaction rate and effect. Description of the Drawings

[0034] Figure 1 It is a schematic perspective view of the overall structure of a gas recovery and purification device for the production experiment of ethoxy pentafluorocyclotriphosphazene provided by an embodiment of the present invention from the first perspective;

[0035] Figure 2 It is a schematic perspective view of the overall structure of a gas recovery and purification device for the production experiment of ethoxy pentafluorocyclotriphosphazene provided by an embodiment of the present invention from the second perspective;

[0036] Figure 3 It is a schematic perspective view of the drain pipe of a gas recovery and purification device for the production experiment of ethoxy pentafluorocyclotriphosphazene provided by an embodiment of the present invention;

[0037] Figure 4 It is for a gas recovery and purification device for the production experiment of ethoxy pentafluorocyclotriphosphazene provided by an embodiment of the present invention Figure 3 Enlarged view of part A;

[0038] Figure 5 A magnified view at B of a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments provided by an embodiment of the present invention Figure 3 ;

[0039] Figure 6 A three-dimensional structure schematic diagram of a second branch pipe of a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments provided by an embodiment of the present invention

[0040] Figure 7 A magnified view at C of a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments provided by an embodiment of the present invention Figure 6 ;

[0041] Figure 8 A magnified view at D of a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments provided by an embodiment of the present invention Figure 7 ;

[0042] Figure 9 A magnified view at E of a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments provided by an embodiment of the present invention Figure 7 ;

[0043] Figure 10 A magnified view at F of a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments provided by an embodiment of the present invention Figure 7 ;

[0044] Figure 11 A magnified view at G of a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments provided by an embodiment of the present invention Figure 6 ;

[0045] Figure 12 A cross-sectional view of a recovery box of a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments provided by an embodiment of the present invention

[0046] Explanation of reference numerals:

[0047] In the figure: 1, support frame; 2, purification tank; 201, bottom liquid tank; 202, filling tank; 203, gas-liquid tank; 204, liquid inlet pipe; 205, conical cylinder; 206, liquid discharge pipe; 207, electric switch valve; 208, limit plate; 3, recycling box; 4, liquid power assembly; 401, power ring; 402, closing block; 403, liquid piston; 404, spring socket; 405, curved push rod; 406, reset curved spring; 407, ejector rod; 408, liquid inlet ring pipe; 409, ring inlet pipe; 4010, liquid outlet ring pipe; 4011, ring outlet pipe; 4012, opening and closing inlet pipe; 4013, opening and closing outlet pipe; 4014, opening and closing valve body; 4015, opening and closing valve core; 4016, liquid channel; 4017, mounting hole; 4018, first hydraulic sleeve ring; 4019, first hydraulic push ring; 4020, first hydraulic telescopic rod; 4021, first hydraulic pipe; 4022, second hydraulic sleeve ring; 4023, second hydraulic push ring; 4024, second hydraulic telescopic rod; 4025, second hydraulic pipe; 4026, stroke curved groove; 5, liquid supply assembly; 501, circulation pump; 502, liquid suction pipe; 503, filter element pipe; 504, liquid supply pipe; 505, first branch pipe; 506, second branch pipe; 507, solenoid valve; 508, spraying ring; 509, spraying head; 6, filling assembly; 601, bottom net plate; 602, closing ring; 603, top net plate; 7, gas-liquid separation assembly; 701, gas-liquid ring; 702, lower folding plate; 703, upper folding plate; 8, rotating gas pipe; 9, activated carbon assembly; 901, purification sleeve box; 902, air vent; 903, fixing plate; 904, activated carbon box; 905, air permeable net pipe; 906, activated carbon net plate; 907, closing plate; 908, handle; 909, recycling gas pipe; 10, blower; 11, first air inlet pipe; 12, second air inlet pipe; 13, controller. Specific embodiments

[0048] The exemplary embodiments of the present invention will be described in more detail below with reference to the accompanying drawings. Although the exemplary embodiments of the present invention are shown in the drawings, it should be understood that the present invention can be implemented in various forms and should not be limited by the embodiments described herein. On the contrary, these embodiments are provided to enable a more thorough understanding of the present invention and to fully convey the scope of the present invention to those skilled in the art.

[0049] As Figures 1 to 12 shown, an embodiment of the present invention provides a gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiments, including: a support frame 1 and a purification tank 2 provided on the support frame 1, and a recycling box 3 is fixed above the support frame 1; further including:

[0050] The power ring 401 is fixed inside the purification tank 2; the closing block 402 is fixed inside the power ring 401 and is used to divide the internal area of the power ring 401; the liquid piston 403 slides inside the power ring 401; the spring sleeve seat 404 is fixed inside the power ring 401; one end of the curved push rod 405 is fixed on the liquid piston 403, and the other end slides through the spring sleeve seat 404; the reset curved spring 406 is sleeved on the curved push rod 405, one end is fixed on the liquid piston 403, and the other end is fixed on the spring sleeve seat 404, and is used to reset the liquid piston 403; the blanking rod 407 is fixed below the end of the curved push rod 405 away from the liquid piston 403, and is used to connect the filler layer and drive the filler layer, gas and purification liquid to perform dynamic contact and adsorption movement;

[0051] The liquid supply assembly 5 is fixed below the purification tank 2; the filling assembly 6 rotates inside the purification tank 2; the gas-liquid separation assembly 7 is fixed inside the purification tank 2;

[0052] The rotating air pipe 8 has one end fixed above the purification tank 2 and the other end extending into the recovery tank 3; the activated carbon assembly 9 is fixed inside the recovery tank 3 and is used to remove harmful substances in the gas;

[0053] The blower 10 is fixed below the purification tank 2; the first air inlet pipe 11 is fixed on the blower 10; the second air inlet pipe 12 has one end fixed on the blower 10 and the other end fixed below the purification tank 2;

[0054] The controller 13 is fixed on the support frame 1.

[0055] The purification tank 2 includes a liquid bottom tank 201, a filling tank 202 and a gas-liquid tank 203; the liquid bottom tank 201 is fixed below on the support frame 1, there are three filling tanks 202, the three filling tanks 202 are arranged from bottom to top, the liquid bottom tank 201 is fixed above below the filling tank 202, and the gas-liquid tank 203 is fixed below above the filling tank 202.

[0056] An inlet liquid pipe 204 is fixed above the liquid bottom tank 201, a conical cylinder 205 is fixed below the liquid bottom tank 201, a drain pipe 206 is fixed below the conical cylinder 205, an electric switch valve 207 is fixed on the drain pipe 206, and a limiting plate 208 is fixed inside the liquid bottom tank 201.

[0057] Specifically, four sets of hydrodynamic components 4 are provided in the same filling tank 202, and the four sets of hydrodynamic components 4 are evenly distributed in the filling tank 202; the filling component 6 can be filled with plastic fillers, metal fillers, ceramic fillers, fiber fillers, etc. The function of the filler in the filling component 6 is to increase the contact area between gas and liquid. By providing a large surface area, pollutants in the gas can interact with it, reducing the consumption of washing liquid and treatment costs, and at the same time reducing energy consumption, because a good filler design can ensure the optimization of gas-liquid contact and improve the overall treatment effect; the liquid for purification is water, acidic solution, alkaline solution, organic solvent, hydrogen peroxide solution, biological filter solution, brine solution, etc. The liquid can fully contact and react or adsorb to improve the gas purification efficiency with the available purified liquid; the liquid bottom tank 201, the filling tank 202 and the gas-liquid tank 203 are butt-jointed by flanges, and a sealing rubber ring is provided at the flange butt-joint; the activated carbon component 9 is filled with activated carbon; a humidity sensor is provided in the rotating air pipe 8 to detect the moisture content of the gas; the controller 13 is used to control the electrical equipment of the device.

[0058] In the actual application process of this embodiment: one end of the first air inlet pipe 11 away from the blower 10 is used to connect the gas to be purified. Through the extraction of the blower 10, it is supplied to the second air inlet pipe 12 and then into the liquid bottom tank 201. The gas passes through the purification of the three filling tanks 202 from bottom to top and then into the gas-liquid tank 203 to separate gas and small liquid droplets; the gas flows from the rotating air pipe 8 to the recovery box 3 and then into the activated carbon component 9. The gas is secondarily purified by the activated carbon, and the purified gas flows out of the recovery box 3 through the recovery air pipe 909; the recovery air pipe 909 is butt-jointed to the storage gas recovery equipment.

[0059] The conical cylinder 205 is used to precipitate impurities in the liquid. The impurities can be discharged by opening the electric switch valve 207 and opening the drain pipe 206; the limiting plate 208 is used to intercept the precipitated impurities, and the liquid inlet pipe 204 is used to switch the purification liquid.

[0060] As a preferred embodiment of the present invention, the hydrodynamic component 4 further includes:

[0061] The liquid inlet ring pipe 408 is located inside the filling tank 202; the ring inlet pipe 409 has one end extending out of the filling tank 202 and the other end fixed to the liquid inlet ring pipe 408; the liquid outlet ring pipe 4010 is located inside the filling tank 202; the ring outlet pipe 4011 has one end extending out of the filling tank 202 and the other end fixed to the liquid outlet ring pipe 4010; the opening and closing inlet pipe 4012 has one end fixed to the power ring 401 and the other end fixed to the liquid inlet ring pipe 408; the opening and closing outlet pipe 4013 has one end fixed to the power ring 401 and the other end fixed to the liquid outlet ring pipe 4010; the opening and closing valve body 4014 is fixed to the opening and closing inlet pipe 4012 and the opening and closing outlet pipe 4013; the opening and closing valve core 4015 slides inside the opening and closing valve body 4014 and is used to move up and down in the opening and closing valve body 4014 to switch the flow passage. The opening and closing valve body 4014 is provided with a liquid passage 4016 and an installation hole 4017.

[0062] The liquid power assembly 4 further includes:

[0063] The first hydraulic sleeve ring 4018 is fixed inside the power ring 401; the first hydraulic push ring 4019 is slidably arranged inside the first hydraulic sleeve ring 4018 and is located inside the power ring 401; the first hydraulic telescopic rod 4020 has a fixed end fixed inside the opening and closing valve body 4014 and a telescopic end fixed inside the installation hole 4017; the first hydraulic pipe 4021 has one end fixed to the first hydraulic sleeve ring 4018 and the other end fixed to the first hydraulic telescopic rod 4020;

[0064] The second hydraulic sleeve ring 4022 is fixed inside the power ring 401; the second hydraulic push ring 4023 is slidably arranged inside the second hydraulic sleeve ring 4022 and is located inside the power ring 401; the second hydraulic telescopic rod 4024 has a fixed end fixed inside the opening and closing valve body 4014 and a telescopic end fixed inside the installation hole 4017; the second hydraulic pipe 4025 has one end fixed to the second hydraulic sleeve ring 4022 and the other end fixed to the second hydraulic telescopic rod 4024;

[0065] The stroke cam groove 4026 is opened above the power ring 401 and is sleeved above the curved push rod 405.

[0066] Furthermore, the liquid supply assembly 5 includes:

[0067] The circulation pump 501 is fixed on the liquid bottom tank 201; the liquid suction pipe 502 has one end fixed to the circulation pump 501 and the other end extending into the liquid bottom tank 201; the filter element pipe 503 is fixed below the liquid suction pipe 502 at the upper part and is located inside the liquid bottom tank 201; the liquid supply pipe 504 has one end fixed to the circulation pump 501 and the other end extending into the filling tank 202.

[0068] The liquid supply assembly 5 further includes:

[0069] The first branch pipe 505 has one end fixed to the liquid supply pipe 504 and the other end fixed to the annular inlet pipe 409; the second branch pipe 506 has one end fixed to the liquid supply pipe 504 and the other end extending into the filling tank 202; the solenoid valve 507 is fixed to the first branch pipe 505 and the second branch pipe 506 and is located outside the filling tank 202 for controlling the opening and closing of the two branch pipes; the spraying ring 508 is located in the filling tank 202, with one side fixed to the second branch pipe 506 and the other side fixed to the annular outlet pipe 4011; the spray head 509 is fixed to the spraying ring 508.

[0070] Furthermore, the filling assembly 6 includes:

[0071] The bottom net plate 601 is fixed below the curved push rod 405 and is located inside the filling tank 202; the sealing ring 602 is fixed below the bottom net plate 601 and is located inside the filling tank 202; the top net plate 603 is fixed below the sealing ring 602 and is located inside the filling tank 202. The bottom net plate 601, the sealing ring 602 and the top net plate 603 together form a filling material area.

[0072] Specifically, the first hydraulic collar 4018 and the first hydraulic push ring 4019 are arranged opposite to the second hydraulic collar 4022 and the second hydraulic push ring 4023 on both sides of the liquid piston 403. The switching of the flow through the opening and closing valve body 4014 and the opening and closing valve core 4015 is controlled by the position of the liquid piston 403. The spray head 509 is used for spraying the purification liquid; the filter element pipe 503 is used for further filtering the essence liquid; the bottom net plate 601, the sealing ring 602 and the top net plate 603 form an area for filling materials, and the solenoid valve 507 is used for controlling the opening of the first branch pipe 505 and the second branch pipe 506.

[0073] In the actual application process of this embodiment, the solenoid valve 507 is used to control the opening of the first branch pipe 505. The purification liquid pushes the displacement of the liquid piston 403 to squeeze the hydraulic oil in the first hydraulic collar 4018 and the first hydraulic push ring 4019 or the second hydraulic collar 4022 and the second hydraulic push ring 4023. The opening of the opening and closing valve body 4014 and the opening and closing valve core 4015 is switched by the flowing hydraulic oil; the circulation pump 501 extracts the purification liquid to the liquid supply pipe 504 through the liquid suction pipe 502 and the filter element pipe 503. The liquid supply pipe 504 then distributes it to the first branch pipe 505 and the second branch pipe 506, and then enters the power ring 401 through the inlet ring pipe 408, the annular inlet pipe 409 and the opening and closing inlet pipe 4012. The purification liquid flows to the spraying ring 508 and the spray head 509 through the outlet ring pipe 4010, the annular outlet pipe 4011 and the opening and closing outlet pipe 4013. The purification liquid sprayed by the spray head 509 is sprayed on the filling materials. The gas fully contacts the purification liquid and the filling materials, and a reaction occurs between the gas and the purification liquid. The impurities in the gas are adsorbed on the filling materials for purifying the gas.

[0074] As a preferred embodiment of the present invention, the gas-liquid separation component 7 includes:

[0075] A gas-liquid ring 701, fixed inside the gas-liquid tank 203; a lower folding plate 702, fixed inside the gas-liquid ring 701; an upper folding plate 703, fixed inside the gas-liquid ring 701 and located above the lower folding plate 702; the inclined surfaces of the lower folding plate 702 and the upper folding plate 703 are used to intercept small liquid droplets in the gas.

[0076] Specifically, when the spraying head 509 sprays out the purification liquid, tiny liquid droplets will disperse. The flow of the gas will carry the liquid droplets upward, and the small liquid droplets are intercepted by the lower folding plate 702 and the upper folding plate 703.

[0077] As a preferred embodiment of the present invention, the activated carbon component 9 includes:

[0078] A purification sleeve box 901, located inside the recovery box 3; air vents 902, opened on both sides of the purification sleeve box 901; a fixing plate 903, fixed inside the recovery box 3 and fixed to the purification sleeve box 901 below; an activated carbon box 904, sliding inside the purification sleeve box 901; an air-permeable net tube 905, fixed inside the activated carbon box 904; activated carbon net plates 906, fixed on both sides of the activated carbon box 904; a closing plate 907, fixed on the activated carbon box 904; a handle 908, fixed on the closing plate 907; a recovery air pipe 909, fixed below the recovery box 3.

[0079] Specifically, activated carbon particles are placed inside the activated carbon box 904. The closing plate 907 is fixed to the activated carbon box 904 by bolts. The closing plate 907 is detachable, which is convenient for replacing the activated carbon particles to ensure the effective purification of the gas; there is a sealing rubber ring at the edge between the activated carbon box 904 and the purification sleeve box 901 for sealing.

[0080] In the actual application process of this embodiment: the lower folding plate 702 and the upper folding plate 703 intercept small liquid droplets, avoiding that after the small liquid droplets enter the activated carbon, they may hinder the contact between the gas and the surface of the activated carbon, reducing the gas adsorption efficiency of the activated carbon; the small liquid droplets cover or fill the pores of the activated carbon, reducing the surface area available for gas adsorption of the activated carbon, interfering with the gas adsorption process, reducing the efficiency of the activated carbon or changing the adsorption mechanism.

[0081] Working principle: Start the blower 10. The blower 10 extracts the gas to be purified through the first air inlet pipe 11 and enters the second air inlet pipe 12 and the liquid bottom tank 201. After the gas to be purified is purified by the purification liquid and the filler three times, it flows through the transfer air pipe 8 to the recovery box 3.

[0082] Start the circulation pump 501. The circulation pump 501 extracts the purified liquid in the liquid bottom tank 201 through the liquid suction pipe 502 and the filter element pipe 503. The purified liquid flows into the liquid supply pipe 504. The solenoid valve 507 on the first branch pipe 505 is opened, and the solenoid valve 507 on the second branch pipe 506 is closed. The purified liquid in the first branch pipe 505 flows into the annular inlet pipe 409 and the liquid inlet annular pipe 408. The purified liquid then flows through the liquid inlet annular pipe 408 into the opening and closing inlet pipe 4012. At this time, the opening and closing valve body 4014 and the opening and closing valve core 4015 are in the open state, and then enters the power ring 401 through the opening and closing inlet pipe 4012. The purified liquid accumulates in the power ring 401 and pushes open the liquid piston 403.

[0083] The liquid piston 403 squeezes the return curved spring 406. The displacement of the liquid piston 403 drives the displacement of the curved push rod 405. The displacement of the curved push rod 405 drives the ejector rod 407 to move along the stroke curved groove 4026. The movement of the ejector rod 407 drives the movement of the bottom mesh plate 601, the sealing ring 602 and the top mesh plate 603 until the liquid piston 403 pushes the second hydraulic push ring 4023 into the second hydraulic sleeve ring 4022. The second hydraulic push ring 4023 squeezes the hydraulic oil in the second hydraulic sleeve ring 4022 and enters the second hydraulic telescopic rod 4024 through the second hydraulic pipe 4025. The elongation of the second hydraulic telescopic rod 4024 drives the opening and closing valve core 4015 to switch the position of the liquid channel 4016 in the opening and closing valve body 4014. At this time, the opening and closing outlet pipe 4013 is communicated with the liquid channel 4016. The return curved spring 406 drives the liquid piston 403 to reset. The liquid piston 403 squeezes the purified liquid in the power ring 401, and the purified liquid flows into the opening and closing outlet pipe 4013, the liquid outlet annular pipe 4010 and the annular outlet pipe 4011. The purified liquid enters the spraying ring 508 and the spray head 509 through the annular outlet pipe 4011, and the purified liquid is sprayed onto the filling material in the bottom mesh plate 601, the sealing ring 602 and the top mesh plate 603 through the spray head 509.

[0084] When the liquid piston 403 of the return curved spring 406 resets, it pushes the first hydraulic push ring 4019 into the first hydraulic sleeve ring 4018. The hydraulic oil in the first hydraulic sleeve ring 4018 enters the first hydraulic telescopic rod 4020 through the first hydraulic pipe 4021. The elongation of the first hydraulic telescopic rod 4020 drives the displacement of the opening and closing valve core 4015 to switch the liquid channel 4016. At this time, the opening and closing inlet pipe 4012 is communicated with the liquid channel 4016. The displacement of the opening and closing valve core 4015 at this time squeezes the retraction of the second hydraulic telescopic rod 4024. The hydraulic oil in the second hydraulic telescopic rod 4024 enters the second hydraulic sleeve ring 4022 through the second hydraulic pipe 4025, and the hydraulic oil pushes out the second hydraulic push ring 4023, and the second hydraulic push ring 4023 resets.

[0085] When the liquid piston 403 resets, it drives the movement of the curved push rod 405 and the ejector rod 407. The ejector rod 407 drives the reset movement of the bottom mesh plate 601, the sealing ring 602 and the top mesh plate 603, so that the bottom mesh plate 601, the sealing ring 602 and the top mesh plate 603 can swing back and forth. When swinging, it drives the filler inside the bottom mesh plate 601, the sealing ring 602 and the top mesh plate 603 to swing, achieving the following effects:

[0086] Effect 1: The swinging of the filler can turn over the filler, which can increase the contact area between the gas and the purification liquid, thereby improving the absorption and purification efficiency of the gas; the larger the surface area of the gas-liquid contact, the higher the removal efficiency of pollutants;

[0087] Effect 2: When the filler remains stationary for a long time, caking or accumulation will occur, which will affect the uniform flow of the fluid; swinging the filler can prevent this phenomenon, ensure the uniform distribution of the filler, and make the gas fully contact with the purification liquid when passing through;

[0088] Effect 3: The swinging of the filler can improve the fluid distribution inside the filler, reduce the dead zone, that is, the area where the fluid flow is not smooth, and ensure that the gas and liquid flow more evenly; the filler with good fluidity can promote the passage of the gas in the purification tank 2, making the purification effect more uniform and efficient;

[0089] Effect 4: The tumbling filler can help maintain the stability of the liquid film, make the coverage of the liquid film more uniform, and thus improve the efficiency of adsorption and chemical reactions;

[0090] Effect 5: For the purification process relying on chemical reactions, the swinging filler can make the contact between the reactants and the catalyst in the purification liquid more sufficient, improving the reaction rate and effect.

[0091] By moving the liquid piston 403 back and forth, it triggers the opening and closing of the first hydraulic collar 4018, the first hydraulic push ring 4019, the first hydraulic telescopic rod 4020 and the first hydraulic pipe 4021 and the second hydraulic collar 4022, the second hydraulic push ring 4023, the second hydraulic telescopic rod 4024 and the second hydraulic pipe 4025, and controls the position switching of the liquid channel 4016 of the opening and closing valve core 4015 in the opening and closing valve body 4014, so that the opening and closing inlet pipe 4012 is connected to the power ring 401 or the opening and closing outlet pipe 4013 is connected to the power ring 401 for switching.

[0092] When the opening and closing inlet pipe 4012 and the power ring 401 are in the open state, the opening and closing outlet pipe 4013 and the power ring 401 are in the closed state. During this process, the spray head 509 stops spraying and there is an intermittent spraying situation for the spray head 509. To solve this intermittent spraying situation; Solution 1 is to use the liquid pistons 403 in the three filling tanks 202 with different moving stroke lengths in the power ring 401 to stagger the spraying of the spray heads 509 in the three filling tanks 202; Solution 2 is to open the solenoid valve 507 on the second branch pipe 506 during the intermittent state, connect the spray ring 508 and the spray head 509 through the second branch pipe 506, and make the spray head 509 spray the purification liquid. This device adopts Solution 2.

[0093] This device in the filling tank 202 can be in two working states. Working state 1: The bottom net plate 601, the closed ring 602 and the top net plate 603 can swing back and forth to make the filling material swing; Working state 2: The bottom net plate 601, the closed ring 602 and the top net plate 603 are fixed.

[0094] The function of the purification liquid is to remove the harmful components in the gas by contacting, dissolving or reacting with the pollutants in the gas; the function of the filling material is to increase the surface area of gas-liquid contact and promote good contact between the gas and the purification liquid.

[0095] The gas to be purified with small liquid droplets exits the filling tank 202 and enters the gas-liquid tank 203. The small liquid droplets are intercepted by the lower folding plate 702 and the upper folding plate 703. At this time, the gas enters the purification sleeve box 901 through the rotating gas pipe 8; the gas enters the breathable network pipe 905 through the purification sleeve box 901, and the gas is filtered by the activated carbon in the activated carbon box 904, enters the recovery box 3 from the activated carbon mesh plate 906 and the breathable port 902, and the purified gas is discharged from the recovery gas pipe 909 and stored by the gas storage device.

[0096] When cleaning this device, first open the electric switch valve 207, discharge the purification liquid in the liquid bottom tank 201 through the drain pipe 206, then pour the cleaning liquid or water through the inlet pipe 204, start the circulation pump 501, and according to the above movement state, make the bottom net plate 601, the closed ring 602 and the top net plate 603 swing back and forth, and the spray head 509 continuously sprays the cleaning liquid or water to clean the filling material.

[0097] After long-term use, contaminants or scale may accumulate on the surface of the packing material. By regularly spraying clean water or cleaning liquid and shaking the packing material from side to side, the accumulation of these contaminants can be effectively prevented, thereby avoiding the blockage of the pores of the packing material and maintaining its high specific surface area and gas-liquid contact efficiency. Shaking the packing material and cleaning the surface of the packing material helps to remove impurities and contaminants attached to the packing material and keep it clean. The adsorption capacity and reaction activity of the packing material are not affected by the accumulation of contaminants, ensuring stable and lasting purification effects. Spraying clean water or cleaning liquid can help dissolve and wash away the contaminants or impurities adsorbed on the surface of the packing material. This cleaning process is similar to the "regeneration" of the packing material, restoring its original adsorption capacity or reaction activity, helping to remove the accumulated contaminants, and enhancing the service life and purification effect of the packing material.

[0098] The above are the preferred embodiments of the present invention. It should be noted that for those of ordinary skill in the art, without departing from the principle of the present invention, several improvements and refinements can be made, and these improvements and refinements should also be regarded as the protection scope of the present invention.

Claims

1. A gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiment, comprising: A support frame and a purification tank arranged on the support frame, wherein a recovery box is fixed on the support frame; characterized in that it also includes: A power ring is fixed in the purification tank; a sealing block is fixed in the power ring and is used to divide the internal area of ​​the power ring; a liquid piston slides in the power ring; a spring sleeve is fixed in the power ring; a crankshaft is fixed on the liquid piston at one end and slides through the spring sleeve at the other end; a reset crankshaft is sleeved on the crankshaft, fixed on the liquid piston at one end and fixed on the spring sleeve at the other end, and is used to reset the liquid piston; a material ejector is fixed at the end of the crankshaft away from the liquid piston at the bottom, and is used to connect the filling material layer and drive the filling material layer, gas and purification liquid to perform dynamic contact and adsorption movement; A liquid supply assembly is fixed under the purification tank; a filling assembly rotates in the purification tank; a gas-liquid separation assembly is fixed in the purification tank; The gas transfer pipe has one end fixed above the purification tank and the other end extending into the recovery box; the activated carbon component is fixed in the recovery box to remove harmful substances in the gas; The blower is fixed under the purification tank; the first air inlet pipe is fixed on the blower; one end of the second air inlet pipe is fixed on the blower, and the other end is fixed under the purification tank; The controller is fixed on the support frame.

2. A gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiment according to claim 1, characterized in that: The purification tank includes a liquid bottom tank, a filling tank and a gas-liquid tank; The bottom of the liquid bottom tank is fixed on the support frame, there are three filling tanks, and the three filling tanks are arranged from bottom to top. The top of the liquid bottom tank is fixed under the filling tank, and the bottom of the gas-liquid tank is fixed above the filling tank.

3. A gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiment according to claim 2, characterized in that: Also includes: The liquid inlet ring pipe is located in the filling tank; the ring inlet pipe has one end extending out of the filling tank and the other end fixed on the liquid inlet ring pipe; the liquid outlet ring pipe is located in the filling tank; A ring outlet pipe, one end of which extends out of the filling tank, and the other end is fixed on the liquid outlet ring pipe; an opening and closing inlet pipe, one end of which is fixed on the power ring, and the other end is fixed on the liquid inlet ring pipe; an opening and closing outlet pipe, one end of which is fixed on the power ring, and the other end is fixed on the liquid outlet ring pipe; an opening and closing valve body, which is fixed on the opening and closing inlet pipe and the opening and closing outlet pipe; an opening and closing valve core, which slides in the opening and closing valve body and is used to move up and down in the opening and closing valve body to switch the flow channel, the opening and closing valve body is provided with a liquid channel, and the opening and closing valve body is provided with a mounting hole.

4. A gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiment according to claim 3, characterized in that: Also includes: A first hydraulic sleeve ring is fixed in the power ring; a first hydraulic push ring is slidably arranged in the first hydraulic sleeve ring and is located in the power ring; a first hydraulic telescopic rod has a fixed end fixed in the opening and closing valve body and a telescopic end fixed in the mounting hole; a first hydraulic pipe has one end fixed on the first hydraulic sleeve ring and the other end fixed on the first hydraulic telescopic rod; A second hydraulic collar is fixed in the power ring; a second hydraulic push ring is slidably arranged in the second hydraulic collar and is located in the power ring; a second hydraulic telescopic rod has a fixed end fixed in the opening and closing valve body and a telescopic end fixed in the mounting hole; a second hydraulic pipe has one end fixed on the second hydraulic collar and the other end fixed on the second hydraulic telescopic rod; The stroke crank groove is arranged above the power ring and sleeved above the crank push rod.

5. The gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiment according to claim 3, characterized in that: The liquid supply assembly comprises: A circulation pump is fixed on the liquid bottom tank; a liquid suction pipe is fixed on the circulation pump at one end and extends into the liquid bottom tank at the other end; a filter element tube is fixed below the liquid suction pipe at the top and is located in the liquid bottom tank; a liquid supply pipe is fixed on the circulation pump at one end and extends into the filling tank at the other end.

6. A gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiment according to claim 5, characterized in that: The liquid supply assembly also includes: The first branch pipe has one end fixed on the liquid supply pipe and the other end fixed on the ring inlet pipe; the second branch pipe has one end fixed on the liquid supply pipe and the other end extending into the filling tank; the solenoid valve is fixed on the first branch pipe and the second branch pipe and is located outside the filling tank, and is used to control the opening and closing of the two branch pipes; the spray ring is located in the filling tank, one side is fixed on the second branch pipe, and the other side is fixed on the ring outlet pipe; the spray head is fixed on the spray ring.

7. A gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiment according to claim 2, characterized in that: A liquid inlet pipe is fixed above the liquid bottom tank, a cone is fixed below the liquid bottom tank, a liquid discharge pipe is fixed below the cone, an electric switch valve is fixed to the liquid discharge pipe, and a limit plate is fixed inside the liquid bottom tank.

8. The gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiment according to claim 2, characterized in that: The filling assembly comprises: The bottom mesh plate is fixed above the crankshaft and is located in the filling tank; the closed ring is fixed above the bottom mesh plate and is located in the filling tank; the top mesh plate is fixed above the closed ring and is located in the filling tank. The bottom mesh plate, the closed ring and the top mesh plate together form a filling material area.

9. The gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiment according to claim 2, characterized in that: The gas-liquid separation component comprises: The gas-liquid ring is fixed in the gas-liquid tank; the lower folding plate is fixed in the gas-liquid ring; the upper folding plate is fixed in the gas-liquid ring and is located above the lower folding plate; the inclined surfaces of the lower folding plate and the upper folding plate are used to intercept small liquid drops in the gas.

10. The gas recovery and purification device for ethoxy pentafluorocyclotriphosphazene production experiment according to claim 2, characterized in that: The activated carbon assembly comprises: The purification box is located in the recovery box; the air vents are opened on both sides of the purification box; the fixing plate is fixed in the recovery box and fixed on the purification box from below; the activated carbon box slides in the purification box; the air permeable mesh pipe is fixed in the activated carbon box; the activated carbon mesh plate is fixed on both sides of the activated carbon box; the closing plate is fixed on the activated carbon box; the handle is fixed on the closing plate; the recovery air pipe is fixed below the recovery box.

Citation Information

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