CN207811506U - Circulating water effluent purifies reutilization system - Google Patents
Circulating water effluent purifies reutilization system Download PDFInfo
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- CN207811506U CN207811506U CN201721691178.0U CN201721691178U CN207811506U CN 207811506 U CN207811506 U CN 207811506U CN 201721691178 U CN201721691178 U CN 201721691178U CN 207811506 U CN207811506 U CN 207811506U
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- biofilter
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- circulating water
- purifies
- reaction tank
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Abstract
The utility model provides a kind of Circulating water effluent purification reutilization system, and removal carbonate hardness reaction tank is communicated with removal non-carbonate hardness reaction tank；Removal non-carbonate hardness reaction tank is communicated with the entrance of mechanical accelerating purifying pool；The outlet of clarifying basin catch basin is communicated with intermediate pool；Biofilter includes biofilter water inlet pipe, bearing plate, several filter caps, aerator and biofilter catch basin；Intermediate pool is connected to biofilter water inlet pipe；Bearing plate is arranged in the top of biofilter water inlet pipe；There are several trepannings, filter cap to be arranged on bearing plate in trepanning；The aerated conduit of aerator is arranged above bearing plate；Object filter tank catch basin is arranged in the both sides on biofilter top.It the advantage is that realization water demineralization, accelerate the degradation under clarification and biofilter synergy；Treated, and water is finally back to circulation, achievees the purpose that water-saving reuse.
Description
Technical field
The utility model is related to a kind of water treatment facilities, more particularly to a kind of Circulating water effluent purifies reutilization system.
Background technology
Recirculated water is as a kind of Industrial Water Saving measure, and widely used in many chemical plant, power plant, water consumption accounts for about entirely
70% or more of industrial water consumption.
Recirculated water is mainly used to condensed steam, cooling product or equipment, if cooling effect is poor, will influence production effect
The quality of rate, the yield and product that make product declines, and can even cause production accident.
For the using water wisely of maximum possible, the cycles of concentration operation for improving recirculated water as far as possible is needed, but with dense
The raising of demagnification number, fouling in water circulation system and corrosion factor more rely on water quality stabilizer, sterilization also with rising at double
In the use of the medicaments such as agent.Improving cycles of concentration too much can also be such that medicament (such as Quadrafos) stops in cooling water system
The time is stayed to increase and hydrolyze.
It is mainly led to the problem of in recirculated water operational process：
(1) incrustation scale：Since recirculated water constantly evaporates in cooling procedure, so that salt concentration in water is constantly increased, be more than
The solubility of certain salts and precipitate.It common are the dirts such as calcium carbonate, calcium phosphate, magnesium silicate.The quality of incrustation scale is dense, greatly
Big reduces heat transfer efficiency, and 0.6 millimeter of dirt is thick just to make heat transfer coefficient reduce 20%.
(2) dirt：Dirt is mainly made of organic matter, microbe colony and secretion, silt, the dust etc. in water, dirt
Quality it is soft, not only reduce heat transfer efficiency but also cause underdeposit corrosion, shorten service life of equipment.
(3) corrode：The corrosion of recirculated water heat exchanging equipment, mainly couple corrosion, Producing reason have device fabrication to lack
It falls into, the dirt that the mucus of corrosive ion (Cl-, Fe2+, Cu2+) and microorganism secretion is generated in oxygen gas and water sufficient in water
The consequence of the factors such as dirt, corrosion is extremely serious, even if uncontrolled extremely short time heat exchanger, hydraulic pipeline equipment scrapping.
(4) microorganism viscosity mud：Because being well suited for dissolved with sufficient oxygen, suitable temperature and rich foster condition in recirculated water
The growth and breeding of microorganism, such as control will rapidly result in water quality deterioration, smelly, blackening not in time, and cooling tower largely sticks dirt deposition
It even blocks, cooling and cooling effect declines to a great extent, equipment corrosion aggravation.Therefore circulating water treatment must control the numerous of microorganism
It grows.
For these for solving the problems, such as to generate in recirculated water operational process, in addition to adding a certain amount of water quality stabilizer, killing
The control of the medicaments such as microbial inoculum is outer, and circulation needs discharge part sewage and supplements new water quality.
Conventional Circulating water effluent water treatment technology includes：It is filtered off by laminated filter and is back to use recirculated water after removing part SS
System, the total hardness in ion exchange resin removal draining, acid adding processing, control PH7.5-8, electrodialysis or reverse osmosis desalination.
Electro-adsorption demineralization：Electrostatic field is formed by applying applied voltage, ion is forced to be moved at the electrode of opposite charges,
The charge and discharge of electric double layer are controlled, the ion concentration at electric double layer is changed, and are allowed to be different from bulk concentration.To realize
To the desalination of aqueous solution.The shortcomings that technology is that cost of investment is higher, causes operating cost higher.
Electrodialytic technique：Electrodialysis be under the action of applying direct current electric field, using the selective penetrated property of amberplex,
Make ion from the physical and chemical process moved in a part of water in another part water.Its major defect is to oils, solid etc.
It requires, equipment will produce dirt, need periodic cleaning, equipment replacement period short.
It is reverse osmosis:Reverse osmosis operation principle is to apply operating pressure in water inlet (concentrated solution) side to overcome naturally osmotic
Pressure.When the operating pressure higher than naturally osmotic pressure is applied to concentrated solution side, the flow direction of hydrone naturally osmotic will be inverse
Turn, water is produced in the purification that the moisture subdivision in water inlet (concentrated solution) becomes weak solution side by film.But the technology is to inflow requirement
It is more harsh.COD≤40mg/l, oil≤0.1mg/l, SDI≤3 are especially required in reusing sewage.And equipment cost is higher, fortune
Row cost is also very high.
Filter by laminated filter:Laminated filtering mainly removes the SS impurity in draining.When flow passes through filtered water inlet mouth
When filtering lamination in into filter, filtering lamination is tightly compressed under the action of spring force and waterpower, impurity
Grain is trapped within lamination crosspoint, and the water by filtering is flowed out from filter main channel.It is more and more with the particle of retention,
The pressure difference of Inlet and outlet water is increasing, when reach setting pressure difference when, filter switch valve, using filtered clear water to lamination into
Row backwash is drained into sewage disposal system processing after cleaning.A kind of its auxiliary controlled generally as circulating water quality,
Continuous filtration treatment is carried out to the part water quality in entire recirculated water, it is general to filter the 5-10% that water is entire recirculated water.With
Particle concentration in control loop water.Due to the characteristic of its object, the dissolubility calcium ions and magnesium ions in water body are not appointed
What practical removal effect.
Ion exchange resin:Ion exchange resin make mainly use ion-exchange process, in water be in ionic state sun,
Anion removes.For main application in the deep desalting treatment of draining, processing cost is higher, and the ion exchanged still needs
Evaporative crystallization or the outer waste water system that is discharged into is wanted to increase waste water treatment system processing load.
Acid adding processing：Control loop water PH7.5-8, water quality have lower crystallization trend at lower PH.It can only
It, cannot be really as the drainage sunk well mode of recirculated water as the supplement of cycle water management.Because with regard to acid adding processing itself
Speech, is only reduction of the pH value of water body, there is no any removals for the polluter in water body.
Utility model content
A kind of Circulating water effluent of the offer of the utility model purifies reutilization system, for using lime soda ash as raw material
Water demineralization, under mechanical agitation under the mechanical accelerating purifying of waste water and ozone, biological aerated filter synergy
Oxidation operation degradation, biodegradable and SS filtering；Prior art problem is solved, to overcome the deficiencies of existing technologies.
The utility model provides a kind of Circulating water effluent purification reutilization system, including：Removal carbonate hardness reaction tank,
Remove non-carbonate hardness reaction tank, mechanical accelerating purifying pool, intermediate pool and biofilter；Remove carbonate hardness reaction tank with
Removal non-carbonate hardness reaction tank communicates；Removal non-carbonate hardness reaction tank is communicated with the entrance of mechanical accelerating purifying pool；
The outlet of clarifying basin catch basin is communicated with intermediate pool；Biofilter include biofilter water inlet pipe, bearing plate, several filter caps,
Aerator and biofilter catch basin；Intermediate pool is connected to biofilter water inlet pipe；Bearing plate setting is intake in biofilter
The top of pipe；There are several trepannings, filter cap to be arranged on bearing plate in trepanning；The aerated conduit setting of aerator is being set off
Above plate；Object filter tank catch basin is arranged in the both sides on biofilter top.
Further, the utility model provides a kind of Circulating water effluent purification reutilization system, can also have such spy
Sign：Biofilter is ozone-biological aerated filter, and aerator is passed through ozone.
Further, the utility model provides a kind of Circulating water effluent purification reutilization system, can also have such spy
Sign：Aerator further includes the air storage chamber being arranged outside biofilter, oxygen produced chamber and ozone generator；The outlet of air storage chamber and system
The entrance of oxygen room connects, and the outlet of oxygen room processed and the entrance of ozone generator connect, the outlet of ozone generator and aeration tube
Road connects；Compressed air from the import of air storage chamber enter, be passed through oxygen produced chamber and carry out oxygen processed, then be transported to ozone generator prepare it is smelly
Oxygen, then be transported in aerated conduit.
Further, the utility model provides a kind of Circulating water effluent purification reutilization system, can also have such spy
Sign：Further include stone bed course, is arranged on the aerated conduit of aerator.
Further, the utility model provides a kind of Circulating water effluent purification reutilization system, can also have such spy
Sign：Further include haydite, is arranged on stone bed course.
Further, the utility model provides a kind of Circulating water effluent purification reutilization system, can also have such spy
Sign：It further include back purge system；Back purge system is connect with biofilter water inlet pipe.
Further, the utility model provides a kind of Circulating water effluent purification reutilization system, can also have such spy
Sign：Mechanical accelerating purifying pool includes lower layer's reative cell and upper layer reative cell；Removal non-carbonate hardness reaction tank is reacted with lower layer
Room communicates；The top of lower layer's reative cell is communicated with the bottom of upper layer reative cell.
Further, the utility model provides a kind of Circulating water effluent purification reutilization system, can also have such spy
Sign：Further include lower layer's charge pipe and upper layer charge pipe；Lower layer's charge pipe is inserted into lower layer's reative cell；It is anti-that upper layer charge pipe is inserted into upper layer
Answer interior.
Further, the utility model provides a kind of Circulating water effluent purification reutilization system, can also have such spy
Sign：Lower layer's charge pipe adds ferrous sulfate；Upper layer charge pipe adds polyacrylamide.
The utility model provides a kind of Circulating water effluent purification reutilization system, water demineralization, machine in conjunction with lime soda ash
SS clarifications, the ozone oxidation of organic matter, biological treatment and secondary filter under tool acceleration is in one, the final reuse of water that treated
In circulation, achieve the purpose that water-saving reuse.
Description of the drawings
Fig. 1 is the structural schematic diagram of Circulating water effluent purification reutilization system.
Fig. 2 is the structural schematic diagram of ozone-biological aerated filter.
Specific implementation mode
The utility model is further described in the following with reference to the drawings and specific embodiments.
Fig. 1 is the structural schematic diagram of Circulating water effluent purification reutilization system.
As shown in Figure 1, Circulating water effluent purifies reutilization system, including：Inlet water lifting pumps 01, the first reaction tank 10,
Two reaction tanks 20, mechanical accelerating purifying pool 30, intermediate pool 40 and ozone-biological aerated filter (O3-BAF) 50.
Recirculated water draining squeezes into the first reaction tank 10 by inlet water lifting pumps 01.First reaction tank 10 is that removal carbonate is hard
Spend (Ca (HCO3)2、Mg(HCO3)2Deng) reaction tank, addition calcium hydroxide (Ca (OH)2).The first stirring of first reaction tank 10 setting
Machine 11 carries out mechanical agitation to pond body, to ensure that liquid is sufficiently mixed with processing water.
Second reaction tank 20 is communicated with the first reaction tank 10.Second reaction tank 20 is removal non-carbonate hardness (CaSO4、
MgSO4、CaCl2、MgCl2、Ca(NO3)2、Mg(NO3)2Deng) reaction tank, addition sodium carbonate (Na2CO3).Second reaction tank 20 is arranged
Second blender 21 carries out mechanical agitation to pond body, to ensure that liquid is sufficiently mixed with processing water.
Mechanical accelerating purifying pool 30 includes：Clarifying basin water inlet pipe 31, lower layer's reative cell 32, upper layer reative cell 33, deflector
34, clarifying basin catch basin 35, stirring elevator 36, enriched chamber 37, lower layer's charge pipe 38 and upper layer charge pipe 39.
One end of clarifying basin water inlet pipe 31 is communicated with the second reaction tank 20, and the other end is communicated with lower layer reative cell 32.Lower layer
33 top of reative cell is umbrella shape, is made of umbrella shape plate 331.The bottom of lower layer's reative cell 33 is infundibulate, in funnel shaped bottom
Lower layer's dredge pump 332 is set.
The top of lower layer's reative cell 32 is communicated with the bottom of upper layer reative cell 33.Deflector 34 is arranged in upper layer reative cell 33
Outside.Deflector 34 is in the top of umbrella shape plate 331.Clarifying basin catch basin 35 is arranged in the outside of deflector 34.
The outside setting concentration baffle 371 of umbrella shape plate 331, forms enriched chamber 37.The bottom setting concentration row of enriched chamber 37
Dirt pump 372.
Lower layer's charge pipe 38 passes through umbrella shape plate 331, is inserted into lower layer's reative cell 32.Lower layer's charge pipe 38 adds ferrous sulfate
(FeSO4).Upper layer charge pipe 39 is inserted into upper layer reative cell 33, adds polyacrylamide (PAM).The setting of elevator 36 is stirred to exist
In lower layer's reative cell 32 and upper layer reative cell 33.
Water after second reaction tank, 20 confection enters lower layer's reative cell 32, with lower layer by clarifying basin water inlet pipe 31
Ferrous sulfate (the FeSO that charge pipe 38 is added4) mixing.Stirring elevator 36 act under, processing water also with upper layer charge pipe 39
The polyacrylamide (PAM) of addition mixes, and increases the chance of particles collision, improves coagulation effect.By the clear water of separation
It ramps up, after the outer wall for flowing through upper layer reative cell 33, is passing through deflector 34, flowing into catch basin 35.The body refuse part avaled is again
Reflux is reacted with dosing raw water mechanical mixture, is deposited on 32 bottom of lower layer's reative cell, can be excluded through lower layer's dredge pump 332.Part
After then concentrated room 37 concentrates, periodically discharged from concentration dredge pump 372.
Clarifying basin catch basin 35 is communicated with intermediate pool 40, and the clear water separated flows into intermediate pool from clarifying basin catch basin 35
40.Intermediate pool 40 has intermediate pool immersible pump 41, and the water in intermediate pool 40 is got to ozone-biological aerated filter (O3-BAF) 50
In.
Ozone-biological aerated filter (O3-BAF) 50 includes：Biofilter water inlet pipe 51, bearing plate 52, several filter caps
53, aerator 54, stone bed course 55, haydite 56, biofilter catch basin 57 and back purge system 58.
Biofilter water inlet pipe 51 is arranged in the bottom of ozone-biological aerated filter (O3-BAF) 50, and water distribution is uniform.It is raw
Object filter tank water inlet pipe 51 is connected to intermediate pool 40, flows into the clear water in intermediate pool 40.The setting of bearing plate 52 is intake in biofilter
The top of pipe 51 is used to support the cobblestone and haydite 56 of the stone bed course 55 that top is accumulated.Uniform pore openings on bearing plate 52, if
Dry filter cap 53 is arranged in the trepanning of bearing plate 52, prevents haydite from being fallen from top and buries the water distribution pipe of lower section.
The aerated conduit of aerator 54 is arranged above bearing plate 52.Aerator 54 further includes being arranged in ozone-exposure
Air storage chamber 541, oxygen produced chamber 542 outside gas biofilter (O3-BAF) 50 and ozone generator 543.The outlet of air storage chamber 541 with
The entrance of oxygen produced chamber 542 connects, and the outlet of oxygen room 542 processed is connect with the entrance of ozone generator 543, ozone generator 543
Outlet connect with aerated conduit.Compressed air enters from the import of air storage chamber 541, is passed through oxygen produced chamber 542 and carries out oxygen processed, then is defeated
It is sent to ozone generator 543 and prepares ozone, be finally delivered to aerated conduit.The ozone one side direct oxidation of aerator 54 point
Solve partial organic substances matter；On the other hand as aeration air source, ensure gas shearing and the souring under biosystem.
Stone bed course 55 is arranged on the aerated conduit of aerator 54.Haydite 56 is arranged on stone bed course 55.Biofilter
Catch basin 57 is arranged in the both sides on 50 top of ozone-biological aerated filter (O3-BAF).Back purge system 58 and biofilter into
Water pipe 51 is connected, and after ozone-biological aerated filter (O3-BAF) 50 runs a period of time, is periodically filtered to ozone-aeration and biological
Pond (O3-BAF) 50 is backwashed with the impurity such as SS inside removing.
Layer of the clear water through filter cap 53, aerator 54, stone bed course 55, haydite 56 entered from biofilter water inlet pipe 51
After layer filtration treatment, the overflow of waste water above flows into reuse after biofilter catch basin 57.
Claims (9)
1. a kind of Circulating water effluent purifies reutilization system, it is characterised in that：Including removal carbonate hardness reaction tank, removal
Non-carbonate hardness reaction tank, mechanical accelerating purifying pool, intermediate pool and biofilter；
Wherein, the removal carbonate hardness reaction tank is communicated with the removal non-carbonate hardness reaction tank；
The removal non-carbonate hardness reaction tank is communicated with the entrance of the mechanical accelerating purifying pool；
The outlet of the clarifying basin catch basin is communicated with the intermediate pool；
The biofilter includes that biofilter water inlet pipe, bearing plate, several filter caps, aerator and biofilter are catchmented
Slot；
The intermediate pool is connected to the biofilter water inlet pipe；The bearing plate is arranged in the upper of the biofilter water inlet pipe
Side；There are several trepannings, the filter cap to be arranged on the bearing plate in the trepanning；The aerated conduit of the aerator
It is arranged above the bearing plate；The both sides on the biofilter top are arranged in object filter tank catch basin.
2. Circulating water effluent as described in claim 1 purifies reutilization system, it is characterised in that：Wherein, the biofilter
For ozone-biological aerated filter, the aerator is passed through ozone.
3. Circulating water effluent as claimed in claim 2 purifies reutilization system, it is characterised in that：Wherein, the aerator
Further include the air storage chamber being arranged outside biofilter, oxygen produced chamber and ozone generator；
The outlet of the air storage chamber is connect with the entrance of the oxygen produced chamber, outlet and the ozone generator of the oxygen room processed
Entrance connection, the outlet of the ozone generator is connect with the aeration tube road；Import of the compressed air from the air storage chamber
Into being passed through the oxygen produced chamber and carry out oxygen processed, then be transported to the ozone generator and prepare ozone, then be transported to the aeration tube
In road.
4. Circulating water effluent as described in claim 1 purifies reutilization system, it is characterised in that：Further include stone bed course, setting
On the aeration tube road of the aerator.
5. Circulating water effluent as claimed in claim 4 purifies reutilization system, it is characterised in that：Further include haydite, setting exists
On the stone bed course.
6. Circulating water effluent as described in claim 1 purifies reutilization system, it is characterised in that：It further include back purge system；
The back purge system is connect with the biofilter water inlet pipe.
7. Circulating water effluent as described in claim 1 purifies reutilization system, it is characterised in that：Wherein, mechanical accelerating purifying
Pond includes lower layer's reative cell and upper layer reative cell；
The removal non-carbonate hardness reaction tank is communicated with lower layer's reative cell；
The top of lower layer's reative cell is communicated with the bottom of the upper layer reative cell.
8. Circulating water effluent as claimed in claim 7 purifies reutilization system, it is characterised in that：Further include lower layer's charge pipe and
Upper layer charge pipe；
Lower layer's charge pipe is inserted into lower layer's reative cell；The upper layer charge pipe is inserted into the upper layer reative cell.
9. Circulating water effluent as claimed in claim 8 purifies reutilization system, it is characterised in that：Wherein, lower layer's charging
Pipe adds ferrous sulfate；The upper layer charge pipe adds polyacrylamide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721691178.0U CN207811506U (en) | 2017-12-07 | 2017-12-07 | Circulating water effluent purifies reutilization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721691178.0U CN207811506U (en) | 2017-12-07 | 2017-12-07 | Circulating water effluent purifies reutilization system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207811506U true CN207811506U (en) | 2018-09-04 |
Family
ID=63335286
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721691178.0U Active CN207811506U (en) | 2017-12-07 | 2017-12-07 | Circulating water effluent purifies reutilization system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207811506U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109111057A (en) * | 2018-10-19 | 2019-01-01 | 江苏道科环境科技有限公司 | A kind of biological deodorizing device that Sprayer Circulation water mixes automatically |
| CN111348756A (en) * | 2020-04-01 | 2020-06-30 | 广西广宇水资源技术开发有限公司 | Process for removing temporary hardness of water by chemical reaction |
-
2017
- 2017-12-07 CN CN201721691178.0U patent/CN207811506U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109111057A (en) * | 2018-10-19 | 2019-01-01 | 江苏道科环境科技有限公司 | A kind of biological deodorizing device that Sprayer Circulation water mixes automatically |
| CN109111057B (en) * | 2018-10-19 | 2023-12-12 | 江苏道科环境科技有限公司 | Biological deodorization device capable of automatically mixing spraying circulating water |
| CN111348756A (en) * | 2020-04-01 | 2020-06-30 | 广西广宇水资源技术开发有限公司 | Process for removing temporary hardness of water by chemical reaction |
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