CN213467230U - Spray tower - Google Patents
Spray tower Download PDFInfo
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- CN213467230U CN213467230U CN202021935206.0U CN202021935206U CN213467230U CN 213467230 U CN213467230 U CN 213467230U CN 202021935206 U CN202021935206 U CN 202021935206U CN 213467230 U CN213467230 U CN 213467230U
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Abstract
The utility model relates to a spray tower, including the cylindrical tower body that has the air inlet, gas outlet, level setting whirl device, spray set and the white defogging device of taking off in the tower body, the air current flows through whirl device, spray set, takes off white defogging device outflow gas outlet from the air inlet in proper order, and the air inlet is provided with a plurality ofly, and a plurality of air inlets set up at the same height of tower body, and the air inlet is connected with the intake pipe, and the direction of admission of intake pipe is tangent with the outer peripheral face of tower body. The utility model discloses each air inlet pipe direction all is tangent with the tower body circumference for the waste gas that gets into the spray column forms the mobile mode of many angular points circle of contact, thereby lets air inlet process loss of pressure very little, and flow distribution on the tower body internal cross-section is even, helps eliminating and sprays the dead angle, simultaneously effectually weakens the wall flow effect under the effect of centrifugal wind, has improved the mass transfer and the heat transfer effect of spray column, and the amount of wind is big more, and the effect is more obvious.
Description
Technical Field
The utility model relates to a chemical industry, environmental protection field especially relate to a spray column.
Background
The spray tower is also called a water washing tower or a washing tower, is one of the common purification devices for treating pollutants such as waste gas, dust and the like in the chemical industry and the environmental protection industry, and has the advantages of simple process, high purification efficiency, low operation cost, convenient installation and the like.
The operating principle of the spray tower is that the gas containing impurities is contacted with the liquid medicine containing the absorbent in the tower, so that the pollutants in the gas are transferred into the liquid, and the purified gas is separated from the liquid, thereby achieving the purpose of purifying the waste gas. However, most of the existing spray towers have an air inlet, and waste gas enters the spray tower and then collides with the tower wall opposite to the inlet, so that great pressure loss is caused, and energy consumption of an air exhaust fan at the downstream of the spray tower is caused.
Disclosure of Invention
An object of the utility model is to provide a spray column, the exhaust gas pressure loss who only has the condition of an air intake to cause to common spray column on the current market is great, and waste gas gets into behind the spray column the problem that the inhomogeneous easy formation of flow distribution sprayed the dead angle on the tower body cross-section provides a novel air inlet mode.
In order to achieve the above purpose, the utility model adopts the technical scheme that:
the utility model provides a spray column, is in including cylindrical tower body, the level setting that has air inlet, gas outlet the tower body in whirl device, spray set and take off white defogging device, the air current follow the air inlet flow through in proper order whirl device, spray set, take off white defogging device and flow out the gas outlet, the air inlet be provided with a plurality ofly, a plurality of the air inlet setting be in the same height of tower body, the air inlet be connected with the intake pipe, the direction of admitting air of intake pipe with the outer peripheral face of tower body tangent.
Preferably, a plurality of air inlet pipes are uniformly distributed on the outer peripheral surface of the tower body.
Preferably, four air inlet pipes are arranged.
Preferably, the swirling device comprises an outer ring body, an inner ring body positioned at the inner side of the outer ring body, and a plurality of vanes connected between the outer ring body and the inner ring body, the axial lines of the outer ring body and the inner ring body are parallel, one ends of the vanes are connected to the inner circumferential surface of the outer ring body, the other ends of the vanes are connected to the outer circumferential surface of the inner ring body, an included angle of more than 0 degree and less than 90 degrees is formed between each vane and the cross section of the outer ring body and the cross section of the inner ring body, holes are formed in the vanes, and the direction of the holes is consistent with the extending direction of the axial lines of the outer ring body and the inner ring body.
Further preferably, the holes are louver holes.
Further preferably, the width of the blade gradually increases from one end to the other end thereof.
Further preferably, the holes are provided with a plurality of groups, and the plurality of groups of holes are distributed along the length direction of the blade.
Still further preferably, the number of holes in each set increases from one end of the blade to the other.
Further preferably, the included angle between the vanes and the cross section of the outer ring body and the inner ring body is 30-60 degrees.
Further preferably, a gap is formed between the projections of the adjacent two vanes on the cross sections of the outer ring body and the inner ring body.
More preferably, the axial lines of the outer ring body and the inner ring body are overlapped.
Preferably, the de-whitening and de-fogging device comprises a plurality of corrugated plates, the corrugated plates are uniformly distributed in the extending direction, an airflow channel is formed between every two adjacent corrugated plates, and the width of the airflow channel is kept unchanged from one end to the other end of the airflow channel.
Further preferably, all of said air flow channels are equal in width.
Further preferably, the width of the air flow channel is 30-50 mm.
Further preferably, said corrugated sheet has only one complete corrugation unit.
Further preferably, the cross section of the device perpendicular to the extending direction of the corrugated plate is circular.
Preferably, the spray tower further comprises a cold source air external air box communicated with the interior of the tower body and used for providing cold source air for the de-whitening and de-fogging device.
Preferably, the tower body be provided with a plurality of access holes along its direction of height, the access hole on be provided with transparent PVC board.
Preferably, the air inlet, the rotational flow device, the spraying device, the white and mist removing device and the air outlet are sequentially arranged from bottom to top.
Because of the application of the technical scheme, compared with the prior art, the utility model has the following advantages:
the utility model overcomes air inlet waste gas loss of pressure great and waste gas get into the spray column after the uneven easy formation of flow distribution in tower body cross-section sprays the problem at dead angle, each intake pipe direction all is tangent with the tower body circumference, make the waste gas that gets into the spray column form the flow mode of many corner cut circles, thereby let air inlet process loss of pressure very little, and flow distribution is even on the tower body internal cross-section, help eliminating and spray the dead angle, simultaneously the effectual wall flow effect that weakens under centrifugal wind's effect, the mass transfer and the heat transfer effect of spray column have been improved, and the amount of wind is big more, the effect is more obvious.
Drawings
FIG. 1 is a schematic perspective view of a spray tower according to the present embodiment;
FIG. 2 is a schematic top view of the spray tower of the present embodiment;
FIG. 3 is a schematic view of the interior of the spray tower in this embodiment;
FIG. 4 is a perspective view of the vortex apparatus of the present embodiment;
FIG. 5 is a schematic front view of the cyclone apparatus of the present embodiment;
FIG. 6 is a schematic view of a vane of the swirling device of the present embodiment;
FIG. 7 is a schematic perspective view of the white and mist removing device in this embodiment;
fig. 8 is a schematic front view of the white and mist removing device in this embodiment.
In the above drawings:
1. a tower body; 10. an air inlet; 11. an air outlet; 12. an air inlet pipe; 20. an outer ring body; 21. an inner ring body; 22. a blade; 220. an aperture; 30. a shower pipe; 31. a water tank; 4. a corrugated plate; 40. an air flow channel; 5. the cold source air is externally connected with an air box; 6. and (6) overhauling holes.
Detailed Description
The technical solution of the present invention will be described clearly and completely with reference to the accompanying drawings, and obviously, the described embodiments are some, but not all embodiments of the present invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
A spray tower as shown in fig. 1-3, including cylindrical tower body 1 with air inlet 10, gas outlet 11, the whirl device of setting in tower body 1, spray set and take off white defogging device, air inlet 10, whirl device, spray set, take off white defogging device, gas outlet from the supreme setting gradually down for the air current flows through whirl device, spray set, takes off white defogging device outflow gas outlet 11 from air inlet 10 in proper order. Wherein:
the spray tower is formed by welding PP plastics. The air inlet 10 is provided with a plurality ofly, and a plurality of air inlets 10 set up the same height at tower body 1, and air inlet 10 is connected with intake pipe 12, and the direction of admitting air of intake pipe 12 is tangent with the outer peripheral face of tower body 1. The number of the illustrated air inlet pipes 12 is four, and the four air inlet pipes 12 are uniformly distributed on the outer circumferential surface of the tower body 1, that is, the included angle between the normal directions of the adjacent air inlet pipes 12 is 90 degrees, as shown in fig. 1 and 2.
The air inlet mode enables the waste gas entering the tower body 1 to form a flow mode with four tangential corners, so that the pressure loss in the air inlet process is very small, the flow distribution on the inner cross section of the tower body 1 is uniform, the spraying dead angle is eliminated, meanwhile, the wall flow effect is effectively weakened under the action of centrifugal air, and the mass transfer and heat transfer effects of the spraying tower are improved.
Example 1 a:
adopt PP material (polypropylene) to make spray column material object according to this embodiment to examine filler absorption effect and pressure drop condition in flue gas denitration experiment, specific content is as follows:
50000m3Air volume/h NO2The content is 1500mg/m3The flue gas is used as a test medium, and outlet NO is measured after the flue gas is washed and purified by a spray tower2The content was 47mg/m3, and the inlet and outlet pressure drop values were found to be 1135 Pa.
Example 1 b:
adopt PP material (polypropylene) to make spray column material object according to this embodiment to examine filler absorption effect and pressure drop condition in flue gas denitration experiment, specific content is as follows:
will 80000m3Air volume/h NO2The content is 2000mg/m3The flue gas is used as a test medium, and outlet NO is measured after the flue gas is washed and purified by a spray tower2The content was 52mg/m3, and the inlet and outlet pressure drop values were 1671 Pa.
Comparative example 1 a:
adopt PP material (polypropylene) to make spray column material object according to conventional air inlet mode to examine filler absorption effect and pressure drop condition in flue gas denitration experiment, specific content is as follows:
50000m3Air volume/h NO2The content is 1500mg/m3The flue gas is used as a test medium, and outlet NO is measured after the flue gas is washed and purified by a spray tower2The content is 74mg/m3The inlet and outlet pressure drop values were measured to be 1446 Pa.
Comparative example 1 b:
adopt PP material (polypropylene) to make spray column material object according to conventional air inlet mode to examine filler absorption effect and pressure drop condition in flue gas denitration experiment, specific content is as follows:
will 80000m3Air volume/h NO2The content is 2000mg/m3The flue gas is used as a test medium, and outlet NO is measured after the flue gas is washed and purified by a spray tower2The content is 113mg/m3The inlet and outlet pressure drop values were found to be 1946 Pa.
As shown in fig. 4-6: the swirling device comprises an outer ring body 20, an inner ring body 21 positioned inside the outer ring body 20, and a plurality of vanes 22 connected between the outer ring body 20 and the inner ring body 21, wherein the axial lines of the outer ring body 20 and the inner ring body 21 are overlapped, namely, the vanes are coaxially arranged, one ends of the vanes 22 are connected to the inner circumferential surface of the outer ring body 20, and the other ends of the vanes 22 are connected to the outer circumferential surface of the inner ring body 21. The rotational flow device is formed by cutting and welding PP materials. Specifically, the method comprises the following steps:
the width of the vanes 22 gradually increases from one end to the other end, the included angle between each vane 22 and the cross section of the outer ring body 20 and the cross section of the inner ring body 21 is 30-60 degrees, and a gap is formed between the projections of two adjacent vanes 22 on the cross section of the outer ring body 20 and the cross section of the inner ring body 21. The vanes 22 are provided with holes 220, the holes 220 in this embodiment are louver holes, and the direction of the holes 220 is the same as the extending direction of the axial lines of the outer ring body 20 and the inner ring body 21, i.e. the holes are vertically provided. The holes 220 are provided in a plurality of sets, the holes 220 are distributed along the length direction of the blade 22, the number of the holes 220 in each set is gradually increased from one end of the blade 22 to the other end, 3 sets are provided as shown in the figure, and the number of the holes is three, four, or five sets in sequence.
The incoming gas flow enters the tower body 1 from the gas inlet 10 and then rises in the direction perpendicular to the cross section of the tower body 1, the incoming gas flows through the cyclone device and then is redistributed, and partial gas vertically rises through the holes 220 on the blades 22 in the cyclone process, so that the problems of high pressure loss and high power consumption of a fan after the gas flows through the cyclone device are effectively solved, meanwhile, the convolution effect caused by the fact that the gas flows through the cyclone plate can be effectively improved, and the gas is distributed more uniformly in the tower.
Example 2:
the inner ring body 21 of the rotational flow device manufactured and molded in the embodiment is welded on the support column in the tower body 1, the outer ring body 20 is welded on the wall of the tower body 1, the manufactured spray tower is put into operation, the pressure loss in the nitrogen oxide waste gas treatment process is detected, and the pressure drop of the gas inlet and the gas outlet of the spray tower is 1215Pa after the operation is stable. The calculated denitration efficiency was 99%.
Comparative example 2:
the spray tower which is provided with the common rotational flow plate and has the same size as the spray tower in the embodiment is put into operation, the pressure loss condition in the nitrogen oxide waste gas treatment process is detected, and the pressure drop of the gas inlet and the gas outlet of the spray tower is 1569Pa after the operation is stable. The calculated denitration efficiency was 90%.
The spraying device comprises a spraying pipe 30 with a nozzle, the spraying pipe 30 is arranged in the tower body 1, and a plurality of groups of spraying pipes 30 can be arranged along the height direction of the tower body 1. The spray pipe 30 has a water tank 31 for supplying spray liquid thereto, and the water tank 31 is provided with a liquid inlet and an overflow outlet of a water pump, as shown in fig. 3.
As shown in fig. 7 and 8: the whitening and defogging device comprises a plurality of corrugated plates 4, wherein the corrugated plates 4 are uniformly distributed in the extending direction, an airflow channel 40 is formed between every two adjacent corrugated plates 4, the width of the airflow channel 40 is kept unchanged from one end to the other end of the airflow channel, and the width of all the airflow channels 40 is 30-50 mm. The corrugated plate 4 shown has only one complete corrugation unit, a sine wave shape, and the cross-section of the device perpendicular to the extension of the corrugated plate 4 is circular. The white and mist removing device is formed by cutting and welding a PP material.
The spray tower also comprises a cold source air external air box 5 which is communicated with the interior of the tower body 1 and provides cold source air for the de-whitening and demisting device.
High-temperature gas comes to flow through and sprays washing back and carry a large amount of wet steam to flow in and take off white defogging device, the cold source air that the external bellows 5 of cold source air provided and waste gas are at the flow mode that adjacent airflow channel 40 cross flow was arranged, waste gas is cooled off after the heat exchange, obtains effectively cooling, the wet steam in the waste gas condenses into a large amount of liquid drops, in colliding 4 walls of buckled plate fall back to the spray column, the clean air outflow after being cooled takes off white defogging device upwards and is taken out the spray column by the air exhauster.
Example 3:
install the white defogging device of taking off of preparation shaping this embodiment in the spray column, utilize this defroster defogging of flue gas wet flue gas desulfurization technology inspection and take off white effect, detect tail gas humidity in tail gas outlet department, the result shows that tail gas outlet waste gas relative humidity is 12%, and the chimney exit does not have white smog.
Comparative example 3:
in the spray tower that will install ordinary defroster equipment, utilize flue gas wet flue gas desulfurization technology to inspect this defroster defogging and take off white effect, detect tail gas relative humidity in the tail gas export, the result shows that tail gas export waste gas relative humidity is 65%, and there is white smog to generate in the chimney outlet.
In addition, tower body 1 is provided with a plurality of access holes 6 along its direction of height, is provided with transparent PVC board on the access hole 6, and every group shower 30 below of picture shows all sets up an access hole 6.
The above embodiments are only for illustrating the technical concept and features of the present invention, and the purpose of the embodiments is to enable people skilled in the art to understand the contents of the present invention and to implement the present invention, which cannot limit the protection scope of the present invention. All equivalent changes and modifications made according to the spirit of the present invention should be covered by the protection scope of the present invention.
Claims (10)
1. The utility model provides a spray column, is in including cylindrical tower body, the level setting that has air inlet, gas outlet the tower body in whirl device, spray set and take off white defogging device, the air current follow the air inlet flow through in proper order whirl device, spray set, take off white defogging device and flow out the gas outlet, its characterized in that: the air inlet be provided with a plurality ofly, a plurality ofly the air inlet set up the same height of tower body, the air inlet be connected with the intake pipe, the direction of admitting air of intake pipe with the outer peripheral face of tower body tangent.
2. The spray tower of claim 1, wherein: the plurality of air inlet pipes are uniformly distributed on the outer peripheral surface of the tower body.
3. The spray tower of claim 1 or 2, wherein: the number of the air inlet pipes is four.
4. The spray tower of claim 1, wherein: the rotational flow device comprises an outer ring body, an inner ring body positioned on the inner side of the outer ring body, and a plurality of vanes connected between the outer ring body and the inner ring body, wherein the axial leads of the outer ring body and the inner ring body are parallel, one ends of the vanes are connected to the inner circumferential surface of the outer ring body, the other ends of the vanes are connected to the outer circumferential surface of the inner ring body, the included angle between the vanes and the cross sections of the outer ring body and the inner ring body is 30-60 degrees, holes are formed in the vanes, and the direction of the holes is consistent with the extending direction of the axial leads of the outer ring body and the inner ring body.
5. The spray tower of claim 4, wherein: the holes are louver holes.
6. The spray tower of claim 4, wherein: the width of the blade is gradually increased from one end to the other end of the blade; the holes are provided with a plurality of groups, the holes are distributed along the length direction of the blade, and the number of the holes in each group is gradually increased from one end of the blade to the other end of the blade.
7. The spray tower of claim 4, wherein: and gaps are reserved between the projections of the adjacent two blades on the cross sections of the outer ring body and the inner ring body.
8. The spray tower of claim 1, wherein: the white defogging device that takes off include the polylith buckled plate, the polylith the unanimous distribution of buckled plate extending direction, adjacent two the buckled plate between form airflow channel, just airflow channel's width keep unchangeable from its one end to the other end.
9. The spray tower of claim 8, wherein: the width of the airflow channel is 30-50 mm.
10. The spray tower of claim 1, wherein: the tower body extend its direction of height and be provided with a plurality of access holes, the access hole on be provided with transparent PVC board.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021935206.0U CN213467230U (en) | 2020-09-07 | 2020-09-07 | Spray tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021935206.0U CN213467230U (en) | 2020-09-07 | 2020-09-07 | Spray tower |
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| Publication Number | Publication Date |
|---|---|
| CN213467230U true CN213467230U (en) | 2021-06-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021935206.0U Active CN213467230U (en) | 2020-09-07 | 2020-09-07 | Spray tower |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117983006A (en) * | 2024-03-21 | 2024-05-07 | 中铁二十三局集团第一工程有限公司 | High-pressure degradation device and degradation method for asphalt smoke |
-
2020
- 2020-09-07 CN CN202021935206.0U patent/CN213467230U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117983006A (en) * | 2024-03-21 | 2024-05-07 | 中铁二十三局集团第一工程有限公司 | High-pressure degradation device and degradation method for asphalt smoke |
| CN117983006B (en) * | 2024-03-21 | 2024-08-13 | 中铁二十三局集团第一工程有限公司 | High-pressure degradation device and degradation method for asphalt smoke |
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Address after: 215000 No. 58, Jinrui Road, Taiping Street, Xiangcheng District, Suzhou City, Jiangsu Province Patentee after: Suzhou Shijing Technology Co.,Ltd. Address before: 215137 4th floor, 82 Jincheng Road, Taiping Street, Xiangcheng District, Suzhou City, Jiangsu Province Patentee before: SUZHOU SHIJING ENVIRONMENTAL TECHNOLOGY Co.,Ltd. |