CN207192961U - A kind of combined type ammonia nitrogen removal equipment - Google Patents
A kind of combined type ammonia nitrogen removal equipment Download PDFInfo
- Publication number
- CN207192961U CN207192961U CN201720785640.7U CN201720785640U CN207192961U CN 207192961 U CN207192961 U CN 207192961U CN 201720785640 U CN201720785640 U CN 201720785640U CN 207192961 U CN207192961 U CN 207192961U
- Authority
- CN
- China
- Prior art keywords
- ammonia
- chamber
- mixing
- combined type
- nitrogen removal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 title claims abstract description 19
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 86
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 43
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 39
- 238000002156 mixing Methods 0.000 claims abstract description 30
- 238000006243 chemical reaction Methods 0.000 claims abstract description 28
- 239000002912 waste gas Substances 0.000 claims abstract description 19
- 238000005086 pumping Methods 0.000 claims abstract description 17
- 239000010865 sewage Substances 0.000 claims abstract description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 14
- 238000012856 packing Methods 0.000 claims abstract description 9
- 238000001179 sorption measurement Methods 0.000 claims abstract description 8
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 7
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 5
- 239000000945 filler Substances 0.000 claims description 3
- 230000009615 deamination Effects 0.000 abstract description 7
- 238000006481 deamination reaction Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract description 3
- 239000006096 absorbing agent Substances 0.000 abstract description 2
- 238000010521 absorption reaction Methods 0.000 abstract description 2
- 239000013043 chemical agent Substances 0.000 abstract description 2
- 230000036632 reaction speed Effects 0.000 abstract description 2
- 238000005457 optimization Methods 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- 239000012535 impurity Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- CDQSJQSWAWPGKG-UHFFFAOYSA-N butane-1,1-diol Chemical compound CCCC(O)O CDQSJQSWAWPGKG-UHFFFAOYSA-N 0.000 description 1
- 229920003123 carboxymethyl cellulose sodium Polymers 0.000 description 1
- 229940063834 carboxymethylcellulose sodium Drugs 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses a kind of combined type ammonia nitrogen removal equipment, including shell, water inlet, filter chamber, screen pack, mixing and reaction chamber, motor, vertical mixing leaf, deflector, pumping blower fan, dividing plate, ammonia tourie, packing layer, waste gas outlet, water purifying chamber, activated carbon adsorption layer, cellulosic ultrafiltration film layer, delivery port, sewage draining exit and except ammonia agent tank.The utility model combined type ammonia nitrogen removal device structure is simple, novel in design, deamination purpose can be effectively achieved in sewage disposal, and can makes ammonia be recycled utilization；The vertical mixing leaf set in mixing and reaction chamber can accelerate the reaction speed of water and chemical agent, so as to reach the effect of quick deamination；Dividing plate can absorb the globule contained in waste gas, avoid influenceing the absorption of ammonia, ammonia absorber can effectively absorb the ammonia contained in waste gas, so that the ammonia in waste gas is recycled utilization, water purifying chamber can handle the sewage after hybrid reaction, make sewage that the process of after-treatment with qualified discharge, can be avoided.
Description
Technical field
A kind of water treatment facilities are the utility model is related to, specially a kind of combined type ammonia nitrogen removal equipment, are belonged at sewage
Manage technical field.
Background technology
Ammonia nitrogen waste water is mainly derived from chemical fertilizer, coking, petrochemical industry, pharmacy, food, refuse landfill etc., a large amount of ammonia nitrogen waste waters
It is discharged into water body not only to cause body eutrophication, cause black and odorous water, makes the difficulty and added cost of water process, or even to crowd
And biology produces toxic action, it is discharged into greatly not only polluted underground water but also crops is caused damage.
But the equipment for removing ammonia nitrogen in waste water at present is the most extensive with stripping tower utilization, although can reach the mesh of quick deamination
, but many imperfections parts also be present in other aspects, and the waste water after processing does not reach discharging standards, it is necessary to carry out secondary
Processing, and the waste gas blown out, without recovery value, causes secondary pollution, and obtain ammonia with the largely globule containing impurity
Less than reusing.Therefore, a kind of combined type ammonia nitrogen removal equipment is proposed regarding to the issue above.
Utility model content
The purpose of this utility model is that to solve the above problems and provides a kind of combined type ammonia nitrogen removal equipment.
The utility model is achieved through the following technical solutions above-mentioned purpose, a kind of combined type ammonia nitrogen removal equipment, including
Shell, mixing and reaction chamber and ammonia tourie, the side wall of outer shell are provided with water inlet, and water inlet connection filter chamber；The mistake
Screen pack, and connection mixing and reaction chamber of filter chamber are provided with inside filter chamber；The hybrid reaction chamber interior is provided with motor, and motor connects
Connect vertical mixing leaf；Deflector, and deflector connection pumping blower fan are provided with the top of the mixing and reaction chamber；The pumping blower fan top
Portion is provided with dividing plate；The pumping blower fan connection ammonia tourie, and it is provided with packing layer inside ammonia tourie；At the top of the ammonia tourie
Provided with waste gas outlet；The mixing and reaction chamber connects water purifying chamber, and water purifying chamber one end is provided with delivery port；The water purifying chamber bottom is set
There is sewage draining exit；Activated carbon adsorption layer is provided with inside the water purifying chamber, and activated carbon adsorption layer side is provided with cellulosic ultrafiltration film layer；Institute
State outer shell outer wall connection and remove ammonia agent tank.
Preferably, it is interconnected between the filter chamber, the mixing and reaction chamber and the water purifying chamber.
Preferably, it is interconnected between the mixing and reaction chamber, the pumping blower fan and the ammonia tourie.
Preferably, described filler layer is provided with two layers, and packing layer is symmetricly set on ammonia tourie both ends.
Preferably, the dividing plate is close web frame, and at the top of the dried hole covering pumping blower fan of diaphragm internal.
Preferably, the deflector and the motor are located at same centerline.
The beneficial effects of the utility model are：This kind of combined type ammonia nitrogen removal equipment can effectively reach in sewage disposal
To deamination purpose, and can makes ammonia be recycled utilization；The vertical mixing leaf set in mixing and reaction chamber can accelerate water and chemical agent
Reaction speed, so as to reach the effect of quick deamination；Dividing plate can absorb the globule contained in waste gas, avoid influenceing the suction of ammonia
Receive, ammonia absorber can effectively absorb the ammonia contained in waste gas, so that the ammonia in waste gas is recycled utilization, water purifying chamber
The sewage after hybrid reaction can be handled, makes sewage that the process of after-treatment with qualified discharge, can be avoided.
Brief description of the drawings
Fig. 1 is the utility model overall structure diagram；
Fig. 2 is the utility model water purifying chamber structural representation.
In figure：1st, shell, 2, water inlet, 3, filter chamber, 4, screen pack, 5, mixing and reaction chamber, 6, motor, 7, vertical mixing
Leaf, 8, deflector, 9, pumping blower fan, 10, dividing plate, 1001, dried hole, 11, ammonia tourie, 12, packing layer, 13, waste gas goes out
Mouthful, 14, water purifying chamber, 1401, activated carbon adsorption layer, 1402, cellulosic ultrafiltration film layer, 15, delivery port, 16, sewage draining exit, 17, except ammonia
Agent tank.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, 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, belong to the scope of the utility model protection.
Refer to shown in Fig. 1-2, a kind of combined type ammonia nitrogen removal equipment, including shell 1, mixing and reaction chamber 5 and ammonia are inhaled
Closed cans 11, the side wall of shell 1 is provided with water inlet 2, and water inlet 2 connects filter chamber 3；The inside of filter chamber 3 is provided with filtering
Net 4, and filter chamber 3 connects mixing and reaction chamber 5；The inside of mixing and reaction chamber 5 is provided with motor 6, and motor 6 connects vertical stir
Mix leaf 7；The top of mixing and reaction chamber 5 is provided with deflector 8, and the connection pumping blower fan 9 of deflector 8；The top of pumping blower fan 9
Provided with dividing plate 10；The pumping blower fan 9 connects ammonia tourie 11, and the inside of ammonia tourie 11 is provided with packing layer 12；The ammonia is inhaled
The top of closed cans 11 is provided with waste gas outlet 13；The mixing and reaction chamber 5 connects water purifying chamber 14, and the one end of water purifying chamber 14 is provided with water outlet
Mouth 15；The bottom of water purifying chamber 14 is provided with sewage draining exit 16；The inside of water purifying chamber 14 is provided with activated carbon adsorption layer 1401, and activity
The side of charcoal adsorption layer 1401 is provided with cellulosic ultrafiltration film layer 1402；The outer wall of shell 1 connection removes ammonia agent tank 17.
Wherein：Except ammonia agent composition is carboxymethyl cellulose sodium 75%-85%, aluminum sulfate 5%-15%, butanediol deaminase
5%-15%.
As a kind of technical optimization scheme of the present utility model, the filter chamber 3, the mixing and reaction chamber 5 and described
It is interconnected between water purifying chamber 14, is easy to the processing of sewage.
As a kind of technical optimization scheme of the present utility model, the mixing and reaction chamber 5, the pumping blower fan 9 and institute
State and be interconnected between ammonia tourie 11, realize the recycling of ammonia.
As a kind of technical optimization scheme of the present utility model, described filler layer 12 is provided with two layers, and packing layer 12 is symmetrical
The both ends of ammonia tourie 11 are arranged on, improve the absorptivity of ammonia.
As a kind of technical optimization scheme of the present utility model, the dividing plate 10 is close web frame, and inside dividing plate 10
The top of the covering pumping of dried hole 1001 blower fan 9, effectively absorbs the moisture in gas.
As a kind of technical optimization scheme of the present utility model, the deflector 8 and the motor 6 are located at same center
At line, accelerate the circulation of gas.
When in use, sewage enters filter chamber 3, the big impurity of preliminary filtering individual to the utility model from water inlet 2, then enters
Enter mixing and reaction chamber 5, sewage produces the waste gas with ammonia in the case where being acted on except chemicals such as ammonia agent；Meanwhile motor 6 drives and stood
Formula paddle 7 rotates, and accelerates the progress of chemical reaction, accelerates the purpose of deamination；Caused waste gas enters pumping by deflector 8
Blower fan 9, the globule contained in waste gas can be absorbed by dividing plate 10, avoid influenceing the absorption of ammonia, and then waste gas enters ammonia tourie 11,
Absorbed when waste gas passes through packing layer 12, other waste gas are discharged through waste gas outlet 13；Waste water after deamination enters water purifying chamber 14, only
After change processing, the water after purification is discharged from delivery port 15, and precipitated impurities are discharged from sewage draining exit 16.
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, it 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.
Moreover, it will be appreciated that although the present specification is described in terms of embodiments, not each embodiment is only wrapped
Containing an independent technical scheme, this narrating mode of specification is only that those skilled in the art should for clarity
Using specification as an entirety, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
It is appreciated that other embodiment.
Claims (6)
1. a kind of combined type ammonia nitrogen removal equipment, including shell (1), mixing and reaction chamber (5) and ammonia tourie (11), its feature
It is：Shell (1) side wall is provided with water inlet (2), and water inlet (2) connection filter chamber (3)；The filter chamber (3) is internal
Provided with screen pack (4), and filter chamber (3) connect mixing and reaction chamber (5)；Motor (6) is provided with inside the mixing and reaction chamber (5),
And motor (6) connection vertical mixing leaf (7)；Deflector (8) is provided with the top of the mixing and reaction chamber (5), and deflector (8) connects
It is evacuated blower fan (9)；Dividing plate (10) is provided with the top of the pumping blower fan (9)；Pumping blower fan (9) the connection ammonia tourie (11),
And it is provided with packing layer (12) inside ammonia tourie (11)；Waste gas outlet (13) is provided with the top of the ammonia tourie (11)；It is described mixed
Reative cell (5) connection water purifying chamber (14) is closed, and water purifying chamber (14) one end is provided with delivery port (15)；Water purifying chamber (14) bottom is set
There is sewage draining exit (16)；Activated carbon adsorption layer (1401), and activated carbon adsorption layer (1401) one are provided with inside the water purifying chamber (14)
Side is provided with cellulosic ultrafiltration film layer (1402)；Shell (1) the outer wall connection removes ammonia agent tank (17).
A kind of 2. combined type ammonia nitrogen removal equipment according to claim 1, it is characterised in that：It is the filter chamber (3), described
It is interconnected between mixing and reaction chamber (5) and the water purifying chamber (14).
A kind of 3. combined type ammonia nitrogen removal equipment according to claim 1, it is characterised in that：The mixing and reaction chamber (5),
It is interconnected between the pumping blower fan (9) and the ammonia tourie (11).
A kind of 4. combined type ammonia nitrogen removal equipment according to claim 1, it is characterised in that：Described filler layer (12) is provided with
Two layers, and packing layer (12) is symmetricly set on ammonia tourie (11) both ends.
A kind of 5. combined type ammonia nitrogen removal equipment according to claim 1, it is characterised in that：The dividing plate (10) is close net
Structure, and dried hole (1001) covering pumping blower fan (9) top that dividing plate (10) is internal.
A kind of 6. combined type ammonia nitrogen removal equipment according to claim 1, it is characterised in that：The deflector (8) and institute
State motor (6) and be located at same centerline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720785640.7U CN207192961U (en) | 2017-07-01 | 2017-07-01 | A kind of combined type ammonia nitrogen removal equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720785640.7U CN207192961U (en) | 2017-07-01 | 2017-07-01 | A kind of combined type ammonia nitrogen removal equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207192961U true CN207192961U (en) | 2018-04-06 |
Family
ID=61784457
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720785640.7U Expired - Fee Related CN207192961U (en) | 2017-07-01 | 2017-07-01 | A kind of combined type ammonia nitrogen removal equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207192961U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108706776A (en) * | 2018-06-12 | 2018-10-26 | 杨柳 | A kind of ammonia nitrogen sewage treatment equipment with high salt |
| CN114368820A (en) * | 2021-12-24 | 2022-04-19 | 安徽华塑股份有限公司 | Method for treating ammonia nitrogen in acetylene purification wastewater |
-
2017
- 2017-07-01 CN CN201720785640.7U patent/CN207192961U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108706776A (en) * | 2018-06-12 | 2018-10-26 | 杨柳 | A kind of ammonia nitrogen sewage treatment equipment with high salt |
| CN114368820A (en) * | 2021-12-24 | 2022-04-19 | 安徽华塑股份有限公司 | Method for treating ammonia nitrogen in acetylene purification wastewater |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180406 |