CN206391836U - A kind of ammonification tail gas absorption adsorption tower - Google Patents
A kind of ammonification tail gas absorption adsorption tower Download PDFInfo
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- CN206391836U CN206391836U CN201720057471.5U CN201720057471U CN206391836U CN 206391836 U CN206391836 U CN 206391836U CN 201720057471 U CN201720057471 U CN 201720057471U CN 206391836 U CN206391836 U CN 206391836U
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- tail gas
- ammonification
- absorption tower
- tower shell
- sprinkler head
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Abstract
The utility model discloses a kind of ammonification tail gas absorption adsorption tower, including absorption tower shell, the side of the absorption tower shell is fixed with control panel and ammonification tail gas air inlet pipe, and being internally embedded for ammonification tail gas air inlet pipe is provided with screen pack, the top of the absorption tower shell offers gas outlet, and the surface of absorption tower shell is provided with observation window, the inside of the absorption tower shell is fixed with the first sprinkler head successively from top to bottom, first packing layer, second sprinkler head, second packing layer and water tank, and the inside of water tank is provided with heat exchanger tube and PH meters, the side of the water tank through absorption tower shell is provided with water inlet and liquid outlet, and being internally embedded for liquid outlet is provided with electromagnetic valve.The utility model water circulating pump, the second sprinkler head and the first sprinkler head are used cooperatively, and can be further ensured that ammonification tail gas by complete adsorption treatment, the heat produced when handling tail gas can be carried out heat exchange processing, can more preferably absorb tail gas by heat exchanger tube.
Description
Technical field
The utility model is related to technical field of chemical, specially a kind of ammonification tail gas absorption adsorption tower.
Background technology
Ammonification tail gas mainly has an ammonia, and ammonia, NH3, colourless gas, there is strong impulse smell.Density 0.7710, phase
To density 0.5971, colourless liquid is easily liquefied as, water, ethanol and ether is dissolved in, nitrogen and hydrogen can be resolved into high temperature
Gas, there is reduction.Nitric oxide can be oxidized in the presence of catalyst by having, for liquid nitrogen processed, ammoniacal liquor, nitric acid, ammonium salt and amine
Class etc., can directly be synthesized and be made by nitrogen and hydrogen, and energy skin ambustion, eyes, the mucous membrane of respiratory apparatus, people's suction are excessive, can draw
Lung swelling is played, so that it is dead therefore particularly important for the processing of ammonification tail gas, in production methyl carbamate and amino first
During acetoacetic ester, ammonification tail gas can be usually produced, if these ammonification tail gas are discharged into atmospheric environment without processing, meeting
Cause serious pollution to environment, destroy ecological environment, however at present for ammonification tail gas processing be by adsorption tower, it is but existing
Some ammonification tail gas absorption adsorption towers are not in use using saving, waste of resource, and assimilation effect is bad, and at place
Meeting amount of heat when managing ammonification tail gas, is unfavorable for absorbing tail gas, so as to be not easy to and promote the use of.
Utility model content
The purpose of this utility model is to provide a kind of ammonification tail gas absorption adsorption tower, to solve to carry in above-mentioned background technology
The problem of going out, is had an advantageous effect in that：Water circulating pump, the second sprinkler head and the first sprinkler head are used cooperatively, Neng Goujin
One step ensures that ammonification tail gas, by complete adsorption treatment, using reliable, economizes on resources, what heat exchanger tube was produced when can be by processing tail gas
Heat carries out heat exchange processing, can more preferably absorb tail gas.
To achieve the above object, the utility model provides following technical scheme：A kind of ammonification tail gas absorption adsorption tower, including
Tower shell is adsorbed, the side of the absorption tower shell is fixed with control panel and ammonification tail gas air inlet pipe, and ammonification tail gas air inlet
Being internally embedded for pipe is provided with screen pack, and the top of the absorption tower shell offers gas outlet, and the surface of absorption tower shell
Observation window is provided with, the inside of the absorption tower shell is fixed with the first sprinkler head, the first packing layer, second successively from top to bottom
Sprinkler head, the second packing layer and water tank, and the inside of water tank is provided with heat exchanger tube and PH meters, the water tank passes through absorption tower shell
Side be provided with water inlet and liquid outlet, and being internally embedded for liquid outlet is provided with electromagnetic valve, the absorption tower casing
The opposite side of body is fixed with water circulating pump, and water circulating pump is connected with the first sprinkler head and the second sprinkler head respectively by delivery pipe
Connect.
It is preferred that, the control panel is located at the top of ammonification tail gas air inlet pipe.
It is preferred that, it is fixed with support base below the absorption tower shell.
It is preferred that, the liquid outlet is located at the lower section of water inlet.
It is preferred that, the heat exchanger tube is made up of stainless steel material component.
Compared with prior art, the beneficial effects of the utility model are：The utility model is reasonable in design, compact conformation, follows
Ring water pump, the second sprinkler head and the first sprinkler head are used cooperatively, and can be further ensured that ammonification tail gas by complete adsorption treatment,
Using reliable, and economize on resources, the screen pack set in ammonification tail gas air inlet pipe can be by the dust granule in ammonification tail gas
Filter out, and by the heat exchanger tube of setting, the heat produced when handling tail gas can be subjected to heat exchange processing, can be more preferable
Tail gas is absorbed, so as to not interfere with the effect of adsorption treatment, and then effect of adsorption tower is effectively increased, therefore, is easy to promote
Use.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is sectional view of the present utility model.
In figure：1- gas outlets；2- adsorbs tower shell；3- observation windows；4- support bases；5- ammonification tail gas air inlet pipe；6- mistakes
Filter screen；7- control panels；8-PH is counted；9- water inlets；10- electromagnetic valves；11- liquid outlets；12- water circulating pumps；13- is conveyed
Pipe；14- heat exchanger tubes；The packing layers of 15- second；The packing layers of 16- first；The sprinkler heads of 17- second；The sprinkler heads of 18- first；19- water tanks.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belongs to the scope of the utility model protection.
Refer to Fig. 1 and Fig. 2, a kind of embodiment that the utility model is provided：A kind of ammonification tail gas absorption adsorption tower, including
Tower shell 2 is adsorbed, the side of absorption tower shell 2 is fixed with control panel 7 and ammonification tail gas air inlet pipe 5, and ammonification tail gas air inlet
Being internally embedded for pipe 5 is provided with screen pack 6, and the top of absorption tower shell 2 offers gas outlet 1, and the surface of absorption tower shell 2
It is provided with observation window 3, the inside of absorption tower shell 2 is fixed with the first sprinkler head 18, the first packing layer 16, the successively from top to bottom
Two sprinkler heads 17, the second packing layer 15 and water tank 19, and the inside of water tank 19 is provided with heat exchanger tube 14 and PH meters 8, water tank 19 is worn
The side for crossing absorption tower shell 2 is provided with water inlet 9 and liquid outlet 11, and being internally embedded for liquid outlet 11 is provided with electromagnetism
Valve 10, the opposite side of absorption tower shell 2 is fixed with water circulating pump 12, and water circulating pump 12 by delivery pipe 13 respectively with first
The sprinkler head 17 of sprinkler head 18 and second is connected.
Control panel 7 is located at the top of ammonification tail gas air inlet pipe 5；The lower section of absorption tower shell 2 is fixed with support base 4；
Liquid outlet 11 is located at the lower section of water inlet 9；Heat exchanger tube 14 is made up of stainless steel material component.
Operation principle：Before use, ammonification tail gas air inlet pipe 5, water inlet 9, liquid outlet 11 and heat exchanger tube 14 are connected successively
Connect, open tap, water is flowed in water tank 19 from water inlet 9, in use, ammonification tail gas is entered by ammonification tail gas air inlet pipe 5
Enter into absorption tower shell 2, tail gas is first handled by the water absorption in water tank 19, opens the switch on control panel 7, water circulating pump
Water in 12 pumping boxes 19 is transported to by delivery pipe 13 in second sprinkler head 17 and the first sprinkler head 18, not absorbed
Tail gas sequentially passes through the second packing layer 15 and the first packing layer 16 is handled, then successively by the second sprinkler head 17 and the first sprinkler head 18
The water absorption processing sprayed out, gas clean afterwards is discharged from gas outlet 1, and the water in water tank 19 can be produced when absorbing tail gas
Substantial amounts of heat, is exchanged heat by heat exchanger tube 14, so as to ensure that ammonification vent gas treatment is not affected by temperature, and then use can
Lean on.
It is obvious to a person skilled in the art that the utility model is not limited to the details of above-mentioned one exemplary embodiment, and
And in the case of without departing substantially from spirit or essential attributes of the present utility model, can realize that this practicality is new in other specific forms
Type.Therefore, no matter from the point of view of which point, embodiment all should be regarded as exemplary, and is nonrestrictive, this practicality is new
The scope of type limits by appended claims rather than described above, it is intended that the equivalency fallen in claim is contained
All changes in justice and scope are included in the utility model.Any reference in claim should not be considered as limitation
Involved claim.
Claims (5)
1. a kind of ammonification tail gas absorption adsorption tower, including absorption tower shell (2), it is characterised in that：The absorption tower shell (2)
Side is fixed with control panel (7) and ammonification tail gas air inlet pipe (5), and being internally embedded for ammonification tail gas air inlet pipe (5) is provided with
Screen pack (6), the top of the absorption tower shell (2) offers gas outlet (1), and the surface of absorption tower shell (2) is provided with
Observation window (3), the inside of the absorption tower shell (2) is fixed with the first sprinkler head (18), the first packing layer successively from top to bottom
(16), the second sprinkler head (17), the second packing layer (15) and water tank (19), and the inside of water tank (19) is provided with heat exchanger tube (14)
(8) are counted with PH, the water tank (19) is provided with water inlet (9) and liquid outlet (11) through the side of absorption tower shell (2), and
Being internally embedded for liquid outlet (11) is provided with electromagnetic valve (10), and the opposite side of the absorption tower shell (2) is fixed with circulation
Water pump (12), and water circulating pump (12) by delivery pipe (13) respectively with the first sprinkler head (18) and the second sprinkler head (17) even
Connect.
2. a kind of ammonification tail gas absorption adsorption tower according to claim 1, it is characterised in that：Control panel (7) position
In the top of ammonification tail gas air inlet pipe (5).
3. a kind of ammonification tail gas absorption adsorption tower according to claim 1, it is characterised in that：The absorption tower shell (2)
Lower section be fixed with support base (4).
4. a kind of ammonification tail gas absorption adsorption tower according to claim 1, it is characterised in that：Liquid outlet (11) position
Lower section in water inlet (9).
5. a kind of ammonification tail gas absorption adsorption tower according to claim 1, it is characterised in that：The heat exchanger tube (14) be by
Stainless steel material component is made.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720057471.5U CN206391836U (en) | 2017-01-17 | 2017-01-17 | A kind of ammonification tail gas absorption adsorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720057471.5U CN206391836U (en) | 2017-01-17 | 2017-01-17 | A kind of ammonification tail gas absorption adsorption tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206391836U true CN206391836U (en) | 2017-08-11 |
Family
ID=59518410
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720057471.5U Active CN206391836U (en) | 2017-01-17 | 2017-01-17 | A kind of ammonification tail gas absorption adsorption tower |
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| Country | Link |
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| CN (1) | CN206391836U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854296A (en) * | 2018-07-12 | 2018-11-23 | 云南文山铝业有限公司 | Ammonia absorbs the method with purification in a kind of aluminium ash treatment process |
| CN110559828A (en) * | 2019-09-06 | 2019-12-13 | 天津大学 | Small tail gas absorption and deodorization device for sludge composting tail gas treatment |
-
2017
- 2017-01-17 CN CN201720057471.5U patent/CN206391836U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854296A (en) * | 2018-07-12 | 2018-11-23 | 云南文山铝业有限公司 | Ammonia absorbs the method with purification in a kind of aluminium ash treatment process |
| CN110559828A (en) * | 2019-09-06 | 2019-12-13 | 天津大学 | Small tail gas absorption and deodorization device for sludge composting tail gas treatment |
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