CN207175557U - A kind of phosphorus reclaims crystallization reactor - Google Patents
A kind of phosphorus reclaims crystallization reactor Download PDFInfo
- Publication number
- CN207175557U CN207175557U CN201720929901.8U CN201720929901U CN207175557U CN 207175557 U CN207175557 U CN 207175557U CN 201720929901 U CN201720929901 U CN 201720929901U CN 207175557 U CN207175557 U CN 207175557U
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- reactor body
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- disturbing cover
- flow disturbing
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- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 238000002425 crystallisation Methods 0.000 title claims abstract description 32
- 230000008025 crystallization Effects 0.000 title claims abstract description 32
- 239000011574 phosphorus Substances 0.000 title claims abstract description 32
- 229910052698 phosphorus Inorganic materials 0.000 title claims abstract description 32
- 238000003860 storage Methods 0.000 claims abstract description 46
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 230000007246 mechanism Effects 0.000 claims abstract description 9
- 238000007599 discharging Methods 0.000 claims abstract description 3
- 238000000926 separation method Methods 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 2
- 238000012544 monitoring process Methods 0.000 claims description 2
- 238000011084 recovery Methods 0.000 abstract description 12
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 239000013078 crystal Substances 0.000 description 6
- 238000006073 displacement reaction Methods 0.000 description 6
- 238000003756 stirring Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000008247 solid mixture Substances 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- 229910019142 PO4 Inorganic materials 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 210000002445 nipple Anatomy 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 2
- 235000021317 phosphate Nutrition 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000012271 agricultural production Methods 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 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
- 239000000835 fiber Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 125000002467 phosphate group Chemical group [H]OP(=O)(O[H])O[*] 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Landscapes
- Removal Of Specific Substances (AREA)
Abstract
The utility model discloses a kind of phosphorus recovery crystallization reactor.Including the up-flow cylinder being arranged from inside to outside and reactor body；Reactor body bottom is provided with crystallized product storage bucket, and crystallized product storage bucket is provided with the plugging device for discharging crystallized product；Reactor body side wall is provided with drug-feeding tube and water inlet pipe；The drainage mechanism of access reactor body overflow water outlet is provided on the outside of reactor body；The air diffuser for reducing feed liquid density in up-flow cylinder, forming feed liquid circulation is vertically set up in the up-flow cylinder；The position that the top of the up-flow cylinder correspondingly flows up cylinder delivery port is provided with the flow disturbing cover extended along delivery port center into reactor body, and flow disturbing cover top is horn-like structure；Blast pipe is provided with the top of flow disturbing cover；The flow disturbing cover is slidably connected with reactor body；Wherein, the region that the outside of flow disturbing cover corresponds to reactor body is settling zone, and the bottom that reactor body is located at settling zone is horn-like structure wide at the top and narrow at the bottom.
Description
Technical field
It the utility model is related to field of water treatment equipment, more particularly to a kind of phosphorus recovery crystallization reactor.
Background technology
Phosphorus is the important element for causing body eutrophication, while is also the indispensable valuable source of production and living.Perhaps
The largely sewage containing high concentration phosphorus, such as livestock breeding wastewater, chemical fertilizer production waste water are produced in multiplexing agricultural production process.Adopt
Chemically phosphorus is separated out with phos-phate forms, be a kind of effective sewage dephosphorization method, while phosphor resource can be realized
Recovery.But currently still lack efficient phosphorus recovery reactor.Current phosphorus recovery uses mechanical agitation, and crystallization process is disturbed
It is dynamic big, while phosphorus recovery product is easily adhered in paddle board, causes stirring efficiency to reduce；Partial reaction device is stirred using full aeration air
Mix (temper in whole reactor), power consumption is higher, and the mode of currently employed air stirring, generally there are for water, gas, consolidates
The problem of three phase separating efficiency is not high.In addition, current reactor is when considering crystallized product discharge, the blocking of upper water,
While excluding product, have a large amount of water and discharge together so that the moisture content of product is high, increases follow-up product.
Utility model content
In view of the above-mentioned problems, the utility model provides a kind of crystallization effect good crystallization reactor phosphorus recovery crystallization reaction
Device.
To reach above-mentioned purpose, a kind of phosphorus recovery crystallization reactor of the utility model includes the up-flow cylinder being arranged from inside to outside
And reactor body；
The reactor body bottom is provided with crystallized product storage bucket, and the crystallized product storage bucket is provided with for arranging
Put the plugging valve of crystallized product；The reactor body side wall is provided with drug-feeding tube and water inlet pipe；The reactor body
Outside is provided for the drainage mechanism of access reactor body overflow；
Air diffuser has vertically been set up in the up-flow cylinder；The top of the up-flow cylinder correspondingly flows up cylinder
The position of delivery port is provided with the flow disturbing cover extended along delivery port center into reactor body；The top of the flow disturbing cover is set
There is blast pipe；The flow disturbing cover is slidably connected with the reactor body.
Further, the position that the reactor body corresponds to the flow disturbing cover bottom is horn-like structure；The loudspeaker
The upper port of shape structure is more than the lower port of horn-like structure.
Further, sliding part is provided with the reactor body, the flow disturbing cover is slidably connected with the sliding part；
The sliding part includes the fixed plate being symmetricly set on reactor body；Cunning is vertically provided with the fixed plate
Groove；Connecting rod corresponding with the fixed plate is provided with blast pipe at the top of the flow disturbing cover；It is provided with the connecting rod
The sliding block being adapted with the chute；Pulling apparatus is additionally provided with the top of the blast pipe.
Further, the drainage mechanism includes the height around water leg described in the water leg set on the outside of reactor body
Height of the degree higher than reactor body；The bottom of the water leg is provided with outlet pipe.
Further, in addition to the separating device that is arranged between reactor body bottom and crystallized product storage bucket；Institute
The separation flashboard in separating device is stated to be arranged at the charging aperture of crystallized product storage bucket, for blocking or opening crystallized product storage
Deposit bucket charging aperture.
Further, the reactor body lower end is arranged with top storage tank；The crystallized product storage bucket upper end set
The bottom storage tank being provided with；The side wall of the top storage tank and the side wall of the bottom storage tank are tightly connected to form flashboard appearance
Put chamber；The length of the accommodating cavity, which is more than, separates flashboard length, and the separation flashboard is slidably arranged in accommodating along its length
Intracavitary；
Wherein, rotatable on the separation flashboard to be provided with a screw rod, the one end of the screw rod away from reactor body is worn
Accommodating groove sidewall is crossed to be connected with storage tank sidewall thread.
Further, it is provided with flowmeter on the water inlet pipe；The drug-feeding tube is provided with health-monitoring installation.
Further, the screw rod has leader through the end set of the accommodating groove sidewall.
The utility model phosphorus reclaims crystallization reactor, by the air diffuser being arranged in up-flow cylinder and is arranged on up-flow
The flow disturbing cover of cylinder top, the feed liquid in reactor body can be made to be entered from the bottom water inlet of up-flow cylinder in up-flow cylinder, and
It is back to after delivery port outflow, collision flow disturbing cover from up-flow cylinder top in reactor body, realizes and cut in relatively low current
Under shear force, feed liquid energy circulation stirring, promote the precipitation of nucleus；Because flow disturbing cover is deep into reactor body so that reactor
It is smaller that the water flow fluctuation in the region on the outside of flow disturbing cover is corresponded in main body, sinks to flowing back into crystallized product storage beneficial to crystallized product
Bucket, while the clean water in the region overflows from reactor body top delivery port, enters drainage mechanism.
In view of the above-mentioned problems, the utility model provides a kind of phosphorus crystallization recovering effect good water treatment facilities.
To reach above-mentioned purpose, a kind of water treatment facilities of the utility model, including above-mentioned phosphorus recovery crystallization reactor.
A kind of water treatment facilities of the utility model, crystallization reactor is reclaimed by being provided with above-mentioned phosphorus, can be to phosphorous
Sewage carries out dephosphorization processing, the phosphorus-containing wastewater after processing is met discharge standard.
Brief description of the drawings
Fig. 1 is the utility model overall structure, principle schematic；
Fig. 2 is sliding block and sliding groove structure schematic diagram in sliding part；
Fig. 3 is reactor body and crystallized product storage bucket separating device floor map；
Fig. 4 is reactor body and crystallized product storage bucket separating device sectional schematic diagram.
Embodiment
The utility model is further described with reference to Figure of description.
Embodiment 1
With reference to Fig. 1, a kind of phosphorus of the utility model recovery crystallization reactor, including the up-flow cylinder 2 being arranged from inside to outside and anti-
Answer device main body 1；
The bottom of reactor body 1 is provided with crystallized product storage bucket 4, the row of the bottom of the crystallized product storage bucket
Put the plugging valve 3 being provided with pipe for discharging crystallized product；The reactor body side wall is provided with drug-feeding tube 5 and water inlet
Pipe 6；The drainage mechanism of access reactor body overflow is provided on the outside of the reactor body；
2 have vertically set up air diffuser 7 in the up-flow cylinder；The top of the up-flow cylinder 2 is corresponding to rise
The position of flow cartridge delivery port is provided with the flow disturbing cover 8 extended along delivery port center into reactor body；The top of the flow disturbing cover
Portion is provided with blast pipe 9；The flow disturbing cover 8 is connected with the reactor body.
In the present embodiment the utility model phosphorus reclaim crystallization reactor, by be arranged on up-flow cylinder in air diffuser and
The flow disturbing cover being arranged on above up-flow cylinder, the feed liquid in reactor body can be made to enter liter from the bottom water inlet of up-flow cylinder
In flow cartridge, and the delivery port from up-flow cylinder top flows out；, can when flowing up water in cylinder, gas, solid mixture collision flow disturbing cover surface
Deviate from gas, rise along loudspeaker section inclined-plane, discharged by gas outlet pipe, solid, liquid mixture is then partly into anti-
Answer and participate in circulating next time in device main body, another part enters reactor body from gap 10 and correspond to consolidating on the outside of flow disturbing cover
Liquid Disengagement zone 11；Due to the barrier effect of flow disturbing cover side wall so that correspond to the separation of solid and liquid on the outside of flow disturbing cover in reactor body
The water flow fluctuation in area 11 is smaller, sinks to flowing back into crystallized product storage bucket beneficial to crystallized product, while solid-liquid displacement zone 11 is upper
Portion's clean water overflows from reactor body top delivery port, enters drainage mechanism.
The air diffuser set in cylinder is flowed up in the present embodiment can play the effect of carbon dioxide stripping simultaneously so that air
Diffuser has carbon dioxide stripping function concurrently, can be to continuous stripping carbon dioxide in cylinder is flowed up, with maintenance reaction device pH stabilizations.
The utility model is realized under relatively low flow shear, feed liquid energy circulation stirring, promotes the precipitation of nucleus.
Embodiment 2
As the further improvement of embodiment 1, the position that the reactor body corresponds to the top of flow disturbing cover 8 is loudspeaker
Shape structure；The upper port of the horn-like structure is less than the lower port of horn-like structure.
The position that the reactor body corresponds to the bottom of the settling zone is horn-like structure wide at the top and narrow at the bottom, described anti-
Answer the horn-like structure of device main body corresponding with the bottom of flow disturbing cover.
By the way that horn-like structure will be arranged on reactor body in the present embodiment so that be located at flow-disturbing in reactor body
The reservoir storage increase of the solid-liquid displacement zone 11 in outside is covered, passes through the current ripple of the stop solid-liquid displacement zone 11 of flow disturbing cover side wall
It is dynamic smaller, flow back into crystallized product storage bucket beneficial to phosphorus crystallization sinking.By the way that horn-like structure will be arranged at the top of flow disturbing cover,
So that gas can be made preferably to deviate from, along loudspeaker section inclined-plane when water, gas, solid mixture collision flow disturbing cover surface in up-flow cylinder
Rise, discharged by gas outlet pipe.
Embodiment 3
As the concrete scheme of embodiment 1, the flow disturbing cover 8 is slidably connected with the reactor body by sliding part,
The sliding part includes symmetrically being fixed in the fixed plate of fixed plate 12 on reactor body vertically admittedly by bolt 32
Surely there is chute 13；It is horizontally disposed on the blast pipe 9 to have connecting rod 14 corresponding with the fixed plate；The connecting rod
The sliding block 15 being adapted with the chute is provided with 14；Pulling apparatus 16 is additionally provided with the top of the blast pipe.
Specific sliding block is provided with by the slipmat of the high materials for support of the coefficient of friction such as cotton, fiber crops in the position that chute contacts
Piece；Specifically, sliding block 12 is embedded in chute 13, can be along brush when the pulling apparatus 16 at the top of by discharge pipe applies external force
Groove moves up and down, and then drives flow disturbing cover 8 to move up and down, when not applying external force, then by the frictional force between sliding block and chute
Overcome the gravity of flow disturbing cover 8 and blast pipe 9, remains stationary.By the way that flow disturbing cover is slidably arranged in into reactor in the present embodiment
In main body so that the regulation of flow disturbing cover upper and lower position, and then realize that flow disturbing cover bottom is located at settling zone bottom with reactor body
The regulation in the gap 10 between the side wall of horn-like structure；I.e. according to the difference of inflow, the height of flow disturbing cover is adjusted, adjusts seam
The width of gap 10.
Embodiment 4
As the concrete scheme of embodiment 1, the drainage mechanism includes being circumferentially positioned at the water leg on the outside of reactor body
17, the height of the water leg 17 is higher than the height of reactor body；The bottom of the water leg is provided with outlet pipe 18.
Embodiment 5
With reference to Fig. 3 and Fig. 4, the present embodiment and the difference of embodiment 1 are reactor body bottom and crystallized product
Separating device is provided between storage bucket；
The separating device includes separating flashboard 19, is set in the top storage tank 20 and set of the reactor body lower end
It is located at the bottom storage tank 21 of the crystallized product storage bucket upper end；The side wall of the top storage tank 20 houses with the bottom
The side wall of groove 21 is tightly connected to form flashboard accommodating cavity 22；
The separation flashboard is arranged in the flashboard accommodating cavity 22；It is rotatable on the separation flashboard to be provided with a screw rod
23, one end of screw rod 23 is rotatably arranged on by swivel 34 to be separated on flashboard 19, and screw rod 23 passes through nipple
24 are connected with storage tank sidewall thread；The screw rod 23 is additionally provided with a drive link 25 through the end of the accommodating groove sidewall,
Handle 26 is provided with drive link 25.When rotational handle 26, screw rod can be driven to rotate, screw rod can axially be transported along nipple
It is dynamic, and then drive separation flashboard inwardly or outwardly to run, when separation flashboard is in the abcd positions in Fig. 3, separate at flashboard
In closed mode, when the ab sides for separating flashboard move to axis a'b', then flashboard is shown in a fully open operation.Specifically, this implementation
The outside of example middle and upper part storage tank 20 and bottom storage tank 21 is provided with flange 27, flange 28, and reactor body 1 and crystallization are produced
Thing storage bucket 4 is fixedly connected by flange 27 with flange 28.
By setting separating device in the present embodiment, when the crystallization reactor is run, separate flashboard and open, reactor
Main body 1 connects with crystallized product storage bucket 4, and the crystallized product in reactor body 1 can be deposited into crystallized product storage bucket 4；
When the crystallized product in crystallized product storage bucket runs up to a certain amount of, close reactor body 1 and crystallized product storage bucket 4 it
Between separation flashboard 19, then open crystallized product storage bucket on plugging valve 3, discharge crystallized product；Excluding crystallization production
While thing is discharged, the water in reactor is prevented to be discharged with crystallized product so that the crystallized product moisture content drop of discharge
It is low, reduce subsequent processes difficulty.
Embodiment 6
As the concrete scheme of embodiment 1, flowmeter 29 is provided with the water inlet pipe 6；The drug-feeding tube 5 is provided with agent
Amount control device.
After sewage is pH adjusted in the present embodiment, phosphorus recovery crystallization reactor is entered by water inlet pipe 6, while by entering medicine
Pipe adds the chemical agent that indissoluble crystal can be generated with solvable phosphate reaction in water by a certain percentage, such as magnesium chloride, calcium chloride
Deng.Water inlet pipe 6 is provided with flowmeter 29, and medicament flow can be controlled by metering device, such as measuring pump.
Embodiment 7
A kind of water treatment facilities in the present embodiment, including any one phosphorus reclaims crystallization reactor in above-described embodiment.
The course of work of phosphorus of the present utility model recovery crystallization reactor is：By drug-feeding tube and water inlet pipe constantly to anti-
Answer and water and medicament are added in device main body；Air device is opened, sky is passed through into up-flow cylinder 2 by air duct, air diffuser 7
Gas, reduce mixed liquor density in up-flow cylinder 2, make in the outer mixed liquor press-in up-flow cylinder 2 of up-flow cylinder, so in up-flow cylinder 2 feed liquid to
Upper motion, flow up after feed liquid encounters the side wall converging transition 31 of flow disturbing cover 8 in cylinder, air and solid (phosphate crystal particle) and moisture
From air is discharged through air discharge duct 9, and water, solid mixture are then folded to lower section, and because overflow acts on, a part is through bell jar bottom
Enter solid-liquid displacement zone 11 with the precipitation pool wall bottom gap 10 of domatic, after remainder declines through Jiang Liu areas 30, then be pressed into
Flow up cylinder and form circulation.Crystal or nucleus into solid-liquid displacement zone 11 are separated from water under gravity, and along through bell jar
Gap 10 between bottom and precipitation pool wall bottom are domatic flows back into Jiang Liu areas, and larger crystal may proceed to sink to entering crystallization production
Thing storage bucket 4, small crystals continue to circulate in reaction, form stirring action, promote phosphate nucleus to be formed, separated out；Specifically
, it is alternatively arranged as nucleus and continues to induce crystal to separate out so that its size continues to become big.The clear water that solid-liquid displacement zone 11 is isolated
Water leg 17 is overflowed to by the annular effluent weir on reactor body top, is flowed out through outlet pipe 18.
More than, preferred embodiment only of the present utility model, but the scope of protection of the utility model is not limited thereto, and is appointed
What those familiar with the art the change that can readily occur in or replaces in the technical scope that the utility model discloses
Change, should all cover within the scope of protection of the utility model.Therefore, the scope of protection of the utility model should be with claim
The protection domain defined is defined.
Claims (9)
1. a kind of phosphorus reclaims crystallization reactor, it is characterised in that including the up-flow cylinder being arranged from inside to outside and reactor body；
The reactor body bottom is provided with crystallized product storage bucket, and the crystallized product storage bucket is provided with for discharging knot
The plugging device of brilliant product；The reactor body side wall is provided with drug-feeding tube and water inlet pipe；Set on the outside of the reactor body
Put the drainage mechanism for access reactor body overflow water outlet；
Vertically set up in the up-flow cylinder for reducing feed liquid density in up-flow cylinder, forming feed liquid in reactor
The air diffuser of inner loop；The position that the top of the up-flow cylinder correspondingly flows up cylinder delivery port is provided with along delivery port center
The flow disturbing cover extended into reactor body；Wherein, the region that the outside of the flow disturbing cover corresponds to reactor body is settling zone；
Blast pipe is additionally provided with the top of the flow disturbing cover；The flow disturbing cover is slidably connected with the reactor body.
2. phosphorus according to claim 1 reclaims crystallization reactor, it is characterised in that is horn-like knot at the top of the flow disturbing cover
Structure, the upper port of the horn-like structure are less than the lower port of horn-like structure.
3. phosphorus according to claim 1 reclaims crystallization reactor, it is characterised in that the reactor body corresponds to described heavy
The position of the bottom in shallow lake area is horn-like structure wide at the top and narrow at the bottom, the horn-like structure of the reactor body and the bottom of flow disturbing cover
Hold corresponding.
4. phosphorus according to claim 1 reclaims crystallization reactor, it is characterised in that is provided with cunning on the reactor body
Dynamic portion, the flow disturbing cover are slidably connected with the sliding part；The sliding part includes being symmetricly set on consolidating on reactor body
Fixed board；Chute is vertically provided with the fixed plate；Be provided with blast pipe at the top of the flow disturbing cover with it is described solid
Connecting rod corresponding to fixed board；The sliding block being adapted with the chute is provided with the connecting rod；The top of the blast pipe is also
It is provided with pulling apparatus.
5. phosphorus according to claim 1 reclaims crystallization reactor, it is characterised in that the drainage mechanism is included around setting
The water leg on the outside of settling zone is corresponded in reactor body, the height of the water leg is higher than the height of reactor body；It is described
The bottom of water leg is provided with outlet pipe.
6. phosphorus according to claim 1 reclaims crystallization reactor, it is characterised in that also includes being arranged on reactor body bottom
Separating device between portion and crystallized product storage bucket；
The separating device includes separating flashboard, is set in the top storage tank of the reactor body lower end and is set in described
The bottom storage tank of crystallized product storage bucket upper end；The side wall of the top storage tank and the side wall of the bottom storage tank seal
Connection forms flashboard accommodating cavity；
The separation flashboard is arranged in the flashboard accommodating cavity；It is rotatable on the separation flashboard to be provided with a screw rod, it is described
The one end of screw rod away from reactor body passes through accommodating groove sidewall to be connected with storage tank sidewall thread.
7. phosphorus according to claim 1 reclaims crystallization reactor, it is characterised in that is provided with flow on the water inlet pipe
Meter；The drug-feeding tube is provided with health-monitoring installation.
8. phosphorus according to claim 6 reclaims crystallization reactor, it is characterised in that the screw rod passes through the storage tank side
The end set of wall has leader.
9. a kind of water treatment facilities, it is characterised in that reclaim crystallization reaction including the phosphorus as described in claim 1-7 any one
Device.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720929901.8U CN207175557U (en) | 2017-07-28 | 2017-07-28 | A kind of phosphorus reclaims crystallization reactor |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201720929901.8U CN207175557U (en) | 2017-07-28 | 2017-07-28 | A kind of phosphorus reclaims crystallization reactor |
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| Publication Number | Publication Date |
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| CN207175557U true CN207175557U (en) | 2018-04-03 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107285443A (en) * | 2017-07-28 | 2017-10-24 | 安徽农业大学 | A kind of phosphorus reclaims crystallization reactor |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107285443A (en) * | 2017-07-28 | 2017-10-24 | 安徽农业大学 | A kind of phosphorus reclaims crystallization reactor |
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