CN208553595U - A kind of new multistage adsorption tower - Google Patents
A kind of new multistage adsorption tower Download PDFInfo
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- CN208553595U CN208553595U CN201821128611.4U CN201821128611U CN208553595U CN 208553595 U CN208553595 U CN 208553595U CN 201821128611 U CN201821128611 U CN 201821128611U CN 208553595 U CN208553595 U CN 208553595U
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Abstract
The utility model discloses a kind of new multistage adsorption towers, including adsorption tower ontology, air inlet, liquid reserve tank, spraying layer, water pump, circulating water pipe, spray head, agitating device, packing layer, primary filter layer, in-depth filtration layer, activated carbon filter layer, exhaust pipe, steam trap, blower and chimney, the bottom end of the adsorption tower ontology is fixedly installed with liquid reserve tank, and is equipped with exhaust pipe at the top of adsorption tower ontology.The utility model is scientific and reasonable for structure, it is easy to operate, pass through liquid reserve tank and spraying layer, spray process can be carried out to gas, the solid particulate matter and impurity adhered in gas can be effectively removed, realize that preliminary purification handles work, the rotation of agitating paddle is driven using motor by agitating device, air-flow can be increased in the time of spray laminar flow, improve spraying effect, by primary filter layer, in-depth filtration layer and activated carbon filter layer, the multistage purification of adsorption tower is realized, effectively improve gas purification quality.
Description
Technical field
The utility model relates to adsorption tower technical field, specifically a kind of new multistage adsorption tower.
Background technique
Adsorption tower is also known as absorption tower, is the equipment for realizing absorption operation, for gas recycling or gas-liquid mixed, by liquid phase
Contact form is divided into three classes, and the first kind is plate column, bubble absorbing tower, the mixing drum of gas in the liquid phase with bubble shape dispersion
Steep absorption tower；Second class is injector, Venturi tube, the spray tower of liquid in the gas phase with droplet-like dispersion；Third class is liquid
The packed absorber and film-falling absorption tower that are contacted with gas phase are moved with membranaceous, the type of flow of gas-liquid two-phase can be inverse in tower
Stream can also cocurrent, generally use counter-current operation, absorbent is flowed from above to below with tower top addition, with the gas flowed from bottom to top
Contact, the liquid for absorbing absorbent are discharged from tower bottom, and purified gas is discharged from tower top, to realize the adsorption cleaning of gas
Effect.
Through retrieving, Chinese patent discloses a kind of adsorption tower (Authorization Notice No. CN202446968U), and the patented technology is logical
Gas is timely dissipated and is distributed by grid and bracing ring by the effect for crossing two layers of adsorbents, thus not will cause gap and
Packing layer displacement is generated, more serious abrasion and impact or even filler boiling effect is generated, leads to carrier performance decline or failure
Phenomenon, still, adsorption tower in the prior art not can be carried out the multi-stage absorption of gas, and clean-up effect is undesirable, and do not have and stir
Device is mixed, spraying effect is poor, while can not achieve the steam separation of gas, and the drop carried secretly in gas is easily to blower, pipeline
Corrosion is generated, service life of equipment is reduced.Therefore, those skilled in the art provide a kind of new multistage adsorption tower, to solve
The problems mentioned above in the background art.
Summary of the invention
It is mentioned above in the background art to solve the purpose of this utility model is to provide a kind of new multistage adsorption tower
Adsorption tower not can be carried out the multi-stage absorption of gas, and clean-up effect is undesirable, and not have agitating device, and spraying effect is poor, together
When can not achieve the steam separation of gas, the drop carried secretly in gas easily generates corrosion to blower, pipeline, reduces equipment and use the longevity
The problem of life.
To achieve the above object, the utility model provides the following technical solutions:
A kind of new multistage adsorption tower, including adsorption tower ontology, air inlet, liquid reserve tank, spraying layer, water pump, circulating water pipe,
Spray head, agitating device, packing layer, primary filter layer, in-depth filtration layer, activated carbon filter layer, exhaust pipe, steam trap, wind
Machine and chimney, the bottom end of the adsorption tower ontology is fixedly installed with liquid reserve tank, and is equipped with exhaust pipe at the top of adsorption tower ontology,
Spraying layer is provided with above the liquid reserve tank, and the side of liquid reserve tank is equipped with water pump, the side of the spraying layer is provided with
Air inlet, and primary filter layer is provided with above spraying layer, the bottom of the spraying layer are provided with packing layer, and spraying layer
It is internally provided with agitating device, the upper end of the water pump is equipped with circulating water pipe, and the bottom end of the circulating water pipe is located at spraying layer
Interior location at spray head is installed, the upper end of the primary filter layer is provided with in-depth filtration layer, the in-depth filtration layer
Upper end is provided with activated carbon filter layer, and the side of the exhaust pipe is equipped with steam trap, and the end of exhaust pipe is connected with
The top of blower, the blower is provided with chimney.
As a further solution of the present invention: the agitating device includes motor, shaft, bearing and agitating paddle,
One end of the agitating device is fixedly installed with motor, and one end of the motor is connected with shaft, and motor and shaft
Junction bearing is installed, be fixedly installed with agitating paddle on the outside of the shaft.
As a further solution of the present invention, the steam trap include entrance, gas vent, water absorption layer and
Condensation-water drain, one end insertion of the steam trap are provided with entrance, and the other end is provided with gas vent, the steam point
Inside from device is equipped with water absorption layer, and the bottom end of steam trap is provided with condensation-water drain.
The liquid reserve tank and spraying layer are penetrated through by circulating water pipe as a further solution of the present invention, connects,
The quantity of the spray head setting is no less than three.
The motor and shaft are rotatablely connected by bearing as a further solution of the present invention, described to stir
Paddle is mixed to be fixedly connected with shaft.
The primary filter layer is a kind of structure of HEPA filter screen material as a further solution of the present invention,
Part, the in-depth filtration layer are a kind of components of fiber glass filtering net material.
The primary filter layer, in-depth filtration layer and activated carbon filter layer as a further solution of the present invention,
Between be provided with gap.
The exhaust pipe and chimney are penetrated through by blower as a further solution of the present invention, connects.
Compared with prior art, the utility model has the beneficial effects that
1, the utility model can carry out spray process to gas, can effectively remove gas by liquid reserve tank and spraying layer
The solid particulate matter and impurity adhered in body realizes that preliminary purification handles work.
2, the utility model is driven the rotation of agitating paddle using motor, can be increased air-flow and sprayed by agitating device
The time of drenching layer flowing, improve spraying effect.
3, the utility model can effectively cross the nocuousness such as particle, PM2.5, the formaldehyde in air filtering by primary filter layer
Gas, and have certain water imbibition, the capturing ability of particle is stronger, and aperture is small, and adsorption capacity is big, purification efficiency
Height, by in-depth filtration layer can high-efficient filter except in gas solid particulate matter and bacterial virus, pass through activated carbon filter layer energy
The desulphurization and denitration effect for enough improving adsorption tower, realizes the multistage purification of adsorption tower, effectively improves gas purification quality.
4, the utility model can be realized the steam separation in air-flow, effectively removed in air-flow and pressed from both sides by steam trap
The drop of band prevents the harmful substance adsorbed in drop from corroding to generations such as Fan pipelines, overcomes traditional equipment corrosion-vulnerable
Phenomenon extends the service life of equipment.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of new multistage adsorption tower；
Fig. 2 is a kind of schematic diagram of internal structure of new multistage adsorption tower；
Fig. 3 is a kind of structural schematic diagram of agitating device in new multistage adsorption tower；
Fig. 4 is a kind of structural schematic diagram of steam trap in new multistage adsorption tower.
In figure: 1, adsorption tower ontology；2, air inlet；3, liquid reserve tank；4, spraying layer；5, water pump；6, circulating water pipe；7, it sprays
Head；8, agitating device；9, packing layer；10, primary filter layer；11, in-depth filtration layer；12, activated carbon filter layer；13, exhaust pipe；
14, steam trap；15, blower；16, chimney；17, motor；18, shaft；19, bearing；20, agitating paddle；21, entrance；22,
Gas vent；23, water absorption layer；24, condensation-water drain.
Specific embodiment
Please refer to Fig. 1~4, in the utility model embodiment, a kind of new multistage adsorption tower, including adsorption tower ontology 1, into
Port 2, liquid reserve tank 3, spraying layer 4, water pump 5, circulating water pipe 6, spray head 7, agitating device 8, packing layer 9, primary filter layer 10, depth
Layer filter layer 11, activated carbon filter layer 12, exhaust pipe 13, steam trap 14, blower 15 and chimney 16, adsorption tower ontology 1
Bottom end is fixedly installed with liquid reserve tank 3, and the top of adsorption tower ontology 1 is equipped with exhaust pipe 13, and the top of liquid reserve tank 3 is provided with spray
Drenching layer 4, and the side of liquid reserve tank 3 is equipped with water pump 5, the side of spraying layer 4 is provided with air inlet 2, and the top of spraying layer 4 is set
It is equipped with primary filter layer 10, the bottom of spraying layer 4 is provided with packing layer 9, and spraying layer 4 is internally provided with agitating device 8, water
The upper end of pump 5 is equipped with circulating water pipe 6, and the bottom end of circulating water pipe 6, which is located at the interior location of spraying layer 4, is equipped with spray head 7, just
The upper end of grade filter layer 10 is provided with in-depth filtration layer 11, and the upper end of in-depth filtration layer 11 is provided with activated carbon filter layer 12, row
The side of tracheae 13 is equipped with steam trap 14, and the end of exhaust pipe 13 is connected with blower 15, the top setting of blower 15
There is chimney 16.
In Fig. 3: agitating device 8 includes motor 17, shaft 18, bearing 19 and agitating paddle 20, one end of agitating device 8
It is fixedly installed with motor 17, one end of motor 17 is connected with shaft 18, and the junction of motor 17 and shaft 18 is installed
There is bearing 19, the outside of shaft 18 is fixedly installed with agitating paddle 20, in order to increase the contact area of gas Yu spraying layer 4.
In Fig. 4: steam trap 14 includes entrance 21, gas vent 22, water absorption layer 23 and condensation-water drain 24, steam
One end insertion of separator 14 is provided with entrance 21, and the other end is provided with gas vent 22, the inside installation of steam trap 14
There is water absorption layer 23, and the bottom end of steam trap 14 is provided with condensation-water drain 24, in order to realize the steam separation of air-flow.
In Fig. 2: liquid reserve tank 3 and spraying layer 4 are connected by the perforation of circulating water pipe 6, and the quantity that spray head 7 is arranged is no less than three
It is a, in order to realize that spray cleaning works.
In Fig. 3: motor 17 is rotatablely connected with shaft 18 by bearing 19, and agitating paddle 20 is fixedly connected with shaft 18,
In order to realize the rotation of agitating paddle 20, increase air flow property.
In Fig. 2: primary filter layer 10 is a kind of component of HEPA filter screen material, and in-depth filtration layer 11 is a kind of glass
The component of fibrous filter net material, in order to realize the multistage purification function of gas.
In Fig. 2: being provided with gap between primary filter layer 10, in-depth filtration layer 11 and activated carbon filter layer 12, be
Raising clean-up effect.
In Fig. 1: exhaust pipe 13 and chimney 16 are connected by the perforation of blower 15, in order to realize exhaust pipe 13 and chimney 16
Connection.
The working principle of the utility model is: firstly, gas will be stored up from the entrance spraying layer 4 of air inlet 2 by water pump 5
Liquid in liquid case 3 is pumped into spraying layer 4, can be carried out spray process to gas by spray head 7, can be effectively removed in gas
The solid particulate matter and impurity of attachment realize that preliminary purification handles work, and then, gas enters in primary filter layer 10, passes through
Primary filter layer 10 can effectively cross the pernicious gases such as particle, PM2.5, the formaldehyde in air filtering, and have certain water suction
Property, the capturing ability of particle is stronger, and aperture is small, and adsorption capacity is big, and purification efficiency is high, further, passes through deep layer mistake
Filtering layer 11 can high-efficient filter except in gas solid particulate matter and bacterial virus then can be mentioned by activated carbon filter layer 12
The desulphurization and denitration effect of high adsorption tower, realizes the multistage purification of adsorption tower, effectively improves gas purification quality, further,
Gas enters in exhaust pipe 13, can be realized the separation of the steam in air-flow by steam trap 14, effectively removes in air-flow and press from both sides
The drop of band prevents the harmful substance adsorbed in drop from corroding to generations such as blower 15 and pipelines, overcomes traditional equipment vulnerable to corruption
The phenomenon that erosion, extends the service life of equipment, finally, the gas after adsorption cleaning is discharged from chimney 16.
It is above-described, the only preferable specific embodiment of the utility model, but the protection scope of the utility model is simultaneously
It is not limited to this, anyone skilled in the art within the technical scope disclosed by the utility model, according to this reality
It is subject to equivalent substitution or change with novel technical solution and its utility model design, should all covers the protection in the utility model
Within the scope of.
Claims (8)
1. a kind of new multistage adsorption tower, including adsorption tower ontology (1), air inlet (2), liquid reserve tank (3), spraying layer (4), water pump
(5), circulating water pipe (6), spray head (7), agitating device (8), packing layer (9), primary filter layer (10), in-depth filtration layer (11),
Activated carbon filter layer (12), exhaust pipe (13), steam trap (14), blower (15) and chimney (16), which is characterized in that described
The bottom end of adsorption tower ontology (1) is fixedly installed with liquid reserve tank (3), and exhaust pipe (13) are equipped at the top of adsorption tower ontology (1),
It is provided with spraying layer (4) above the liquid reserve tank (3), and the side of liquid reserve tank (3) is equipped with water pump (5), the spraying layer
(4) side is provided with air inlet (2), and primary filter layer (10) are provided with above spraying layer (4), the spraying layer (4)
Bottom be provided with packing layer (9), and spraying layer (4) is internally provided with agitating device (8), the upper end peace of the water pump (5)
Equipped with circulating water pipe (6), the bottom end of the circulating water pipe (6), which is located at the interior location of spraying layer (4), is equipped with spray head (7),
The upper end of the primary filter layer (10) is provided with in-depth filtration layer (11), and the upper end of the in-depth filtration layer (11) is provided with work
Property charcoal filter layer (12), the side of the exhaust pipe (13) is equipped with steam trap (14), and the end of exhaust pipe (13) connects
It is connected to blower (15), the top of the blower (15) is provided with chimney (16).
2. a kind of new multistage adsorption tower according to claim 1, which is characterized in that the agitating device (8) includes electricity
One end of motivation (17), shaft (18), bearing (19) and agitating paddle (20), the agitating device (8) is fixedly installed with motor
(17), one end of the motor (17) is connected with shaft (18), and motor (17) and the junction of shaft (18) are equipped with
Bearing (19) is fixedly installed with agitating paddle (20) on the outside of the shaft (18).
3. a kind of new multistage adsorption tower according to claim 1, which is characterized in that the steam trap (14) includes
Entrance (21), gas vent (22), water absorption layer (23) and condensation-water drain (24), one end insertion of the steam trap (14)
It is provided with entrance (21), the other end is provided with gas vent (22), and the inside of the steam trap (14) is equipped with water absorption layer
(23), and the bottom end of steam trap (14) is provided with condensation-water drain (24).
4. a kind of new multistage adsorption tower according to claim 1, which is characterized in that the liquid reserve tank (3) and spraying layer
(4) by circulating water pipe (6) perforation connection, the quantity of spray head (7) setting is no less than three.
5. a kind of new multistage adsorption tower according to claim 2, which is characterized in that the motor (17) and shaft
(18) it is rotatablely connected by bearing (19), the agitating paddle (20) is fixedly connected with shaft (18).
6. a kind of new multistage adsorption tower according to claim 1, which is characterized in that the primary filter layer (10) is one
The component of kind HEPA filter screen material, the in-depth filtration layer (11) is a kind of component of fiber glass filtering net material.
7. a kind of new multistage adsorption tower according to claim 1, which is characterized in that the primary filter layer (10), depth
Gap is provided between layer filter layer (11) and activated carbon filter layer (12).
8. a kind of new multistage adsorption tower according to claim 1, which is characterized in that the exhaust pipe (13) and chimney
(16) pass through blower (15) perforation connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821128611.4U CN208553595U (en) | 2018-07-17 | 2018-07-17 | A kind of new multistage adsorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821128611.4U CN208553595U (en) | 2018-07-17 | 2018-07-17 | A kind of new multistage adsorption tower |
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| Publication Number | Publication Date |
|---|---|
| CN208553595U true CN208553595U (en) | 2019-03-01 |
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ID=65493549
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| Application Number | Title | Priority Date | Filing Date |
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| CN201821128611.4U Active CN208553595U (en) | 2018-07-17 | 2018-07-17 | A kind of new multistage adsorption tower |
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| CN (1) | CN208553595U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111672257A (en) * | 2020-07-01 | 2020-09-18 | 李柏青 | Dust type mixed waste gas environmental protection treatment facility |
| CN115430222A (en) * | 2022-09-05 | 2022-12-06 | 徐州燃烧控制研究院有限公司 | Dry-type fixed bed flue gas desulfurization and denitrification device with annular bin |
-
2018
- 2018-07-17 CN CN201821128611.4U patent/CN208553595U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111672257A (en) * | 2020-07-01 | 2020-09-18 | 李柏青 | Dust type mixed waste gas environmental protection treatment facility |
| CN111672257B (en) * | 2020-07-01 | 2021-11-16 | 宿迁启瑞环保科技股份有限公司 | Dust type mixed waste gas environmental protection treatment facility |
| CN115430222A (en) * | 2022-09-05 | 2022-12-06 | 徐州燃烧控制研究院有限公司 | Dry-type fixed bed flue gas desulfurization and denitrification device with annular bin |
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