CN209668962U - A kind of SNCR denitration agent automatic assembly line water quality mixing system - Google Patents
A kind of SNCR denitration agent automatic assembly line water quality mixing system Download PDFInfo
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- CN209668962U CN209668962U CN201920341546.1U CN201920341546U CN209668962U CN 209668962 U CN209668962 U CN 209668962U CN 201920341546 U CN201920341546 U CN 201920341546U CN 209668962 U CN209668962 U CN 209668962U
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- Prior art keywords
- filter vat
- water quality
- assembly line
- water
- automatic assembly
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 83
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 16
- 238000002156 mixing Methods 0.000 title claims abstract description 14
- 238000004062 sedimentation Methods 0.000 claims abstract description 25
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000012528 membrane Substances 0.000 claims abstract description 20
- 239000010865 sewage Substances 0.000 claims description 14
- 230000001376 precipitating effect Effects 0.000 claims description 11
- 239000003153 chemical reaction reagent Substances 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 9
- 239000004065 semiconductor Substances 0.000 claims description 5
- 239000005341 toughened glass Substances 0.000 claims description 4
- 238000001914 filtration Methods 0.000 abstract description 13
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 10
- 241000894006 Bacteria Species 0.000 abstract description 7
- 239000003814 drug Substances 0.000 abstract description 7
- 239000012535 impurity Substances 0.000 abstract description 6
- 238000000746 purification Methods 0.000 abstract description 6
- 239000000084 colloidal system Substances 0.000 abstract description 5
- 229910052742 iron Inorganic materials 0.000 abstract description 5
- 125000001309 chloro group Chemical group Cl* 0.000 abstract description 4
- 239000005416 organic matter Substances 0.000 abstract description 4
- -1 peculiar smell Substances 0.000 abstract description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 22
- 101100372509 Mus musculus Vat1 gene Proteins 0.000 description 9
- 238000000108 ultra-filtration Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003916 acid precipitation Methods 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of SNCR denitration agent automatic assembly line water quality mixing systems, including the first filter vat and the second filter vat, it is connected between first filter vat and the second filter vat by pipeline, the inside of first filter vat and the second filter vat is separately installed with activated carbon filter layer and hyperfiltration membrane assembly, and the bottom of first filter vat and the second filter vat passes through drainpipe and is connected with sedimentation basin.Activated carbon filter layer and hyperfiltration membrane assembly are installed respectively in the inside of the first filter vat and the second filter vat, activated carbon filter layer carries out primary filtration to raw water, peculiar smell, organic matter, colloid, iron and chlorine residue etc. in raw water body are filtered, then into the second filter vat, by hyperfiltration membrane assembly in water body bacterium and impurity carry out exquisite filtering, it improves purification of water quality and reaches water quality requirement needed for medicament is deployed, denitration efficiency when medicament uses can be effectively promoted, it is spare by the progress constant temperature storage of constant temperature memory module after water filtration.
Description
Technical field
The utility model relates to SNCR denitration agent preparation technical field, specially a kind of SNCR denitration agent automatic assembly line water
Matter mixing system.
Background technique
Nitrogen oxides (NOx) is main atmosphere pollution, can cause acid rain, photochemical pollution, greenhouse effects and smelly
The destruction of oxygen layer.The main source of nitrogen oxides (NOx) first is that the flue gas that fired coal combustion is discharged, containing a large amount of NO, NO2 and
A small amount of N2O, the followed by tail gas of motor vehicle emission.With the development of China's power industry and universal, the nitrogen oxidation of private savings automobile
The total emission volumn of object (NOx) is quickly increasing, and the pollution for controlling and administering nitrogen oxides (NOx) is extremely urgent, wherein firing
The denitration of flue-gas is to control one of the important measures of nitrogen oxides (NOx).
When preparing denitrfying agent, need to the more demanding of water quality, at present only using to water quality carry out precipitating and
Filtering, but the impurity in water still cannot have and can effectively remove, and influence medicament preparation quality.For this purpose, it is proposed that a kind of
SNCR denitration agent automatic assembly line water quality mixing system.
Utility model content
The purpose of this utility model is to provide a kind of SNCR denitration agent automatic assembly line water quality mixing systems, by
Activated carbon filter layer and hyperfiltration membrane assembly are installed in the inside of one filter vat and the second filter vat respectively, and activated carbon filter layer is to raw water
Primary filtration is carried out, peculiar smell, organic matter, colloid, iron and chlorine residue etc. in raw water body are filtered, then into the second mistake
Lauter tub, by hyperfiltration membrane assembly in water body bacterium and impurity carry out exquisite filtering, to solve to propose in above-mentioned background technique
The problem of impurities in water remains.
To achieve the above object, the utility model provides the following technical solutions: a kind of SNCR denitration agent automatic assembly line water
Matter mixing system, including the first filter vat and the second filter vat, pass through pipeline between first filter vat and the second filter vat
It is connected, the inside of first filter vat and the second filter vat is separately installed with activated carbon filter layer and hyperfiltration membrane assembly, institute
The bottom for stating the first filter vat and the second filter vat passes through drainpipe and is connected with sedimentation basin, is equipped with water on the sedimentation basin
Pump, the water outlet of the water pump are connected by outlet pipe with water inlet pipe, and the water inlet pipe is connected to the inside of the first filter vat,
One side bottom of the sedimentation basin is communicated with sewage pipe, and solenoid valve, institute are mounted on the sewage pipe, drainpipe and outlet pipe
It states solenoid valve to be connected with control panel, pure water outlet tube is communicated on the hyperfiltration membrane assembly.
Preferably, timing module and microprocessor are connected on the control panel.
Preferably, one end of the pure water outlet tube is communicated with coil pipe, and the coil pipe is installed on heat-conducting plate, described to lead
The side of hot plate is equipped with semiconductor chilling plate.
Preferably, check-valves is installed on the pipeline.
Preferably, blender, precipitating reagent adding mouth and liquid level meter are installed on the sedimentation basin.
Preferably, the side of the sedimentation basin offers observation window, is equipped with toughened glass layer in the observation window.
Compared with prior art, the utility model has the beneficial effects that
1, the utility model by the inside of the first filter vat and the second filter vat install respectively activated carbon filter layer and
Hyperfiltration membrane assembly, activated carbon filter layer carries out primary filtration to raw water, by peculiar smell, organic matter, colloid, iron and chlorine residue in raw water body
Etc. being filtered, then into the second filter vat, by hyperfiltration membrane assembly in water body bacterium and impurity carry out it is exquisite
Filtering improves purification of water quality and reaches water quality requirement needed for medicament is deployed, can effectively promote denitration efficiency when medicament uses, water
It is spare by the progress constant temperature storage of constant temperature memory module after matter filtering；
2, the water quality filtered out in the first filter vat and the second filter vat is drained by the utility model by drainpipe
It is precipitated in sedimentation basin, is carried out by the solenoid valve on control panel control of sewage disposal pipe, drainpipe and outlet pipe every a timing
Between open primary, be conducive to the recycling of water, save water resource.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the schematic diagram of the section structure of the utility model sedimentation basin；
Fig. 3 is the schematic diagram of the section structure of the utility model the first filter vat and the second filter vat.
In figure: 1 first filter vat, 2 second filter vats, 3 activated carbon filter layers, 4 hyperfiltration membrane assemblies, 5 drainpipes, 6 electromagnetism
Valve, 7 control panels, 8 sedimentation basins, 9 pure water outlet tubes, 10 water inlet pipes, 11 water pumps, 12 outlet pipes, 13 sewage pipes, 14 coil pipes,
15 heat-conducting plates, 16 semiconductor chilling plates, 17 pipelines, 18 check-valves, 19 blenders, 20 precipitating reagent adding mouths, 21 liquid level meters, 22 are determined
When module, 23 microprocessors, 24 observation windows, 25 toughened glass layers.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Fig. 1~3 are please referred to, the utility model provides a kind of technical solution: a kind of SNCR denitration agent automatic assembly line water quality
Mixing system, including the first filter vat 1 and the second filter vat 2, pass through pipe between first filter vat 1 and the second filter vat 2
Road 17 is connected, and the inside of first filter vat 1 and the second filter vat 2 is separately installed with activated carbon filter layer 3 and ultrafiltration membrane
Component 4, filter membrane screening process, using the pressure difference of film two sides as driving force, using ultrafiltration membrane as filter medium, in certain pressure
Under, when stoste flows through film surface, the densely covered many tiny micropores of ultrafiltration membrane surface only allow water and small-molecule substance to pass through
And become permeate, and the substance that volume is greater than film surface micropore diameter in stoste is then trapped within the liquid feeding side of film, becomes concentration
Liquid, thus realize the purpose to the purification of stoste, separation and concentration.There are about 6,000,000,000 0.01 on every meter long of ultrafiltration membrane filaments tube wall
The micropore of micron, aperture only allows hydrone, the beneficial mineral matter in water and microelement to pass through, and is currently known the world most
The volume of small bacterium is therefore bacterium and the colloid more much bigger than bacterium volume, iron rust, suspended matter, silt, big at 0.2 micron
Molecular organic etc. can be retained down by ultrafiltration membrane, so that purification process is realized, first filter vat 1 and the second filtering
The bottom of bucket 2 passes through drainpipe 5 and is connected with sedimentation basin 8, and water pump 11 is equipped on the sedimentation basin 8, the water pump 11
Water outlet is connected by outlet pipe 12 with water inlet pipe 10, and the water inlet pipe 10 is connected to the inside of the first filter vat 1, described heavy
One side bottom in shallow lake pond 8 is communicated with sewage pipe 13, is mounted on solenoid valve on the sewage pipe 13, drainpipe 5 and outlet pipe 12
6, the solenoid valve 6 is connected with control panel 7, is communicated with pure water outlet tube 9 on the hyperfiltration membrane assembly 4, the pure water
Outlet tube 9 is connected to constant temperature storage box, convenient for saving to water body.
Specifically, being connected with timing module 22 and microprocessor 23 on the control panel 7.The timing module 22 is used to set
It fixes time, the switch of battery valve 6 is controlled by microprocessor 23, is drained into sedimentation basin 8 convenient for sewage and sinks in sedimentation basin 8
The sewage in shallow lake is discharged from sewage pipe 13.
Specifically, one end of the pure water outlet tube 9 is communicated with coil pipe 14, the coil pipe 14 is installed on heat-conducting plate 15
On, the side of the heat-conducting plate 15 is equipped with semiconductor chilling plate 16.The semiconductor chilling plate 16 heating passes through heat thermally conductive
Plate 15 passes to pure water outlet tube 9, heats to purified water, in order to mitigate the constant temperature and pressure of constant temperature storage box.
Specifically, being equipped with check-valves 18 on the pipeline 17.The check-valves 18 can prevent pure in the second filter vat 2
Water purification flows back in the first filter vat 1.
Specifically, being equipped with blender 19, precipitating reagent adding mouth 20 and liquid level meter 21 on the sedimentation basin 8.The liquid level meter
21 are convenient for precipitating reagent and water convenient for the liquid level in observation sedimentation basin 8, precipitating reagent adding mouth 20 convenient for addition precipitating reagent, blender 19
Fusion.
Specifically, the side of the sedimentation basin 8 offers observation window 24, toughened glass layer is installed in the observation window 24
25.The observation window 24 is convenient for the inner case of observation sedimentation basin 8.
Working principle: in use, raw water body is passed into the first filter vat 1 by water inlet pipe 10, activated carbon filter layer 3
Primary filtration is carried out to raw water, peculiar smell, organic matter, colloid, iron and chlorine residue etc. in raw water body are filtered, then into
Second filter vat 2, by hyperfiltration membrane assembly 4 in water body bacterium and impurity carry out exquisite filtering, improve purification of water quality and reach
Water quality requirement needed for deploying to medicament can effectively promote denitration efficiency when medicament uses, be gone out after water filtration by pure water
Liquid pipe 9 is passed into that constant temperature storage box is spare, and the water quality filtered out in the first filter vat 1 and the second filter vat 2 passes through drainpipe 5
It being drained into sedimentation basin 8, precipitating reagent is added in sedimentation basin 8, turn on agitator 19 precipitates the fusion of precipitating reagent and water,
Open at regular intervals once by the solenoid valve 6 on 7 control of sewage disposal pipe 13 of control panel, drainpipe 5 and outlet pipe 10,
Clear water in sedimentation basin 8 is pumped into the first filter vat 1 by water pump 11, is conducive to the recycling of water, saves water resource, precipitating
Sewage afterwards is discharged from sewage pipe 13.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (6)
1. a kind of SNCR denitration agent automatic assembly line water quality mixing system, including the first filter vat (1) and the second filter vat (2),
It is connected between first filter vat (1) and the second filter vat (2) by pipeline (17), it is characterised in that: first mistake
The inside of lauter tub (1) and the second filter vat (2) is separately installed with activated carbon filter layer (3) and hyperfiltration membrane assembly (4), and described first
The bottom of filter vat (1) and the second filter vat (2) passes through drainpipe (5) and is connected with sedimentation basin (8), the sedimentation basin (8)
On be equipped with water pump (11), the water outlet of the water pump (11) is connected by outlet pipe (12) with water inlet pipe (10), it is described into
Water pipe (10) is connected to the inside of the first filter vat (1), and a side bottom of the sedimentation basin (8) is communicated with sewage pipe (13), institute
It states and is mounted on solenoid valve (6) on sewage pipe (13), drainpipe (5) and outlet pipe (12), the solenoid valve (6) and control panel
(7) it is connected, is communicated with pure water outlet tube (9) on the hyperfiltration membrane assembly (4).
2. a kind of SNCR denitration agent automatic assembly line water quality mixing system according to claim 1, it is characterised in that: described
Timing module (22) and microprocessor (23) are connected on control panel (7).
3. a kind of SNCR denitration agent automatic assembly line water quality mixing system according to claim 1, it is characterised in that: described
One end of pure water outlet tube (9) is communicated with coil pipe (14), and the coil pipe (14) is installed on heat-conducting plate (15), the heat-conducting plate
(15) side is equipped with semiconductor chilling plate (16).
4. a kind of SNCR denitration agent automatic assembly line water quality mixing system according to claim 1, it is characterised in that: described
Check-valves (18) are installed on pipeline (17).
5. a kind of SNCR denitration agent automatic assembly line water quality mixing system according to claim 1, it is characterised in that: described
Blender (19), precipitating reagent adding mouth (20) and liquid level meter (21) are installed on sedimentation basin (8).
6. a kind of SNCR denitration agent automatic assembly line water quality mixing system according to claim 1, it is characterised in that: described
The side of sedimentation basin (8) offers observation window (24), is equipped with toughened glass layer (25) in the observation window (24).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920341546.1U CN209668962U (en) | 2019-03-18 | 2019-03-18 | A kind of SNCR denitration agent automatic assembly line water quality mixing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920341546.1U CN209668962U (en) | 2019-03-18 | 2019-03-18 | A kind of SNCR denitration agent automatic assembly line water quality mixing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209668962U true CN209668962U (en) | 2019-11-22 |
Family
ID=68571997
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920341546.1U Expired - Fee Related CN209668962U (en) | 2019-03-18 | 2019-03-18 | A kind of SNCR denitration agent automatic assembly line water quality mixing system |
Country Status (1)
| Country | Link |
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| CN (1) | CN209668962U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113304532A (en) * | 2020-10-15 | 2021-08-27 | 昆山金和诚自动化设备有限公司 | Full-automatic backwashing filter |
| CN114646743A (en) * | 2022-03-17 | 2022-06-21 | 重庆昕晟环保科技有限公司 | Test device for removing residual chlorine from secondary water supply terminal filter element |
-
2019
- 2019-03-18 CN CN201920341546.1U patent/CN209668962U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113304532A (en) * | 2020-10-15 | 2021-08-27 | 昆山金和诚自动化设备有限公司 | Full-automatic backwashing filter |
| CN114646743A (en) * | 2022-03-17 | 2022-06-21 | 重庆昕晟环保科技有限公司 | Test device for removing residual chlorine from secondary water supply terminal filter element |
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| 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: 20191122 |