CN219209416U - Cyclone spray tower and exhaust gas treatment assembly line - Google Patents

Abstract

The utility model discloses a cyclone spray tower and an exhaust gas treatment assembly line, wherein the spray tower comprises a tower body, a cyclone barrel and a funnel, the tower body is provided with a spray chamber, a filter ball and a plurality of mounting seats are arranged in the spray chamber, heating pipes are arranged in the mounting seats and positioned below the filter ball, and a plurality of heating pipes are arranged at intervals along the circumferential direction of the spray chamber and form a heating zone; the swirl barrel is installed in spray room below, and the bottom of funnel is connected with the water tank, and the water pump is installed to the water tank, and the water pump is connected with circulating line, and circulating line's delivery port sets up towards the spray room. Through setting up the heating pipe, can effectively improve the liveness of liquid molecule, make liquid molecule and dust granule contact fusion more frequently, improve the speed that dust and liquid combine by a wide margin, effectively improve exhaust treatment efficiency, reinforcing exhaust purification's effect.

Description

Cyclone spray tower and exhaust gas treatment assembly line

Technical Field

The utility model relates to the technical field of waste gas treatment, in particular to a cyclone spray tower and a waste gas treatment assembly line.

Background

The cyclone spray tower is one of the mainstream exhaust gas treatment equipment, and its main structure includes the cyclone tower and sprays the layer, and waste gas lets in the cyclone tower from the outside and begins high-speed rotation, and the smoke and dust in the waste gas combines together with the liquid that sprays the layer and flow down, and the rethread centrifugal force realizes gas-liquid separation to purify waste gas, current spray tower spun water source is difficult to with contain the abundant contact of dust's gas, and its exhaust gas treatment efficiency is low, and exhaust gas purification effect is not good.

Disclosure of Invention

The present utility model aims to solve at least one of the technical problems in the related art to some extent. Therefore, the cyclone spray tower provided by the utility model can effectively improve the waste gas treatment efficiency and enhance the waste gas purification effect.

The utility model provides an exhaust gas treatment assembly line comprising the cyclone spray tower.

According to an embodiment of the first aspect of the utility model, the cyclone spray tower comprises a tower body, a cyclone barrel and a funnel, wherein the tower body is provided with a spray chamber, a filter ball and a plurality of heating pipes are arranged in the spray chamber, the heating pipes are positioned below the filter ball, and the heating pipes are arranged at intervals along the circumferential direction of the spray chamber and form a heating zone; the cyclone barrel is arranged below the spray chamber and is provided with an inlet and an outlet, and the outlet is communicated with the heating area; the funnel install in whirl bucket below, one side of funnel is equipped with the air intake, the air intake with the entry intercommunication, the bottom of funnel is connected with the water tank, the water pump is installed to the water tank, the water pump is connected with circulating line, circulating line's one end with the water tank intercommunication, the other end is located spray room top, circulating line's delivery port orientation spray room setting.

According to the cyclone spray tower provided by the embodiment of the first aspect of the utility model, the cyclone spray tower has at least the following beneficial effects: when the spray tower works, waste gas firstly enters the inlet of the cyclone barrel from the air inlet, then starts to move upwards at a high speed under the guidance of the circulation, meanwhile, liquid in the water tank is sprayed to the spray chamber through the circulating pipeline, the liquid enters the spray chamber and then is heated by the heating area, the liquid continuously moves downwards and is intersected with the waste gas at the partition plate at the top of the cyclone barrel, smoke dust and liquid particles in the waste gas are combined and separated from gas under the action of centrifugal force, finally fall into the bottom of the water tank, the heating pipe is arranged and the heating area is formed to heat the liquid, so that the activity of liquid molecules can be effectively improved, the liquid molecules and dust particles are contacted and fused more frequently, the rate of combining dust and liquid is greatly improved, the waste gas treatment efficiency is effectively improved, and the waste gas purification effect is enhanced.

According to some embodiments of the utility model, the cyclone barrel is provided with a plurality of inlets, and the inlets of the cyclone barrels are arranged towards the same side and are communicated with the air inlet.

According to some embodiments of the utility model, the spray chamber is fitted with a protective cover covering the heating tube.

According to some embodiments of the utility model, the tower body is provided with a pressure detector, the pressure detector is electrically connected with the heating pipe, and a detection end of the pressure detector is arranged towards the heating area.

According to some embodiments of the utility model, an overflow tank is installed between the funnel and the water tank, an outlet of the funnel is accommodated in the overflow tank, an overflow port is arranged on one side of the overflow tank, facing the water tank, of the overflow tank, and the overflow port is communicated with the water tank.

According to some embodiments of the utility model, a filter screen is installed between the overflow tank and the water tank, the overflow tank is provided with a guide plate, the guide plate is positioned between the overflow port and the filter screen, and the guide plate is arranged in a downward inclined way near a section of the overflow port.

According to some embodiments of the utility model, the spray chamber is connected with a hollowed-out drawer, the hollowed-out drawer is in sliding fit with the spray chamber, and the filter ball is mounted on the hollowed-out drawer.

According to some embodiments of the utility model, a plurality of hollowed-out drawers are arranged, and the hollowed-out drawers are arranged at intervals along the vertical direction.

According to some embodiments of the utility model, the swirl pot and the spray chamber are both provided with an observation window on the same side.

An exhaust gas treatment line according to an embodiment of the second aspect of the present utility model comprises a cyclonic spray tower according to an embodiment of the first aspect.

Additional aspects and advantages of the utility model will be set forth in part in the description which follows, and in part will be obvious from the description, or may be learned by practice of the utility model.

Drawings

FIG. 1 is a front view of a cyclonic spray tower according to an embodiment of the present utility model;

FIG. 2 is an enlarged view of FIG. 1A;

FIG. 3 is a side view of a cyclonic spray tower according to an embodiment of the present utility model;

fig. 4 is an enlarged view of B in fig. 2.

Reference numerals: a tower 100; a spray chamber 110; a filter ball 120; a heating pipe 130; a protective cover 140; hollow drawer 150; a viewing window 160; a mounting base 170; swirl barrels 200; an inlet 210; an outlet 220; a funnel 300; an air inlet 310; a water tank 320; a water pump 330; a circulation pipe 340; overflow tank 350; an overflow 351; a guide plate 352; a screen 360.

Detailed Description

Embodiments of the present utility model are described in detail below, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to like or similar elements or elements having like or similar functions throughout. The embodiments described below by referring to the drawings are illustrative only and are not to be construed as limiting the utility model.

In the description of the present utility model, a number means one or more, a number means two or more, and greater than, less than, exceeding, etc. are understood to not include the present number, and above, below, within, etc. are understood to include the present number. The description of the first and second is for the purpose of distinguishing between technical features only and should not be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated or implicitly indicating the precedence of the technical features indicated.

Embodiments of the present application are further described below with reference to the accompanying drawings.

Referring to fig. 1 to 4, a cyclone spray tower according to an embodiment of the present utility model includes a tower body 100, a cyclone barrel 200 and a funnel 300, the tower body 100 is provided with a spray chamber 110, the spray chamber 110 is provided with a filter ball 120 and a plurality of mounting seats 170, heating pipes 130 are installed in the mounting seats 170, the heating pipes 130 are positioned under the filter ball 120, the plurality of heating pipes 130 are spaced apart along the circumference of the spray chamber 110 and form a heating zone, and since the cyclone spray tower body is generally provided as a cube, the plurality of heating pipes 130 can also be regarded as being spaced apart along a rectangular border of a horizontal section of the cube and form a rectangular heating zone; the cyclone barrel 200 is arranged below the spray chamber 110, the cyclone barrel 200 is provided with an inlet 210 and an outlet 220, and the outlet 220 is communicated with the heating area; the funnel 300 is installed in swirl barrel 200 below, and one side of funnel 300 is equipped with air intake 310, and air intake 310 and entry 210 intercommunication, and the bottom of funnel 300 is connected with water tank 320, and water tank 320 installs water pump 330, and water pump 330 is connected with circulation pipeline 340, and circulation pipeline 340's one end and water tank 320 intercommunication, the other end is located spray room 110 top, and circulation pipeline 340's delivery port sets up towards spray room 110.

It can be understood that, during operation of the spray tower, the exhaust gas enters the inlet 210 of the cyclone barrel 200 from the air inlet 310, and then starts to move upwards at a high speed under the guidance of the circulation flow, meanwhile, the circulating pipeline 340 sprays the liquid in the water tank 320 to the spray chamber 110, the liquid enters the spray chamber 110 and is heated by the heating area, and continues to move downwards and is converged with the exhaust gas at the fan-shaped partition plate (not shown in the figure) at the top of the cyclone barrel 200, the smoke dust and the liquid particles in the exhaust gas are combined and separated from the gas under the centrifugal force, finally fall into the bottom of the water tank 320, and the heating pipe 130 is arranged to heat the liquid to form the heating area, so that the activity of the liquid molecules can be effectively improved, the liquid molecules and the dust particles are more frequently contacted and fused, the rate of dust and liquid combination is greatly improved, the exhaust gas treatment efficiency is effectively improved, and the exhaust gas purification effect is enhanced.

Further, the cyclone barrel 200 is provided in plurality, and the inlets 210 of the cyclone barrels 200 are disposed toward the same side and are all communicated with the air inlet 310. The cyclone barrels 200 are arranged in a plurality, so that the air inflow of the spray tower can be increased, more waste gas can be treated by the spray tower in the same time, the inner space of the tower body 100 is reasonably utilized, and the waste gas treatment efficiency of the spray tower is further improved.

Referring to fig. 1, it can be understood that the spray chamber 110 is connected with a hollowed drawer 150, the hollowed drawer 150 is slidably matched with the spray chamber 110, and the filter ball 120 is installed on the hollowed drawer 150. The hollow drawer 150 is a drawer with a hollow structure (not shown in the figure) arranged at the bottom and the periphery, the hollow drawer 150 can ensure that liquid smoothly passes through the spraying layer, the filter balls 120 are installed through the hollow drawer 150, the filter balls 120 can be checked and replaced by a user pulling the hollow drawer 150, the hollow drawer 150 is simple in structure and convenient to operate, the use experience of the user can be effectively improved, and the maintenance cost of the later stage of the spray tower is reduced.

Further, the hollowed-out drawers 150 are provided with a plurality of hollowed-out drawers 150, and the hollowed-out drawers 150 are arranged at intervals along the vertical direction. The hollowed-out drawers 150 are arranged in a plurality, more filtering solutions can be installed on the hollowed-out drawers 150, so that water mist blown out from circulation selection can be absorbed more comprehensively and effectively, the purity of discharged gas is improved, and the exhaust gas purifying effect of the spray tower is further enhanced.

Referring to fig. 2, it can be understood that the shower chamber 110 is installed with a protective cover 140, and the protective cover 140 is covered on the heating pipe 130. The protective cover 140 is arranged outside the heating pipe 130, and the protective cover 140 can protect the heating pipe 130, so that corrosion of waste gas, liquid and water mist to the heating pipe 130 is reduced, and the service life of the heating pipe 130 is effectively prolonged.

Further, the tower body 100 is provided with a pressure detector, and the pressure detector is electrically connected with the heating pipe 130, and the detection end of the pressure detector is arranged towards the heating area. The heating pipe 130 can slowly rise the regional temperature of the heating zone in the operation process, and this can lead to the pressure of the heating zone to rise simultaneously, and high temperature and high pressure's environment easily causes the potential safety hazard, through setting up pressure detector, pressure detector can real-time detection heating zone's pressure numerical value and feed back to the heating pipe 130, and heating pipe 130 changes heating temperature according to actual pressure value to adjust heating chamber's temperature and pressure, make heating chamber's temperature and pressure's vertical keep in reasonable within range, under the prerequisite that improves liquid molecule liveness, improve spray tower's safety in utilization.

It should be noted that, since the operation temperature of the heating area is generally greater than 100 degrees and greater than the boiling point of water, the liquid in the water tank 320 (or the circulation pipe 340) is not generally pure water (when the liquid is water, the heating pipe 130 adopts a low-temperature heating mode to avoid evaporation and gasification of pure water as much as possible), but industrial clean oil with a high boiling point and good adhesion or a chemical solvent with similar properties, and the type of the circulation liquid is not particularly limited as long as the circulation liquid can be effectively fused with smoke particles in the exhaust gas.

Referring to fig. 1 and 3, it can be appreciated that both the swirl pot 200 and the spray chamber 110 are provided with an observation window 160 on the same side. Through setting up observation window 160, the user can observe the waste gas (water smoke) processing condition in swirl barrel 200 and spray room 110 through observation window 160, and the user of help in time knows the actual condition that the clean condition of waste gas and swirl barrel 200 and filtration were solved, further improves user's use experience degree.

Referring to fig. 4, it can be understood that an overflow groove 350 is installed between the funnel 300 and the water tank 320, the outlet 220 of the funnel 300 is received in the overflow groove 350, an overflow hole 351 is provided at a side of the overflow groove 350 facing the water tank 320, and the overflow hole 351 is communicated with the water tank 320. The outlet 220 of the funnel 300 is arranged in the overflow tank 350, the liquid under the funnel 300 slowly flows into the overflow tank 350 and dynamically seals the outlet 220 of the funnel 300, the tightness of the funnel 300 is effectively improved (a baffle is usually arranged at the outer side of the cyclone barrel 200 to seal the top end opening of the funnel 300), the leakage of waste gas entering from the air inlet 310 is avoided, the loss of an external waste gas blower (not shown in the figure) is reduced, in addition, when the liquid is higher than the ground of the overflow tank 351 in the overflow tank 350, the liquid flows towards the water tank 320, and the bottom of the overflow tank 350 is filled upwards when the liquid is in the liquid, so that the splashing phenomenon of the liquid can be reduced, the waste of the liquid in the water tank 320 is reduced, and the pollution of the splashed liquid to the environment is avoided.

Further, a filter screen 360 is installed between the overflow tank 350 and the water tank 320, the overflow tank 350 is provided with a guide plate 352, the guide plate 352 is positioned between the overflow 351 and the filter screen 360, and a section of the guide plate 352 adjacent to the overflow 351 is inclined downward. In general, the liquid flowing into the water tank 320 from the overflow tank 350 contains dust particles, which are generally precipitated in the water tank 320 under the action of gravity, but are still likely to be absorbed by the water pump 330 and enter the circulating pipe 340, and by providing the guide plate 352 and the filter screen 360, the guide plate 352 can guide the liquid containing dust particles to quickly flow to the filter screen 360, so that the operation smoothness of the basin is further improved, the filter screen 360 filters the liquid containing dust particles once before the liquid containing dust particles enters the water tank 320, thereby reducing the impurity of the liquid in the water tank 320, effectively improving the purity of the liquid in the circulating pipe 340, and further enhancing the exhaust gas purifying effect of the spray tower.

An exhaust treatment line according to an embodiment of the second aspect of the present utility model includes a cyclone spray tower of the above-described embodiments.

While the preferred embodiment of the present utility model has been described in detail, the present utility model is not limited to the above embodiments, and those skilled in the art can make various equivalent modifications or substitutions without departing from the spirit of the present utility model, and these equivalent modifications or substitutions are included in the scope of the present utility model as defined in the appended claims.

Claims (10)

1. A cyclone spray tower, comprising:

the tower body is provided with a spray chamber, the spray chamber is provided with a filter ball and a plurality of heating pipes, the heating pipes are positioned below the filter ball, and the plurality of heating pipes are arranged at intervals along the circumferential direction of the spray chamber and form a heating zone;

the cyclone barrel is arranged below the spray chamber and is provided with an inlet and an outlet, and the outlet is communicated with the heating area;

the funnel is installed in whirl bucket below, one side of funnel is equipped with the air intake, the air intake with the entry intercommunication, the bottom of funnel is connected with the water tank, the water pump is installed to the water tank, the water pump is connected with circulating line, circulating line's one end with the water tank intercommunication, the other end is located spray room top, circulating line's delivery port orientation spray room setting.

2. The cyclone spray tower as claimed in claim 1, wherein the cyclone barrels are provided in plurality, and inlets of the cyclone barrels are disposed toward the same side and are communicated with the air inlet.

3. The cyclone spray tower of claim 2, wherein the spray chamber is provided with a protective cover, and the protective cover is covered on the heating pipe.

4. A cyclone spray tower according to claim 2 or 3, wherein the tower body is provided with a pressure detector, the pressure detector is electrically connected with the heating pipe, and the detection end of the pressure detector is arranged towards the heating area.

5. The cyclone spray tower as claimed in claim 1, wherein an overflow tank is installed between the funnel and the water tank, an outlet of the funnel is accommodated in the overflow tank, an overflow port is provided at a side of the overflow tank facing the water tank, and the overflow port is communicated with the water tank.

6. The cyclone spray tower as claimed in claim 5, wherein a filter screen is installed between the overflow tank and the water tank, the overflow tank is provided with a guide plate, the guide plate is positioned between the overflow port and the filter screen, and the guide plate is disposed adjacent to a section of the overflow port in a downward inclined manner.

7. The cyclone spray tower of claim 1, wherein the spray chamber is connected with a hollowed-out drawer, the hollowed-out drawer is in sliding fit with the spray chamber, and the filter ball is mounted on the hollowed-out drawer.

8. The cyclone spray tower of claim 7, wherein a plurality of the hollowed-out drawers are provided, and a plurality of the hollowed-out drawers are arranged at intervals along the vertical direction.

9. The cyclone spray tower of claim 1, wherein the cyclone barrel and the spray chamber are provided with viewing windows on the same side.

10. An exhaust gas treatment line comprising a cyclonic spray tower as claimed in any one of claims 1 to 9.

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