CN209468232U - A kind of high-salt wastewater softening plant - Google Patents
A kind of high-salt wastewater softening plant Download PDFInfo
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- CN209468232U CN209468232U CN201822235863.3U CN201822235863U CN209468232U CN 209468232 U CN209468232 U CN 209468232U CN 201822235863 U CN201822235863 U CN 201822235863U CN 209468232 U CN209468232 U CN 209468232U
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- softening
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Abstract
The utility model discloses a kind of high-salt wastewater softening plants, including conditioning tank, softening pond, coagulating basin, clarifying basin, microfiltration systems and the nanofiltration system being sequentially communicated from beginning to end；It adjusts bottom of pond portion and is connected with the first spoil disposal pipeline；It is connected with crystal seed at the top of softening pond and launches pipeline and the first medicament delivery pipeline, softening bottom of pond portion is connected with the second spoil disposal pipeline；It is connected with second medicament at the top of coagulating basin and launches pipeline, coagulation bottom of pond portion is connected to the second spoil disposal pipeline；Clarification bottom of pond portion is connected to the second spoil disposal pipeline；Microfiltration equipment is equipped with inside microfiltration systems, and microfiltration equipment is connected to nanofiltration system；Concentrated water room, freshwater room and the nanofiltration membrane between concentrated water room and freshwater room are equipped with inside nanofiltration system.The utility model has the following beneficial effects: the property of can choose by Ca2+The softening medicament excessively added from separation, selective recovery in waste water, the dosage and cost that reduce the production quantity of sediment in softening process, reduce softening agent.
Description
Technical field
The utility model relates to environmental technology fields, in particular to a kind of high-salt wastewater softening plant.
Background technique
In the industrial wastewater of all polymorphic types, high-salt wastewater is since salt content is high, discharge capacity is big and has corrosivity to metal
(such as Cl-Corrosion) etc. features, direct outlet can cause to seriously endanger to ecological environment, therefore discharge again after being handled.Mesh
Before, embrane method is one of the main method of high-salt wastewater processing, due to being often rich in Ca in waste water2+And Mg2+, it is easy to cause filter membrane
Fouling, it is therefore necessary to first carry out softening pretreatment.Conventional softening method is by Ca2+And Mg2+It is all removed, such as ripe stone
Ash-Method of Soda, caustic soda-Method of Soda and lime method etc., this method there are softening agent consumptions it is big, precipitation capacity is big the problems such as.
Due to Mg2+Scale problems can by adjust pH be controlled, even if formed Mg (OH)2Also usable acid is clear for dirt
It washes；And Ca2+The CaSO of formation4The extremely difficult cleaning of dirt, dirt, which is known from experience, causes irreversible influence to filter membrane.It therefore, if can selectivity
Ground removes Ca2+Without removing Mg2+, softening efficiency not only can be improved, can more reduce reagent cost.(the step-by-step precipitation methods such as Li Xin
Remove the research water treatment technology of calcium and magnesium in RE waste water, 2016,42 (7): 88-92) it proposes and a kind of is selectively gone with oxalic acid
Except RE waste water Ca2+Method, (a kind of high magnesium low calcium desulfurization wastewater softens pretreatment unit Chinese patent: ZL to Li Fei etc.
201721032808.3) and Liu Haiyang etc. (a kind of high magnesium low calcium desulfurization wastewater softens pretreatment unit Chinese patent: ZL
201721032793.0) propose a kind of heat-engine plant desulfurized waste water Ca of oxalates selective removal2+Method, these methods exist
Remove Ca2+While to Mg2+Influence it is very low, can be effectively reduced softening agent consumption and precipitating yield.However, above-mentioned soft
Change method is both needed to excessively add oxalic acid or oxalates, and the medicament excessively added fails using just discharging, due to these medicament valences
Lattice are higher, excessively add part if can recycle, can reduce softening reagent cost.
Utility model content
To solve the above problems, can choose the purpose of this utility model is to provide a kind of high-salt wastewater softening plant
Property by Ca2+Excessively soften medicament from separation, selective recovery in waste water, reduce the production quantity of sediment in softening process, drop
The dosage and cost of low softening agent.
The utility model provides a kind of high-salt wastewater softening plant, including be sequentially communicated from beginning to end conditioning tank, softening pond,
Coagulating basin, clarifying basin, microfiltration systems and nanofiltration system；
The adjusting bottom of pond portion is connected with the first spoil disposal pipeline；
It is connected with crystal seed at the top of the softening pond and launches pipeline and the first medicament delivery pipeline, the softening bottom of pond portion connection
There is the second spoil disposal pipeline；
It is connected with second medicament at the top of the coagulating basin and launches pipeline, the coagulation bottom of pond portion is connected to second sludge pipe
Road；
The clarification bottom of pond portion is connected to the second spoil disposal pipeline；
Microfiltration equipment is equipped with inside the microfiltration systems, and the microfiltration equipment is connected to the nanofiltration system；
Concentrated water room, freshwater room are equipped with inside the nanofiltration system and between the concentrated water room and the freshwater room
Nanofiltration membrane.
It is further improved as the utility model, is connected with concentrate between the concentrated water room and softening pond top
Reflux line, the nanofiltration system are connected to by the concentrate reflux line with the softening pond.
It further improves as the utility model, is connected between the second spoil disposal pipeline and softening pond top
Crystal seed reflux line.
It is further improved as the utility model, the first agitating device is equipped with inside the softening pond.
It is further improved as the utility model, the second agitating device is equipped with inside the coagulating basin.
It is further improved as the utility model, the softening medicament launched in the first medicament delivery pipeline is oxalic acid
Sodium.
It is further improved as the utility model, it is calcium oxalate that the crystal seed, which launches the crystal seed launched in pipeline,.
It is further improved as the utility model, it is coagulant that the second medicament, which launches the medicament launched in pipeline,.
The utility model has the following beneficial effects:
1. having recycled the oxalate denominationby being excessively added, the injected volume and cost of softening medicament are reduced.
2. being concentrated and having recycled the sulfate ion in waste water, Ca in softening pond can promote2+Sedimentation, further drop
The injected volume and cost of low softening medicament.
3. can be by the Ca in high-salt wastewater2+Selective Separation is having substantially no effect on Mg2+It is under the premise of concentration that waste water is soft
Change.
4. relative to by Ca2+And Mg2+The softening process being all removed reduces sediment production quantity and softening medicament
Injected volume and cost.
5. solving suspended matter contained by waste water and foulant CaSO in subsequent embrane method treatment process4Equipment is influenced to operate normally
The problem of.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of high-salt wastewater softening plant described in the utility model embodiment.
In figure,
1, conditioning tank；2, soften pond；3, coagulating basin；4, clarifying basin；5, the first agitating device；6, the second agitating device；7,
First spoil disposal pipeline；8, crystal seed reflux line；9, the second spoil disposal pipeline；10, crystal seed launches pipeline；11, the first medicament delivery pipe
Road；12, second medicament launches pipeline；13, microfiltration systems；14, microfiltration equipment；15, nanofiltration system；16, concentrate reflux line；
17, concentrated water room；18, freshwater room.
Specific embodiment
Below by specific embodiment and in conjunction with attached drawing, the utility model is further described in detail.
As shown in Figure 1, a kind of high-salt wastewater softening plant of the utility model embodiment, including the tune being sequentially communicated from beginning to end
Save pond 1, softening pond 2, coagulating basin 3, clarifying basin 4, microfiltration systems 13 and nanofiltration system 15.
1 bottom of conditioning tank is connected with the first spoil disposal pipeline 7, and the suspended matter settled in high-salt wastewater in conditioning tank 1 passes through the
The discharge of one spoil disposal pipeline 7.
The crystal seed for launching crystal seed is connected at the top of softening pond 2 to launch pipeline 10 and soften the first of medicament for launching
Medicament delivery pipeline 11.Crystal seed can be selected as calcium oxalate, and softening medicament can be selected as sodium oxalate, and after adding sodium oxalate, control is heavy
The molar concentration for dropping waste water mesoxalic acid sodium is Ca2+1-2 times of molar concentration.Softening 2 bottom of pond is connected with the second spoil disposal pipeline 9,
Soften the sediment inside pond 2 to be discharged by the second spoil disposal pipeline 9.Further, soften and be equipped with the first agitating device inside pond 2
5, it can be promoted in softening pond 2 by the first agitating device 5 and soften reaction efficiency.
It is connected with the second medicament for launching coagulated agent at the top of coagulating basin 3 and launches pipeline 12.Coagulated agent is can
It generates the flocculant for stablizing floccule and auxiliary improves the flocculation aid of coagulation effect.3 bottom of coagulating basin is connected to the second spoil disposal pipeline
9, the sediment inside coagulating basin 3 passes through the second spoil disposal pipeline 9 and is discharged.Further, the second stirring dress is equipped with inside coagulating basin 3
6 are set, the coagulation speed of suspended matter in 3 internal softening waste water of coagulating basin can be accelerated by the second agitating device 6.
4 bottom of clarifying basin is connected to the second spoil disposal pipeline 9, and the sediment inside clarifying basin 4 passes through 9 row of the second spoil disposal pipeline
Out.
Microfiltration equipment 14 is equipped with inside microfiltration systems 13, and microfiltration equipment 14 is connected to nanofiltration system 15, microfiltration equipment 14
Small suspended matter and particulate matter etc. are separated by filtration, micro-filtration is obtained and produces water, micro-filtration produces water and enters nanofiltration system 15.
Concentrated water room 17, freshwater room 18 and receiving between concentrated water room 17 and freshwater room 18 are equipped with inside nanofiltration system 15
Filter membrane, most of divalent ion (including oxalate denominationby C2O4 2-With sulfate ion SO4 2-Deng) concentrated water is retained in by nanofiltration membrane
In room 17, nanofiltration concentrate is formed, most of moisture and monovalent ion enter freshwater room 18 by nanofiltration membrane, obtain nanofiltration and produce
Water.
Further, it is connected with concentrate reflux line 16 between 2 top of concentrated water room 17 and softening pond, nanofiltration system 15 is logical
Concentrate reflux line 16 is crossed to be connected to softening pond 2.Concentrate in concentrated water room 17 contains sulfate ion and is excessively added
Oxalate denominationby, concentrated liquid reflux line 16 return to softening pond 2, and oxalate denominationby can be used as softening medicament and recycle, sulphur
Acid ion can promote Ca2+Sedimentation.
Further, it is connected with crystal seed reflux line 8 between 2 top of the second spoil disposal pipeline 9 and softening pond, is produced from softening pond 2
Raw partly precipitated object returns in softening pond 2 through the second spoil disposal pipeline 9 and crystal seed reflux line 8, as supplement crystal seed.
High-salt wastewater softening is carried out based on above-mentioned high-salt wastewater softening plant, comprising the following steps:
Step 1, high-salt wastewater enters conditioning tank 1, and setting hydraulic detention time is 1~6 hour, and high-salt wastewater flow is adjusted
Section is stablized, and the partial suspended thing in high-salt wastewater is settled down to the bottom of pond of conditioning tank 1, and is discharged by the first spoil disposal pipeline 7, conditioning tank
Sedimentation waste water is obtained inside 1.
Step 2, sedimentation waste water enters softening pond 2, adds softening medicine into softening pond 2 from the first medicament delivery pipeline 11
Agent, preferably sodium oxalate accelerate softening reaction speed by the first agitating device 5, will settle the Ca in waste water2+Precipitating, adds
After sodium oxalate, the molar concentration of control settlement waste water oxalate is Ca2+1-2 times of molar concentration.In order to improve precipitation and separation
Effect, while pipeline 10 is launched from crystal seed and adds crystal seed, preferably calcium oxalate, control crystal seed and sedimentation waste water into softening pond 2
Mass ratio be 2 ‰ -5 ‰, setting hydraulic detention time be 1~2 hour, sediment is discharged by the second spoil disposal pipeline 9, soften pond
Softening waste water is obtained inside 2.Meanwhile softening the partly precipitated object of the generation of pond 2 by the second spoil disposal pipeline 9 and crystal seed reflux line 8
Softening pond 2 is returned to, as supplement crystal seed.
Step 3, softening waste water enters coagulating basin 3, launches the dosing coagulant into coagulating basin 3 of pipeline 12 from second medicament,
Accelerate the coagulation speed of suspended matter in softening waste water by the second agitating device 6, sediment is discharged by the second spoil disposal pipeline 9, is mixed
Coagulation waste water is obtained inside solidifying pond 3.
Step 4, coagulation waste water enters clarifying basin 4, and sediment is further by sedimentation separation, and by 9 row of the second spoil disposal pipeline
Out, clarified wastewater is obtained inside clarifying basin 4.
Step 5, clarified wastewater enters microfiltration systems 13, small suspended matter and particulate matter by the filtering point of microfiltration equipment 14
From, obtain micro-filtration produce water.
Step 6, micro-filtration production water enters nanofiltration system 15, and most of divalent ion is retained in concentrated water room 17 by nanofiltration membrane,
Nanofiltration concentrate is formed, the concentrate in concentrated water room 17 returns to softening pond 2 by concentrate reflux line 16, due to containing in concentrate
The oxalate denominationby for having sulfate ion and being excessively added, wherein oxalate denominationby is recycled as softening medicament, sulfate radical
Ion promotes Ca2+Precipitating, remaining most of moisture and monovalent ion enter freshwater room 18 by nanofiltration membrane, obtain nanofiltration production
Water, as system produce water.
The high-salt wastewater softening plant of the utility model can be by the Ca in high-salt wastewater2+Selective Separation, in not shadow substantially
Ring Mg2+Waste water is softened under the premise of concentration.Using the high-salt wastewater softening plant of the utility model, relative to by Ca2+And Mg2 +The softening process being all removed, the injected volume and cost for reducing sediment production quantity, softening medicament are returned by concentrate
Flow tube road has recycled the oxalate denominationby being excessively added, and further reduced the injected volume and cost of softening medicament, simultaneously
The sulfate ion in waste water is concentrated and recycled by concentrate reflux line, can promote Ca in softening pond2+Sedimentation,
Further reduce the injected volume and cost of softening medicament.In addition, the high-salt wastewater softening plant of the utility model is combined
Microfiltration systems 13 and nanofiltration system 15, solve waste water contained suspended matter and foulant in subsequent embrane method treatment process
CaSO4Influence the problem of equipment operates normally.
The above descriptions are merely preferred embodiments of the present invention, is not intended to limit the utility model, for this
For the technical staff in field, various modifications and changes may be made to the present invention.It is all in the spirit and principles of the utility model
Within, any modification, equivalent replacement, improvement and so on should be included within the scope of protection of this utility model.
Claims (8)
1. a kind of high-salt wastewater softening plant, which is characterized in that including be sequentially communicated from beginning to end conditioning tank (1), softening pond (2),
Coagulating basin (3), clarifying basin (4), microfiltration systems (13) and nanofiltration system (15)；
Conditioning tank (1) bottom is connected with the first spoil disposal pipeline (7)；
It is connected with crystal seed at the top of the softening pond (2) and launches pipeline (10) and the first medicament delivery pipeline (11), the softening pond
(2) bottom is connected with the second spoil disposal pipeline (9)；
It is connected with second medicament at the top of the coagulating basin (3) and launches pipeline (12), coagulating basin (3) bottom is connected to described second
Spoil disposal pipeline (9)；
Clarifying basin (4) bottom is connected to the second spoil disposal pipeline (9)；
Microfiltration equipment (14) are equipped with inside the microfiltration systems (13), and the microfiltration equipment (14) and the nanofiltration system (15)
Connection；
It is equipped with concentrated water room (17), freshwater room (18) inside the nanofiltration system (15) and is located at the concentrated water room (17) and described
Nanofiltration membrane between freshwater room (18).
2. high-salt wastewater softening plant according to claim 1, which is characterized in that the concentrated water room (17) and the softening
It is connected with concentrate reflux line (16) between at the top of pond (2), the nanofiltration system (15) passes through the concentrate reflux line
(16) it is connected to the softening pond (2).
3. high-salt wastewater softening plant according to claim 1, which is characterized in that the second spoil disposal pipeline (9) and institute
It states between at the top of softening pond (2) and is connected with crystal seed reflux line (8).
4. high-salt wastewater softening plant according to claim 1, which is characterized in that be equipped with the inside the softening pond (2)
One agitating device (5).
5. high-salt wastewater softening plant according to claim 1, which is characterized in that be equipped with the inside the coagulating basin (3)
Two agitating devices (6).
6. high-salt wastewater softening plant according to claim 1, which is characterized in that the first medicament delivery pipeline (11)
The softening medicament of interior dispensing is sodium oxalate.
7. high-salt wastewater softening plant according to claim 1, which is characterized in that the crystal seed is launched in pipeline (10) and thrown
The crystal seed put is calcium oxalate.
8. high-salt wastewater softening plant according to claim 1, which is characterized in that the second medicament launches pipeline (12)
The medicament of interior dispensing is coagulant.
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607867A (en) * | 2018-12-28 | 2019-04-12 | 大唐环境产业集团股份有限公司 | A kind of high-salt wastewater softening plant and method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN109607867A (en) * | 2018-12-28 | 2019-04-12 | 大唐环境产业集团股份有限公司 | A kind of high-salt wastewater softening plant and method |
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