Water-vapor separation device for waste gas treatment process
By installing a water vapor separation device between the spray tower and the dry filter box, and using a swirl blade cooler to condense the water vapor in the exhaust gas, the problem of equipment blockage caused by high water vapor content after the spray tower is solved, and the filtration and adsorption effects are improved.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-05-07
- Publication Date
- 2026-04-10
AI Technical Summary
In existing waste gas treatment processes, the gas after spraying has a high water vapor content, which can easily cause blockage of subsequent filtration and adsorption equipment.
A water vapor separation device is installed between the spray tower and the dry filter box, including a three-way pipe, a water storage component and a swirl component. The swirl blades cool the exhaust gas, causing the water vapor to condense and be collected, thus preventing water vapor from being carried into subsequent equipment.
This effectively prevents water vapor from condensing and clogging in the dry filter box and activated carbon adsorption box, improving the filtration and adsorption effect and extending the service life of the equipment.
Smart Images

Figure CN224100327U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model relates to waste gas treatment technical field especially, relates to a water vapor separation device for waste gas treatment process. BACKGROUND
[0002] The waste gas produced in industrial production usually contains a large amount of dust, volatile organic compounds, acid gases, heavy metal particles and other pollutants. If these pollutants are directly discharged without effective treatment, not only will they seriously pollute the atmospheric environment and harm human health, but also may violate environmental protection regulations. Therefore, waste gas treatment has become an indispensable environmental protection link in industrial production.
[0003] The existing industrial waste gas treatment process generally uses the way of spray tower, such as Figure 1 As shown, the spray tower realizes the preliminary removal of gas cooling, dust and soluble pollutants through water mist spraying, and then the gas enters the dry filter box and the activated carbon adsorption box in sequence through the pipeline for secondary filtration, and is discharged by the fan again.
[0004] However, the gas after spraying will carry a large amount of water vapor and tiny droplets, if directly entering the dry filter box and the activated carbon adsorption box, the water vapor will condense a lot on the filter material and the adsorption material even block, resulting in the significant reduction of the filtration effect and the adsorption effect, and the filter material and the adsorption material need to be replaced frequently. UTILITY MODEL CONTENT
[0005] The utility model aims at providing a water vapor separation device for waste gas treatment process, solving the problem that the water vapor content in the gas after spraying is high in the existing waste gas treatment process, which is easy to cause the subsequent filtration and adsorption blockage.
[0006] In order to achieve this purpose, the utility model adopts the following technical scheme:
[0007] A water vapor separation device for waste gas treatment process is connected to the gas outlet end of the spray tower, characterized in that it comprises:
[0008] A three-way pipe, the first port of the three-way pipe is connected to the spray tower, and the second port is connected to the dry filter box;
[0009] A water storage assembly is arranged at the third port of the three-way pipe, and the third port is located below the first port and the second port;
[0010] A cyclone assembly is arranged at the position close to the first port on the three-way pipe, and the cyclone assembly at least comprises a cooler and a cyclone vane, the cooler is arranged outside the three-way pipe, and the cyclone vane is arranged inside the three-way pipe.
[0011] Optionally, the cyclone assembly further comprises:
[0012] A gas collecting pipe, the cyclone vane is sleeved outside the gas collecting pipe, and a plurality of gas outlet holes are spirally and spaced apart on the pipe wall near the upper end;
[0013] An air inlet funnel is connected to the top end of the gas collecting pipe.
[0014] Optionally, the cyclone assembly further comprises:
[0015] A leakage member is movably arranged at the lower end of the gas collecting pipe.
[0016] Optionally, the cyclone assembly further comprises:
[0017] A flow baffle is arranged on the cyclone vane, and a plurality of flow baffles are spaced apart.
[0018] The height of the flow baffle is less than the pitch of the cyclone vane, and the adjacent two flow baffles are arranged in a staggered manner.
[0019] Optionally, a flow guide groove is formed in the cyclone vane.
[0020] Optionally, the cyclone assembly further comprises:
[0021] A fan is arranged inside the gas collecting pipe and located at the upper end of the gas collecting pipe.
[0022] Optionally, the three-way pipe has a hydrophobic coating on the inner wall.
[0023] Optionally, the water vapor separation device further comprises:
[0024] An air outlet pipe is connected between the second port and the dry filter box, and the air outlet pipe is gradually inclined upward in the direction of the three-way pipe to the dry filter box.
[0025] Optionally, the water storage assembly comprises:
[0026] A sealing cover is movably connected to the third port of the three-way pipe.
[0027] A water leakage bucket is arranged in the sealing cover.
[0028] A water collecting bottle is screwed to the bottom of the sealing cover and communicates with the water leakage bucket.
[0029] Optionally, the water storage assembly further comprises:
[0030] A water permeable plate is arranged inside the three-way pipe and located above the water leakage bucket.
[0031] Compared with the prior art, the utility model has the following beneficial effects:
[0032] The utility model provides a water vapor separation device for waste gas treatment process, through setting up water vapor separation device between spraying tower and dry type filter case, after the waste gas of spraying enters the tee pipe from first port and flows downward, the flow velocity of waste gas is slowed down when passing cyclone vane, the waste gas that passes cyclone vane is cooled by cooler, the water vapor in waste gas can condense into liquid water, liquid water flows to third port along tee pipe wall and enters water storage component, thereby can realize the separation of waste gas and water vapor, can effectively avoid the waste gas carrying a large amount of water vapor to enter dry type filter case and the activated carbon adsorption tank of rear end, and then can avoid the dry type filter case and activated carbon adsorption tank to be blocked because of the adsorption of a large amount of moisture of filter material and adsorption material, be favorable to improving the absorption effect and service life of dry type filter case and activated carbon adsorption tank. BRIEF DESCRIPTION OF DRAWINGS
[0033] In order to more clearly illustrate the technical scheme in the embodiments of the utility model or prior art, the following will briefly introduce the drawings needed to be used in the embodiment or prior art description, obviously, the drawings in the following description are only some embodiments of the utility model, and for those skilled in the art, other drawings can also be obtained according to these drawings without creative labor.
[0034] The structure, proportion, size and the like shown in the drawings of the specification are only used to cooperate with the content disclosed in the specification, to enable those skilled in the art to understand and read, and are not used to limit the limiting conditions that can be implemented by the utility model, so they do not have technical substantive significance, any modification of structure, change of proportion relationship or adjustment of size, without affecting the effect and purpose that can be produced by the utility model, should still fall within the scope covered by the technical content disclosed by the utility model.
[0035] Figure 1 It is a waste gas treatment process schematic diagram in prior art.
[0036] Figure 2 It is a water vapor separation device structure schematic diagram for waste gas treatment process.
[0037] Figure 3 It is a tee pipe structure schematic diagram in the water vapor separation device for waste gas treatment process.
[0038] Figure 4 It is a tee pipe structure sectional view in the water vapor separation device for waste gas treatment process.
[0039] Figure 5 It is a heavy cyclone component structure schematic diagram in the water vapor separation device for waste gas treatment process.
[0040] Illustration: 1, spray tower; 2, dry filter box; 3, activated carbon adsorption box; 4, three-way pipe; 41, first port; 42, second port; 43, third port; 5, cyclone assembly; 51, cooler; 52, cyclone vane; 53, gas collecting pipe; 531, gas outlet; 54, air inlet funnel; 55, leakage; 56, flow baffle; 57, flow guide groove; 6, water storage assembly; 61, sealing cover; 62, water leakage funnel; 63, water collecting bottle; 64, water seepage plate; 7, gas outlet pipe. DETAILED DESCRIPTION
[0041] In order to make the application purpose, features and advantages of the utility model more obvious and easy to understand, the technical solutions in the embodiments of the utility model will be clearly and completely described below in combination with the drawings in the embodiments of the utility model. Obviously, the embodiments described below are only part of the embodiments of the utility model, rather than all the embodiments. Based on the embodiments in the utility model, all other embodiments obtained by those skilled in the art without creative labor belong to the scope of protection of the utility model.
[0042] In the description of the utility model, it should be understood that the terms "upper", "lower", "top", "bottom", "inner", "outer" and the like indicate the orientation or positional relationship shown in the drawings, and are only for the convenience of describing the utility model and simplifying the description, and do not indicate or imply that the devices or elements referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore cannot be understood as a limitation on the utility model. It should be noted that when a component is considered to be "connected" to another component, it can be directly connected to the other component or there can be a component disposed therebetween.
[0043] In the industrial waste gas treatment process, the waste gas is preliminarily removed of large-particle dust in the spray tower. However, the gas after spraying carries a large amount of water vapor, and if it directly enters the subsequent filtering and adsorbing equipment, the water is adsorbed on the filtering material in large quantities, causing blockage.
[0044] Based on this, the utility model embodiment provides a water vapor separation device for waste gas treatment process, which is connected to the gas outlet end of the spray tower. The water vapor separation device comprises a three-way pipe, a water storage assembly and a cyclone assembly. The first port of the three-way pipe is connected to the spray tower, and the second port is connected to the dry filter box. The water storage assembly is arranged on the third port of the three-way pipe, and the third port is located below the first port and the second port. The cyclone assembly is arranged on the three-way pipe at a position close to the first port, and the cyclone assembly at least comprises a cyclone vane of a cooler. The cooler is arranged outside the three-way pipe, and the cyclone vane is arranged inside the three-way pipe.
[0045] By setting the water vapor separation device between the spray tower and the dry filter box, the waste gas after spraying enters the tee pipe from the first port and flows downward, the flow speed of the waste gas is slowed down when passing through the cyclone vane, the cooler cools the waste gas passing through the cyclone vane, and the water vapor in the waste gas can be condensed into liquid water, the liquid water flows to the third port along the tee pipe wall and enters the water storage assembly, so that the separation of waste gas and water vapor can be realized, and effectively avoiding the waste gas carrying a large amount of water vapor into the dry filter box and the active carbon adsorption box at the rear end, which is beneficial to improve the absorption effect and service life of the dry filter box and the active carbon adsorption box.
[0046] The technical solutions of the utility model are further illustrated below in combination with the drawings and through specific embodiments.
[0047] As Figure 2 , Figure 3 , Figure 4 The utility model discloses a water vapor separation device for waste gas treatment process is provided, and is connected to the gas outlet end of spray tower 1, and the water vapor separation device includes tee pipe 4, water storage assembly 6 and cyclone assembly 5. The first port 41 of tee pipe 4 is connected to spray tower 1, and the second port 42 is connected to dry filter box 2. The water storage assembly 6 is arranged on the third port 43 of the tee pipe 4, and the third port 43 is located below the first port 41 and the second port 42. The cyclone assembly 5 is arranged on the tee pipe 4 at a position close to the first port 41, and the cyclone assembly 5 at least includes the cyclone vane 52 of the cooler 51. The cooler 51 is arranged on the outside of the tee pipe 4, and the cyclone vane 52 is arranged in the tee pipe 4.
[0048] Specifically, the water vapor separation device can be installed in the waste gas treatment process between the spray tower 1 and the dry filter box 2 to separate the water vapor in the waste gas after spraying. The tee pipe 4 has a first port 41, a second port 42 and a third port 43, the first port 41 and the third port 43 are on the same vertical line, and the third port 43 is below the first port 41 and the second port 42. The first port 41 of the tee pipe 4 is connected to the gas outlet end of the spray tower 1, and the second port 42 is connected to the gas inlet end of the dry filter box 2. The cyclone assembly 5 is arranged on the tee pipe 4 and located on the side close to the first port 41, for separating the water vapor in the waste water. Among them, the cooler 51 can be a circulating water cooling cooler 51, a air-cooled cooler 51 and the like, for continuously providing cold to the inside of the tee pipe 4 at the location; the cyclone vane 52 is a spiral vane structure similar to a screw.
[0049] The waste gas is sprayed by the spray tower 1, enters the tee pipe 4 from the third port 43 and flows downward, when the waste gas flows through the cyclone assembly 5, the cyclone vane 52 increases the flow path of the waste gas, the time of the waste gas flow through the cyclone vane 52 part is increased, the cooler 51 arranged outside the tee pipe 4 can continuously cool the waste gas flowing through the cyclone vane 52 part, the water vapor in the waste gas can be condensed into liquid water, and the liquid water can directly drip or flow along the wall of the tee pipe 4 to the third port 43 and enter the water storage assembly 6, and the separated waste gas can enter the dry filter box 2 from the second port 42. Thus, the water vapor in the waste gas can be separated, the waste gas carrying a large amount of water vapor can be effectively avoided to enter the dry filter box 2 and the activated carbon adsorption box 3 at the rear end, and then the dry filter box 2 and the activated carbon adsorption box 3 can be avoided to be blocked due to the adsorption of a large amount of water by the filter material and the adsorption material, and the absorption effect and the service life of the dry filter box 2 and the activated carbon adsorption box 3 can be improved.
[0050] For example, the wall of the tee pipe 4 can be a metal pipe or a glass pipe with high thermal conductivity at the position where the cooler 51 is arranged, so as to improve the heat exchange efficiency between the cooler 51 and the tee pipe 4.
[0051] As shown in Figure 3 , Figure 4 and Figure 5 , in the embodiment of the utility model, the cyclone assembly 5 further includes a gas collecting pipe 53 and an air inlet funnel 54. The cyclone vane 52 is sleeved on the outer wall of the gas collecting pipe 53, and a plurality of air outlet holes 531 are spirally and spaced apart on the wall of the gas collecting pipe 53 close to the upper end. The air inlet funnel 54 is connected to the top end of the gas collecting pipe 53.
[0052] Specifically, the air inlet funnel 54 is connected to the top end of the gas collecting pipe 53, the waste gas enters the gas collecting pipe 53 from the air inlet funnel 54, and then flows in the gas collecting pipe 53 and enters the lumen where the cyclone vane 52 is located from the air outlet hole 531. The speed of the waste gas flow through the cyclone assembly 5 can be further slowed down, and the separation effect of the water vapor in the waste gas can be improved.
[0053] Further, the cyclone assembly 5 further includes a leakage member 55. The leakage member 55 is movably arranged at the lower end of the gas collecting pipe 53. The leakage member 55 can prevent the waste gas from flowing out from the bottom end of the gas collecting pipe 53, and the liquid water condensed in the gas collecting pipe 53 can be collected at the bottom of the gas collecting pipe 53 and then seep out and drip to the water storage assembly 6 through the leakage member 55. At the same time, the dust and other small particulate matters mixed in the waste gas can also be collected at the bottom of the gas collecting pipe 53 and filtered by the leakage member 55. The leakage member 55 is movably installed at the bottom of the gas collecting pipe 53, and can be replaced or maintained regularly to avoid blockage of the leakage member 55.
[0054] As shown in Figure 4 , Figure 5As shown, in an embodiment of the utility model, cyclone assembly 5 further includes baffle 56. Baffle 56 is fixedly connected to cyclone vane 52, and multiple baffles 56 are arranged at intervals. The height of baffle 56 is less than the pitch of cyclone vane 52, and the adjacent two baffles 56 are arranged in an up-down staggered manner.
[0055] Specifically, baffle 56 is a vertical plate fixed to cyclone vane 52, multiple baffles 56 are arranged at intervals in a spiral manner along cyclone vane 52, and the adjacent two baffles 56 are arranged in an up-down staggered manner, that is, one of the two adjacent baffles 56 is fixedly connected to cyclone vane 52 at the lower end, and the other is fixedly connected to cyclone vane 52 at the upper end. When the exhaust gas flows through cyclone vane 52, the water vapor in the exhaust gas will adhere to the inner wall of three-way pipe 4 and cyclone vane 52, and baffle 56 can increase the adhesion area of water vapor and improve the water vapor separation efficiency. At the same time, the adjacent two baffles 56 are arranged in an up-down staggered manner, so that the exhaust gas can flow in an S-shaped flow direction when flowing through cyclone vane 52, which can further slow down the flow speed of the exhaust gas and improve the water vapor separation efficiency.
[0056] Further, a guide groove 57 is formed on cyclone vane 52, and the guide groove 57 is spiral downward. After the water vapor adhering to the wall of three-way pipe 4, cyclone vane 52 and baffle 56 is condensed into liquid water, it can flow down along the guide groove 57.
[0057] Still further, cyclone assembly 5 can further include a fan, which is arranged inside the gas collecting pipe 53 and located at the upper end of the gas collecting pipe 53. The fan is arranged towards the inside of the gas collecting pipe 53, and the fan can accelerate the rate of exhaust gas entering the gas collecting pipe 53. The fan blows air into the gas collecting pipe 53, which can accelerate the circulation of exhaust gas in the gas collecting pipe 53 and discharge it from the air outlet 531, avoiding the accumulation of exhaust gas in the gas collecting pipe 53.
[0058] Still further, the inner wall of three-way pipe 4 has a hydrophobic coating, and the outer surface of cyclone vane 52 and the outer surface of baffle 56 can also be coated with a hydrophobic coating. This can reduce water droplet adhesion and promote the rapid flow of condensed water to the third port 43.
[0059] In the utility model embodiment, the water vapor separation device further comprises an air outlet pipe 7, the air outlet pipe 7 is connected between the second port 42 and the dry filter box 2, and the air outlet pipe 7 is gradually inclined upwards along the direction of the tee pipe 4 to the dry filter box 2. After flowing through the cyclone assembly 5, the exhaust gas enters the air outlet pipe 7 from the second port 42 and enters the dry filter box 2 from the air outlet pipe 7. The exhaust gas after passing through the cyclone assembly 5 can still carry water vapor, so that the water vapor can be attached to the wall of the air outlet pipe 7, and the water droplets after condensation can flow in the air outlet pipe 7, and the water droplets on the wall of the tee pipe 4 close to the first port 41 side can also flow into the air outlet pipe 7. Therefore, the air outlet pipe 7 is inclined to be arranged, so that the water droplets in the air outlet pipe 7 can be prevented from flowing into the dry filter box 2, and the water vapor separation effect is further improved.
[0060] As shown in Figure 3 , Figure 4 In the utility model embodiment, the water storage assembly 6 comprises a sealing cover 61, a water leakage bucket 62 and a water collecting bottle 63. The sealing cover 61 is movably connected to the third port 43 of the tee pipe 4; the water leakage bucket 62 is arranged in the sealing cover 61; and the water collecting bottle 63 is screwed to the bottom of the sealing cover 61 and communicates with the water leakage bucket 62.
[0061] Specifically, the sealing cover 61 is installed at the third port 43 of the tee pipe 4 to prevent the exhaust gas from flowing out of the third port 43, the water leakage bucket 62 is arranged in the sealing cover 61, the upper end edge of the water leakage bucket 62 is aligned with the inner wall of the tee pipe 4, and the water droplets flowing down along the inner wall of the tee pipe 4 can flow into the water collecting bottle 63 through the water leakage bucket 62. The water collecting bottle 63 can be cleaned regularly.
[0062] Further, the water storage assembly 6 further comprises a water permeable plate 64, which is arranged inside the tee pipe 4 and above the water leakage bucket 62. The water permeable plate 64 can be made of cloth or a plate material having a permeation effect, and is arranged on the side of the tee pipe 4 close to the third port 43 and can be flush with the lower end of the second port 42. The water droplets flowing down along the wall of the tee pipe 4 can permeate through the water permeable plate 64 and then fall on the water leakage bucket 62, and meanwhile, the water permeable plate 64 can block the exhaust gas from entering the cavity of the tee pipe 4 below to prevent the exhaust gas from gathering in the lower section of the tee pipe 4.
[0063] For example, the water storage assembly 6 comprises the sealing cover 61, an electromagnetic valve and a liquid level sensor, and the electromagnetic valve is installed on the sealing cover 61, and when the accumulated water level reaches a set value, the electromagnetic valve is opened to automatically drain water.
[0064] The above-described above embodiments are only used to illustrate the technical solutions of the present application, and are not limited thereto; although the present application has been described in detail with reference to the foregoing embodiments, those skilled in the art should understand that the technical solutions recorded in the foregoing embodiments can still be modified, or some technical features therein can be replaced by equivalents; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the spirit and scope of the technical solutions of the embodiments of the present application.
Claims
1. A water vapor separation device for exhaust gas treatment processes, connected to the gas outlet end of a spray tower (1), characterized in that, The utility model relates to a water vapor separation device, including: A three-way pipe (4), the first port (41) of the three-way pipe (4) is connected to the spray tower (1), and the second port (42) is connected to the dry filter box (2); A water storage assembly (6) is arranged at the third port (43) of the three-way pipe (4), and the third port (43) is located below the first port (41) and the second port (42); A cyclone assembly (5) is arranged on the three-way pipe (4) close to the first port (41), and the cyclone assembly (5) at least includes a cooler (51) and a cyclone vane (52), the cooler (51) is arranged outside the three-way pipe (4), and the cyclone vane (52) is arranged inside the three-way pipe (4).
2. The water vapor separation device for an exhaust gas treatment process according to claim 1, characterized in that, The cyclone assembly (5) further includes: A gas collecting pipe (53), the cyclone vane (52) is sleeved outside the gas collecting pipe (53), and a plurality of air outlet holes (531) are spirally and spaced apart on the pipe wall close to the upper end of the gas collecting pipe (53); An air inlet funnel (54) is connected to the top end of the gas collecting pipe (53).
3. The water vapor separation device for an exhaust gas treatment process according to claim 2, characterized in that, The cyclone assembly (5) further includes: A leakage piece (55) movably arranged at the lower end of the gas collecting pipe (53).
4. The water vapor separation device for an exhaust gas treatment process of claim 2, wherein, The cyclone assembly (5) further includes: A flow baffle (56) is arranged on the cyclone vane (52), and a plurality of flow baffles (56) are spaced apart. The height of the flow baffle (56) is less than the pitch of the cyclone vane (52), and the adjacent two flow baffles (56) are arranged in a staggered manner.
5. The water vapor separation device for an exhaust gas treatment process of claim 4, wherein, A flow guide groove (57) is formed in the cyclone vane (52).
6. The water vapor separation device for an exhaust gas treatment process of claim 2, wherein, The cyclone assembly (5) further includes: A fan is arranged inside the gas collecting pipe (53) and located at the upper end of the gas collecting pipe (53).
7. The water vapor separation device for an exhaust gas treatment process of claim 5, wherein, The inner wall of the three-way pipe (4) has a hydrophobic coating.
8. The water vapor separation device for an exhaust gas treatment process of claim 1, wherein, The water vapor separation device further includes: An air outlet pipe (7) is connected between the second port (42) and the dry filter box (2), and the air outlet pipe (7) is gradually inclined upward along the three-way pipe (4) towards the dry filter box (2).
9. The water vapor separation device for an exhaust gas treatment process of claim 1, wherein, The water storage assembly (6) includes: A sealing cover (61) movably connected to the third port (43) of the three-way pipe (4); A water leakage bucket (62) is arranged in the sealing cover (61); A water collecting bottle (63) is screwed on the bottom of the sealing cover (61) and communicates with the water leakage bucket (62).
10. The water vapor separation device for an exhaust gas treatment process of claim 9, wherein, The water storage assembly (6) further includes: A water seepage plate (64) is arranged inside the three-way pipe (4) and located above the water leakage bucket (62).