CN207330480U - A kind of removing of iron and manganese mixes molten gas oxidator - Google Patents
A kind of removing of iron and manganese mixes molten gas oxidator Download PDFInfo
- Publication number
- CN207330480U CN207330480U CN201720796401.1U CN201720796401U CN207330480U CN 207330480 U CN207330480 U CN 207330480U CN 201720796401 U CN201720796401 U CN 201720796401U CN 207330480 U CN207330480 U CN 207330480U
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- CN
- China
- Prior art keywords
- dissolving
- jet ring
- jet
- ring
- iron
- 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.)
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Abstract
The utility model discloses a kind of removing of iron and manganese to mix molten gas oxidator,Including dissolving,Jet ring and filtering cabin,If dried layer jet ring is provided with dissolving,Jet ring is cavity ring structure,Delivered inside gas,Its both ends is by jet ring fixed frame on dissolving inner wall,The upper end of dissolving is provided with several flow distribution plates and is uniformly distributed,Flow distribution plate connects isocon,The upper end oligomerisation of isocon is simultaneously connected with one end of inlet channel,The lower end of dissolving is connected by water-supply-pipe and is connected with filtering cabin,Filter layer is installed inside filtering cabin,If the utility model sets dried layer jet ring in dissolving,Jet ring carries out jet purification when current are come in current,Allow to water and gas contact it is more abundant,What is purified is cleaner,And the manufacture cost of jet ring is comparatively low,Save cost,Installation is also convenient for,Jet by filtering cabin carries out primary purification again after having purified,So that the degree higher of purification.
Description
Technical field
It the utility model is related to water purifying equipment field, and in particular to a kind of removing of iron and manganese mixes molten gas oxidator.
Background technology
The concentration of ferrimanganic exceedes certain limit, will produce sediment russet, in life, can be in white fabrics or use
Macula lutea is left on hydrophone ware, while is also easy to breed iron bacteria, blocks pipeline, and drinking water ferrimanganic is excessive, can cause appetite
The problems such as depressed, vomiting, diarrhea, gastrointestinal disturbance, not normal stool.And existing removing of iron and manganese oxidator generally existing removal rate compared with
It is low, it is unable to reach ferrimanganic normal concentration, the shortcomings of installation is complicated, of high cost, and cleaning filtering is not in place, undercompounding.So
Develop a kind of removing of iron and manganese and mix molten gas oxidator.
Utility model content
Above-mentioned in order to solve the problems, such as, the utility model provides a kind of removing of iron and manganese and mixes molten gas oxidator, can solve
The problem of certainly being mentioned in background technology.
The utility model is to be achieved through the following technical solutions：
A kind of removing of iron and manganese mixes molten gas oxidator, including dissolving, jet ring and filtering cabin, is provided with the dissolving
If dried layer jet ring, the jet ring is cavity ring structure, and delivered inside gas, its both ends is fixed by jet ring fixed frame
On dissolving inner wall, the side of the jet ring connects feeder by jet delivery pipe, and the upper end of the dissolving is set
Be equipped with several flow distribution plates and be uniformly distributed, the flow distribution plate connects isocon, the upper end oligomerisation of the isocon and with water inlet
One end connection of pipeline, the lower end of the dissolving is connected by water-supply-pipe to be connected with filtering cabin, installation inside the filtering cabin
There is filter layer.
Further, respectively one exhaust pipe of installation, the exhaust pipe are to set obliquely for the upper end both sides of the dissolving.
Further, the filter layer uses conical design, and lower section tapered end connection blow-off pipe, under the filter layer
Side is equipped with drainpipe.
Further, a circle fumarole is provided with the jet ring, the fumarole direction jet ring central shaft is simultaneously oblique
Upward jet.
Compared with prior art, the beneficial effects of the utility model are：The utility model sets some in dissolving
Layer jet ring, jet ring carry out jet purification when current are come in current so that can be contacted more with water and gas
Fully, purification is more clean, and the manufacture cost of jet ring is comparatively low, saves cost, and installation is also convenient for, jet
Primary purification is carried out by filtering cabin again after having purified so that the degree higher of purification.
Brief description of the drawings
Fig. 1 is the overall structure diagram of the utility model；
Fig. 2 is the structure diagram of the jet ring of the utility model.
In figure：1st, dissolving；2nd, exhaust pipe；3rd, inlet channel；4th, isocon；5th, flow distribution plate；6th, jet ring；7th, jet ring
Fixed frame；8th, jet delivery pipe；9th, feeder；10th, filtering cabin；11st, water-supply-pipe；12nd, filter layer；13rd, blow-off pipe；14th, arrange
Water pipe；15th, fumarole.
Embodiment
The utility model is described in further detail with embodiment below in conjunction with the accompanying drawings：
As shown in Figs. 1-2, a kind of removing of iron and manganese mixes molten gas oxidator, including dissolving 1, jet ring 6 and filtering cabin 10, molten
If being provided with dried layer jet ring 6 in gas tank 1, jet ring 6 is cavity ring structure, and delivered inside gas, its both ends passes through jet
Ring fixed frame 7 is fixed on 1 inner wall of dissolving, and the side of jet ring 6 connects feeder 9, supply dress by jet delivery pipe 8
Put 9 and provide gas for jet ring 6, be then diverted to by jet delivery pipe 8 in each jet ring 6, one is provided with jet ring 6
Fumarole 15 is enclosed, fumarole 15 is directed toward 6 central shaft of jet ring and jet, the gas of jet ring 6 are oblique by fumarole 15 obliquely
Upper ejection, against the current fallen；The upper end of dissolving 1 is provided with several flow distribution plates 5 and is uniformly distributed, and flow distribution plate 5 connects
Isocon 4 is connect, the upper end oligomerisation of isocon 4 is simultaneously connected with one end of inlet channel 3, the water come in from the interior conveying of inlet channel 3
Some tributaries are separated by isocon 4, moisture is spread out by flow distribution plate 5 when then each Zhi Liuxiang dissolvings 1 flow into
Come so that more preferably merged with gas；The lower end of dissolving 1 is connected by water-supply-pipe 11 and is connected with filtering cabin 10, in filtering cabin 10
Portion is provided with filter layer 12, and filter layer 12 uses conical design, and lower section tapered end connection blow-off pipe 13, the lower section of filter layer 12
Equipped with drainpipe 14, the sludge filtered out is discharged by blow-off pipe 13, and clear water is transported in clear water reserviors by drainpipe 14；It is molten
An exhaust pipe 2 is respectively installed in the upper end both sides of gas tank 1, the gas in dissolving 1 is discharged by exhaust pipe 2, exhaust pipe 2
To set obliquely so that water can be placed and flowed into exhaust pipe 2.
Operation principle：Water is come in from the input of inlet channel 3, then separates some tributaries by isocon 4, then each
Flow to when dissolving 1 flows into and moisture is spread out to flow into dissolving 1, while feeder 9 produces by flow distribution plate 5
Gas, is then respectively transmitted in each jet ring 6 by jet delivery pipe 8, and the gas in jet ring 6 passes through fumarole 15
Sprayed to the water fallen so that water and gas current, accomplish more fully to mix, water does not lead to during falling
Crossing a jet ring 6 just has a mixing；Then the water in dissolving 1 is flowed into filtering cabin 10 by water-supply-pipe 11, is passed through
Filter layer 12 in filter position 10 is transported in clear water reserviors after filtering by drainpipe 14, and sludge can pass through blow-off pipe on filter layer 12
13 discharges；Discharged after use by exhaust pipe in the gas of dissolving 1.
The basic principle, main feature and advantage of the utility model has been shown and described above.The technical staff of the industry
It should be appreciated that the present utility model is not limited to the above embodiments, the above embodiments and description only describe this
The principle of utility model, on the premise of not departing from the spirit and scope of the utility model, the utility model also has various change
And improvement, these various changes and improvements fall within the scope of the claimed invention.The utility model requires protection scope
It is defined by the appending claims and its equivalent thereof.
Claims (4)
1. a kind of removing of iron and manganese mixes molten gas oxidator, including dissolving（1）, jet ring（6）And filtering cabin（10）, its feature exists
In：The dissolving（1）If inside it is provided with dried layer jet ring（6）, the jet ring（6）For cavity ring structure, delivered inside
Gas, its both ends pass through jet ring fixed frame（7）It is fixed on dissolving（1）On inner wall, the jet ring（6）Side pass through spray
Letter shoot（8）Connect feeder（9）, the dissolving（1）Upper end be provided with several flow distribution plates（5）And uniformly divide
Cloth, the flow distribution plate（5）Connect isocon（4）, the isocon（4）Upper end oligomerisation and and inlet channel（3）One end connect
Connect, the dissolving（1）Lower end pass through water-supply-pipe（11）With filtering cabin（10）Connection, the filtering cabin（10）Inside is provided with
Filter layer（12）.
2. a kind of removing of iron and manganese according to claim 1 mixes molten gas oxidator, it is characterised in that：The dissolving（1）'s
Upper end both sides are respectively installed by one exhaust pipe（2）, the exhaust pipe（2）To set obliquely.
3. a kind of removing of iron and manganese according to claim 1 mixes molten gas oxidator, it is characterised in that：The filter layer（12）Adopt
With conical design, and lower section tapered end connection blow-off pipe（13）, the filter layer（12）Lower section be equipped with drainpipe（14）.
4. a kind of removing of iron and manganese according to claim 1 mixes molten gas oxidator, it is characterised in that：The jet ring（6）On
It is provided with a circle fumarole（15）, the fumarole（15）It is directed toward jet ring（6）Central shaft and obliquely jet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720796401.1U CN207330480U (en) | 2017-07-04 | 2017-07-04 | A kind of removing of iron and manganese mixes molten gas oxidator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720796401.1U CN207330480U (en) | 2017-07-04 | 2017-07-04 | A kind of removing of iron and manganese mixes molten gas oxidator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207330480U true CN207330480U (en) | 2018-05-08 |
Family
ID=62427133
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720796401.1U Expired - Fee Related CN207330480U (en) | 2017-07-04 | 2017-07-04 | A kind of removing of iron and manganese mixes molten gas oxidator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207330480U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110156220A (en) * | 2019-07-03 | 2019-08-23 | 浙江海洋大学 | A kind of harbour oil spot treatment device |
-
2017
- 2017-07-04 CN CN201720796401.1U patent/CN207330480U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110156220A (en) * | 2019-07-03 | 2019-08-23 | 浙江海洋大学 | A kind of harbour oil spot treatment device |
| CN110156220B (en) * | 2019-07-03 | 2023-12-29 | 浙江海洋大学 | Port greasy dirt processing apparatus |
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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 |
Granted publication date: 20180508 Termination date: 20190704 |
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| CF01 | Termination of patent right due to non-payment of annual fee |