CN208586173U - Fiber industrial water circulator and system - Google Patents
Fiber industrial water circulator and system Download PDFInfo
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- CN208586173U CN208586173U CN201820351216.6U CN201820351216U CN208586173U CN 208586173 U CN208586173 U CN 208586173U CN 201820351216 U CN201820351216 U CN 201820351216U CN 208586173 U CN208586173 U CN 208586173U
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- 239000008235 industrial water Substances 0.000 title claims abstract description 36
- 239000000835 fiber Substances 0.000 title claims abstract description 28
- 239000010865 sewage Substances 0.000 claims abstract description 78
- 238000012545 processing Methods 0.000 claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 229920000742 Cotton Polymers 0.000 claims abstract description 20
- 238000004062 sedimentation Methods 0.000 claims abstract description 16
- 230000003750 conditioning effect Effects 0.000 claims abstract description 15
- 238000001914 filtration Methods 0.000 claims abstract description 14
- 230000001954 sterilising effect Effects 0.000 claims abstract description 10
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 10
- 230000015271 coagulation Effects 0.000 claims abstract description 7
- 238000005345 coagulation Methods 0.000 claims abstract description 7
- 238000005188 flotation Methods 0.000 claims abstract description 6
- 230000008859 change Effects 0.000 claims abstract description 5
- 238000005273 aeration Methods 0.000 claims description 71
- 239000010802 sludge Substances 0.000 claims description 67
- 238000005192 partition Methods 0.000 claims description 63
- 230000003197 catalytic effect Effects 0.000 claims description 52
- 230000003647 oxidation Effects 0.000 claims description 52
- 238000007254 oxidation reaction Methods 0.000 claims description 52
- 230000003139 buffering effect Effects 0.000 claims description 39
- 238000004891 communication Methods 0.000 claims description 32
- 238000010992 reflux Methods 0.000 claims description 14
- 239000000126 substance Substances 0.000 claims description 13
- 238000003860 storage Methods 0.000 claims description 12
- 238000005276 aerator Methods 0.000 claims description 11
- 230000018044 dehydration Effects 0.000 claims description 11
- 238000006297 dehydration reaction Methods 0.000 claims description 11
- 239000012223 aqueous fraction Substances 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 238000005868 electrolysis reaction Methods 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 229910052698 phosphorus Inorganic materials 0.000 claims description 3
- 239000011574 phosphorus Substances 0.000 claims description 3
- 238000004064 recycling Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 18
- 238000006243 chemical reaction Methods 0.000 abstract description 7
- 239000002957 persistent organic pollutant Substances 0.000 abstract description 5
- 238000000034 method Methods 0.000 description 9
- 230000008569 process Effects 0.000 description 8
- 239000007788 liquid Substances 0.000 description 6
- 230000015556 catabolic process Effects 0.000 description 5
- 238000006731 degradation reaction Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 239000005416 organic matter Substances 0.000 description 5
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 239000000975 dye Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000020477 pH reduction Effects 0.000 description 3
- 150000003384 small molecules Chemical class 0.000 description 3
- 239000004094 surface-active agent Substances 0.000 description 3
- 230000007704 transition Effects 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000007380 fibre production Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 239000004753 textile Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000003721 gunpowder Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model provides a kind of fiber industrial water circulator and system, it is related to technical field of sewage, to solve since a large amount of sewage can be generated in cotton processing, the sewage has the characteristics that water is big, organic pollutant content is high, coloration is deep, change of water quality is big, and the technical issues for the treatment of effect should be had by being not achieved using traditional processing mode.It is related to a kind of fiber industrial water circulator, comprising: filtering ponds, filtering ponds are interior to be equipped with grid component, and filtering ponds have been sequentially communicated conditioning tank, anaerobic pond, multi-stage biological processing pond, coagulation reaction tank, sedimentation basin, sterilization pool, flotation tank and reuse tank.Further relate to a kind of industrial water circulatory system, comprising: above-mentioned fiber industrial water circulator.The fiber industrial water circulator and system can preferably handle sewage, reach the standard of reuse and discharge.
Description
Technical field
The utility model relates to technical field of sewage, more particularly, to a kind of fiber industrial water circulator and are
System.
Background technique
Cotton is the strategic materials to involve the interests of the state and the people, and is only second to the second largest crops of grain.Cotton is to be related to
The commodity of agricultural and the big industry of textile industry two are the main sources of more than the 100000000 cotton grower's incomes in the whole nation, are the main originals of textile industry
The daily necessities of material and numerous people, the important goods that cotton yarn, cotton and clothes are still exported goods and earned foreign currency.Cotton can be with
For the cord, gunpowder and pharmaceutical cotton etc. for manufacturing tire etc..Therefore, production, circulation, processing and the consumption of cotton, with people
The life of the people masses and the interests of numerous cotton growers are closely bound up, also have an important influence to the development of national economy.
Cotton after picking needs the manufacturing procedure complicated by some column, which includes: to smash, be modified, taking off
Water, drying and packing etc., the cotton after packing, which directly can be sold or be sent to, to continue to process it at subsequent processing
Processing.
However, a large amount of sewage can be generated in its process for the processing technology of above-mentioned cotton, sewage tool
There is the features such as water is big, organic pollutant content is high, coloration is deep, change of water quality is big, is not achieved using traditional processing mode and is answered
Some treatment effects.If the sewage direct emission not only has adverse effect on environment, but also for rare water resource
For be also very big waste.
Utility model content
The first of the utility model is designed to provide a kind of fiber industrial water circulator, to solve to add due to cotton
A large amount of sewage can be generated during work, the sewage is big with water, organic pollutant content is high, coloration is deep, change of water quality is big
The features such as, the technical issues for the treatment of effect should be had by being not achieved using traditional processing mode.
Fiber industrial water circulator provided by the utility model, comprising: the filtering ponds being connected to Sewage outlet, institute
It states and is equipped with grid component in filtering ponds, the filtering ponds have been sequentially communicated conditioning tank, anaerobic pond, multi-stage biological processing pond, coagulation
Reaction tank, sedimentation basin, sterilization pool, flotation tank and reuse tank.
Multiple high concentration aerators are equipped in the conditioning tank；The anaerobic pond uses opposing seal structure, and sets in it
There are multiple baffle plates for increasing dwell time of sewage.
The multi-stage biological processing pond includes the aeration zone being sequentially communicated, a heavy area, catalytic oxidation area and two heavy areas.
The sedimentation basin, a heavy pond and the secondary settling tank are all connected with same sludge treatment equipment, in the reuse tank
Clear water be back in cotton manufacturing procedure.
Further, the multi-stage biological processing pond includes pond body and is arranged in the intracorporal multiple partitions in the pond, muti-piece
The pond body is successively divided into the first contact zone, the first aeration zone, the second aeration zone, the first buffering by the partition from left to right
Area, the second contact zone, the first catalytic oxidation area, the second catalytic oxidation area and second buffering area.
First contact zone, first aeration zone and second aeration zone composition aeration zone, described first
A heavy pond is equipped in buffer area, the first buffering area and a heavy pond constitute a heavy area, second contact zone, institute
It states the first catalytic oxidation area and second catalytic oxidation area and constitutes the catalytic oxidation area, be equipped with two in the second buffering area
Heavy pond, the second buffering area and the secondary settling tank constitute the two heavy area.
Partition described in muti-piece successively includes first partition, second partition, third partition, the 4th partition, the 5th from left to right
Partition, the 6th partition and the 7th partition.
Further, first contact zone is equipped with sewage inlet, the bottom face of the first partition and the pond body it
Between be equipped with the first communication port, between the second partition and the top end face of the pond body be equipped with the second communication port, described second every
It is equipped with third connecting mouth between plate and the bottom face of the pond body, is equipped between the third partition and the top end face of the pond body
First sludge reflux mouth is equipped with the 4th communication port between the third partition and the bottom face of the pond body.
The one heavy pond is respectively equipped with the first sludge reflux channel, the first sludge flow pass and a heavy pond outlet of sewer.
Further, described one heavy pond outlet of sewer is constituted between the 4th partition and the pond body top end face, it is described
Second contact zone passes through described one heavy pond outlet of sewer and described one heavy Chi Liantong, the 5th partition and the pond body bottom face
Between be equipped with the 5th communication port, between the 6th partition and the top end face of the pond body be equipped with the 6th communication port, the described 6th
It is equipped with the 7th communication port between partition and the bottom face of the pond body, is set between the 7th partition and the top end face of the pond body
There is the second sludge reflux mouth, eight connectivity mouth is equipped between the 7th partition and the bottom face of the pond body.
The secondary settling tank is respectively equipped with the second sludge reflux channel, the second sludge flow pass and secondary settling tank outlet of sewer.
Further, the bottom end of first aeration zone is equipped with the first lifting device, and first lifting device can
Sewage in first aeration zone is pushed into second aeration zone, the first buffering area by second communication port
It is inside equipped with the second lifting device, the sewage in the first buffering area can be pushed to described one and sunk by second lifting device
Pond.
The top end part of second aeration zone is equipped with third lifting device, and the third lifting device can push described the
Sewage in two aeration zones flows downward, so that foul water fraction flows into first aeration zone, another part flows into described first
Buffer area.
Further, the bottom end in first catalytic oxidation area is equipped with the 4th lifting device, the 4th lifting device
Sewage in first catalytic oxidation area can be pushed to second catalytic oxidation area, institute by the 6th communication port
It states and is equipped with the 5th lifting device in second buffering area, the 5th lifting device can push away the sewage in the second buffering area
It send to the secondary settling tank.
The top end part in second catalytic oxidation area is equipped with the 6th lifting device, and the 6th lifting device can push institute
The sewage stated in the second catalytic oxidation area flows downward, so that foul water fraction flows into first catalytic oxidation area, another part
Flow into the second buffering area.
Further, register is equipped in the conditioning tank, the register includes temperature sensor, temperature reducing unit
And control unit, the temperature sensor and the temperature reducing unit are electrically connected with the control unit.
Further, the anaerobic pond is connected with the chemicals dosing plant for nitrogen, phosphorus recycling to be added.
Further, the sludge treatment equipment includes sludge storage pool and sludge dehydration device；The sludge storage pool and institute
It states and is connected with shut-off valve, the first sludge pump and electrolysis machine on the pipeline between sedimentation basin, the sludge outlet of the sludge storage pool connects
Connect the inlet port of the sludge dehydration device.
The second sludge pump is connected on pipeline between the sludge storage pool and the sludge dehydration device.
Fiber industrial water circulator provided by the utility model the utility model has the advantages that
In the fiber industrial water circulator, in such a way that anaerobism and multi-stage biological processing combine, wherein more
Grade biological treatment tank includes the aeration zone being sequentially communicated, a heavy area, catalytic oxidation area and two heavy areas, and in anaerobism section water occurs for sewage
Solution, acidification, become lesser molecule, so as to improve the biodegradability of waste water, create conditions for Aerobic Process for Treatment.In addition, the production
With water circle device further include the conditioning tank being sequentially communicated, anaerobic pond, coagulation reaction tank, sedimentation basin, sterilization pool, flotation tank and return
Use pond.By a series of above-mentioned processing operations, following purpose can be reached: (1) making water quality and quantity equal and guarantee subsequent processing system
System is continuous to run well；(2) by the substance of macromolecular and bio-refractory, such as various chemical dyes and surfactant transitions
To be easy to the small-molecule substance degraded, and part COD is removed, to improve the ratio of BOD/COD；(3) more efficient process is dirty
Object is contaminated, pollutant concentration is greatly lowered.The purified processing and sewage after sterilizing enters reuse tank, in clear water can return
In other processes for cotton processing.
As known from the above, which can improve the biodegradability energy of sewage, absorption, degradation a part
Organic matter and the effect that excess sludge is digested, and then realize the advanced treating of sewage, so that the treatment effect of sewage
More thoroughly, to reach the demand of effluent standard and reuse.
The second of the utility model is designed to provide a kind of industrial water circulatory system, to solve since cotton is processed
Cheng Zhonghui generates a large amount of sewage, which has the spies such as water is big, organic pollutant content is high, coloration is deep, change of water quality is big
Point, the technical issues for the treatment of effect should be had by being not achieved using traditional processing mode.
The industrial water circulatory system provided by the utility model, comprising: above-mentioned fiber industrial water circulator.
The industrial water circulatory system provided by the utility model the utility model has the advantages that
Above-mentioned fiber industrial water circulator is set in the industrial water circulatory system, wherein fiber production
It has been described in detail in above-mentioned text with the specific structure of water circle device, connection relationship and beneficial effect etc.,
This is repeated no more.
Detailed description of the invention
It, below will be right in order to illustrate more clearly of specific embodiment of the present invention or technical solution in the prior art
Specific embodiment or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, it is described below
In attached drawing be that some embodiments of the utility model are not paying creativeness for those of ordinary skill in the art
Under the premise of labour, it can also be obtained according to these attached drawings other attached drawings.
Fig. 1 is the attachment structure schematic diagram for the fiber industrial water circulator that the embodiments of the present invention provide；
Fig. 2 is the structural schematic diagram of multi-stage biological processing pond shown in Fig. 1；
Fig. 3 is the structural schematic diagram of aerator；
Fig. 4 is the structural schematic diagram of aerated conduit shown in Fig. 3；
Fig. 5 is another structural schematic diagram of aerated conduit shown in Fig. 3.
Icon: the first contact zone 100-；The first aeration zone 200-；The second aeration zone 300-；400- mono- sinks pond；500-
Two contact zones；The first catalytic oxidation of 600- area；The second catalytic oxidation of 700- area；800- secondary settling tank；900- aerator；910- exposes
Feed channel；920- flow adjusts component；9201- air blower；9202- solenoid valve；9203- liquid level sensor.
Specific embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally
Field those of ordinary skill all other embodiment obtained without making creative work belongs to practical
Novel protected range.
It is in the description of the present invention, it should be noted that term " center ", "upper", "lower", "left", "right", " perpendicular
Directly ", the orientation or positional relationship of the instructions such as "horizontal", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
For ease of description the utility model and simplify description, rather than the mechanism of indication or suggestion meaning or element must have it is specific
Orientation, be constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.In addition, term " the
One ", " second " is used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.
Embodiment one
As shown in Figure 1, the present embodiment one provides a kind of fiber industrial water circulator, comprising: with Sewage outlet
The filtering ponds of connection, filtering ponds are interior to be equipped with grid component, and filtering ponds have been sequentially communicated conditioning tank, anaerobic pond, multi-stage biological processing
Pond, coagulation reaction tank, sedimentation basin, sterilization pool, flotation tank and reuse tank；Multiple high concentration aerators are equipped in conditioning tank；Anaerobism
Pond uses opposing seal structure, and multiple baffle plates for increasing dwell time of sewage are equipped in it；Multi-stage biological processing pond
Including aeration zone, a heavy area, catalytic oxidation area and the two heavy areas being sequentially communicated；Sedimentation basin, a heavy area and two heavy areas are all connected with together
One sludge treatment equipment, the clear water in reuse tank are back in cotton manufacturing procedure.
In the fiber industrial water circulator, in such a way that anaerobism and multi-stage biological processing combine, wherein more
Grade biological treatment tank includes the aeration zone being sequentially communicated, a heavy area, catalytic oxidation area and two heavy areas, and in anaerobism section water occurs for sewage
Solution, acidification, become lesser molecule, so as to improve the biodegradability of waste water, create conditions for Aerobic Process for Treatment.In addition, the production
With water circle device further include the conditioning tank being sequentially communicated, anaerobic pond, coagulation reaction tank, sedimentation basin, sterilization pool, flotation tank and return
Use pond.By a series of above-mentioned processing operations, following purpose can be reached: (1) making water quality and quantity equal and guarantee subsequent processing system
System is continuous to run well；(2) by the substance of macromolecular and bio-refractory, such as various chemical dyes and surfactant transitions
To be easy to the small-molecule substance degraded, and part COD is removed, to improve the ratio of BOD/COD；(3) more efficient process is dirty
Object is contaminated, pollutant concentration is greatly lowered.The purified processing and sewage after sterilizing enters reuse tank, in clear water can return
In other processes for cotton processing.
As known from the above, which can improve the biodegradability energy of sewage, absorption, degradation a part
Organic matter and the effect that excess sludge is digested, and then realize the advanced treating of sewage, so that the treatment effect of sewage
More thoroughly, to reach the demand of effluent standard and reuse.
In the embodiment, as shown in Fig. 2, multi-stage biological processing pond includes pond body and is arranged in the intracorporal multiple partitions in pond,
Pond body is successively divided into the first contact zone 100, the first aeration zone 200, the second aeration zone 300, by multiple partitions from left to right
One buffer area A, the second contact zone 500, the first catalytic oxidation area 600, the second catalytic oxidation area 700 and second buffering area B；The
One contact zone 100, the first aeration zone 200 and the second aeration zone 300 constitute aeration zone, are equipped with a heavy pond in first buffering area A
The heavy pond 400 400, first buffering area A and one constitutes a heavy area, and the second contact zone 500, the first catalytic oxidation area 600 and second connect
It touches zoneofoxidation 700 and constitutes catalytic oxidation area, be equipped with secondary settling tank 800, second buffering area B and secondary settling tank 800 in second buffering area B
Constitute two heavy areas；Multiple partitions from left to right successively include first partition, second partition, third partition, the 4th partition, the 5th every
Plate, the 6th partition and the 7th partition.
Please continue to refer to Fig. 2, the first contact zone 100 is equipped with sewage inlet, sets between first partition and the bottom face of pond body
There is the first communication port, the second communication port, the bottom face of second partition and pond body are equipped between second partition and the top end face of pond body
Between be equipped with third connecting mouth, between third partition and the top end face of pond body be equipped with the first sludge reflux mouth, third partition and pond
The 4th communication port is equipped between the bottom face of body；One heavy pond 400 is respectively equipped with the first sludge reflux channel, the outflow of the first sludge is led to
Road and a heavy pond outlet of sewer.
Fig. 2 please be continuing with, a heavy pond outlet of sewer, the second contact are constituted between the 4th partition and the top end face of pond body
Area 500 is connected to by a heavy pond outlet of sewer with a heavy pond 400, and the 5th is equipped between the 5th partition and the bottom face of pond body and is connected to
Mouthful, it is equipped with the 6th communication port between the 6th partition and the top end face of pond body, the is equipped between the 6th partition and the bottom face of pond body
Seven communication ports are equipped with the second sludge reflux mouth, the bottom face of the 7th partition and pond body between the 7th partition and the top end face of pond body
Between be equipped with eight connectivity mouth；Secondary settling tank 800 is respectively equipped with the second sludge reflux channel, the second sludge flow pass and secondary settling tank
Outlet of sewer.
In the multi-stage biological processing pond, contact zone (the first contact zone 100 and the second contact zone 500) can sufficiently be sent out
The Adsorption effect for waving microorganism, enables by the organic matter fast degradation of microorganism adsorption, handles phase with traditional wastewater
Than faster, removal organic matter is more thorough, and has for be difficult to degrade for the speed of the multi-stage biological processing pond degradation of organic substances
Machine object also has good removal to act on.
Also, due to the setting of the first aeration zone 200 and the second aeration zone 300, increase sewage following in aeration zone
Ring and stop enable the aeration zone preferably to increase dissolved oxygen content, greatly promote aeration efficiency and aeration effect.
In addition, increasing treatment sewage due to the setting in the first catalytic oxidation area 600 and the second catalytic oxidation area 700
With the time of biofilm contact, the activated sludge collective effect of biomembrane and suspension, to have the function that purify sewage.This is more
Sewage in grade biological treatment tank is able to achieve self-loopa, and the residence time in the pond is longer, so as to efficiently handle
Pollutant concentration is greatly lowered in pollutant, so that treatment sewage be made to reach reuse and discharge standard requirement.
In the embodiment, the bottom of pond body is arranged in the first communication port and third connecting mouth, and the second communication port is arranged in pond
The top of body, treatment sewage successively enters the first aeration zone 200 by the first communication port, then enters second by the second communication port and expose
Gas area 300 increases residence time of the sewage in aeration zone, can return plus into foul water fraction in the second aeration zone 300
It is flow to the first aeration zone 200, to further extend time of the sewage in aeration zone, greatly improves aeration efficiency and exposure
Gas effect.
In addition, a heavy pond 400 is equipped in first buffering area A, it can will be in first buffering area A by the second lifting device
Sewage is sent to a heavy pond 400, thus, the foul water fraction flowed out through the second aeration zone 300 stays in first buffering area A, and part is first
It, can successively will be in first buffering area A after the sewage in a heavy pond 400 is from a heavy pond outlet of sewer outflow into a heavy pond
Sewage is sent to being precipitated in a heavy pond 400, to improve sedimentation effect of the sewage in a heavy pond 400.
In addition, a heavy pond 400 is respectively equipped with sludge reflux channel and sludge flow pass, partial sludge mixed liquor is by again
It send to the second aeration zone 300, partial sludge carries out subsequent processing by output.
On the basis of the above embodiments, the bottom of pond body, the 6th connection is arranged in the 5th communication port and the 7th communication port
Mouth is arranged in the top of pond body, treatment sewage successively by heavy second contact zone of pond outlet of sewer 500, by the 5th communication port into
Enter the first catalytic oxidation area 600, then the second catalytic oxidation area 700 is entered by the 6th communication port, is being contacted to increase sewage
Residence time in zoneofoxidation, reflowable to the first catalytic oxidation plus foul water fraction in the second catalytic oxidation area 700 is entered
Area 600 increases treatment sewage and biofilm contact to further extend time of the sewage in catalytic oxidation area
Time, by the activated sludge collective effect of biomembrane and suspension, so as to have the function that purify sewage.
In the embodiment, the bottom end of the first aeration zone 200 is equipped with the first lifting device, and the first lifting device can be by the
Sewage in one aeration zone 200 pushes to the second aeration zone 300 by the second communication port, is equipped with second in first buffering area A and mentions
Device is risen, the sewage in first buffering area A can be pushed to a heavy pond 400 by the second lifting device.
Herein on basis, the top end part of the second aeration zone 300 is equipped with third lifting device, and third lifting device can push away
The sewage in the second aeration zone 300 is sent to flow downward, so that foul water fraction flows into the first aeration zone 200, another part flows into the
One buffer area A.
On the basis of the above embodiments, the bottom end in the first catalytic oxidation area 600 is equipped with the 4th lifting device, and the 4th mentions
The second catalytic oxidation area 700 can be pushed to by the 6th communication port for the sewage in the first catalytic oxidation area 600 by rising device, the
The 5th lifting device is equipped in two buffer area B, the sewage in second buffering area B can be pushed to secondary settling tank by the 5th lifting device
In 800.
It, can will be in second buffering area B by the 5th lifting device due to being equipped with secondary settling tank 800 in second buffering area B
Sewage is sent to secondary settling tank 800, thus, the foul water fraction flowed out through the second catalytic oxidation area 700 stays in second buffering area B, part
Secondary settling tank 800 is initially entered, it, can be successively by the second buffering after the sewage in secondary settling tank 800 is from the outflow of secondary settling tank outlet of sewer
Sewage in area B is sent to being precipitated in secondary settling tank 800, to improve sedimentation effect of the sewage in secondary settling tank 800.
In addition, secondary settling tank 800 is respectively equipped with the second sludge reflux channel and the second sludge flow pass, partial sludge mixing
Liquid is sent again to the second catalytic oxidation area 700, and partial sludge carries out subsequent processing by output.
In the embodiment, the top end part in the second catalytic oxidation area 700 is equipped with the 6th lifting device, and the 6th lifting device can
The sewage pushed in the second catalytic oxidation area 700 flows downward, so that foul water fraction flows into the first catalytic oxidation area 600, it is another
Part flows into second buffering area B.The design of 6th lifting device accelerates stream of the sewage in the second catalytic oxidation area 700
It is dynamic, improve the cycle rate of sewage.
The device further includes control unit, and the first lifting device, the second lifting device, third lifting device, the 4th are promoted
Device, the 5th lifting device and the 6th lifting device are electrically connected with control unit.Wherein, can be controlled by control unit
One lifting device, the second lifting device, third lifting device, the 4th lifting device, the 5th lifting device and the 6th lifting device
Movement.
Wherein, the first lifting device, the second lifting device, third lifting device, the 4th lifting device, the 5th lifting device
It can be identical with the structure of the 6th lifting device.
Such as: the first lifting device, the second lifting device, third lifting device, the 4th lifting device, the 5th lifting device
Air lift unit is all made of with the 6th lifting device；The lifting device is realized pair by blasting air in corresponding region
The push of sewage acts on.
In the embodiment, sludge treatment equipment includes sludge storage pool and sludge dehydration device；Sludge storage pool and sedimentation basin it
Between pipeline on be connected with shut-off valve, the first sludge pump and electrolysis machine, the sludge outlet of sludge storage pool connects sludge dehydration device
Inlet port；The second sludge pump is connected on pipeline between sludge storage pool and sludge dehydration device.
Be provided with filtering ponds before sewage treatment, be equipped with grid component in filtering ponds, grid component include coarse rack and
Thin grid, which, which can largely remove flocking, floating material and inorganic grit in raw sewage etc., influences biological treatment and sludge
Handle the impurity of operation.
In the embodiment, it is equipped with agitating device in conditioning tank, keep water quality and quantity equal and guarantees that follow up device is continuously normally transported
Turn；In addition, being additionally provided with register in conditioning tank, register includes temperature sensor, temperature reducing unit and control unit, temperature
Sensor and temperature reducing unit are electrically connected with control unit；When work, water temperature in temperature sensor real-time monitoring conditioning tank, when
Water temperature in conditioning tank is higher, is such as higher than 40 DEG C, sends the signal to control unit, and control unit receives signal control drop
Warm cell operation carries out cooling processing to the water in pond.Wherein, temperature reducing unit uses existing cooling device.
In the embodiment, anaerobic pond is connected with the chemicals dosing plant for nitrogen, phosphorus recycling to be added, using anaerobe into
The degradation of row organic pollutant.
The microbial flora is able to carry out hydrolysis, acidification reaction under conditions of anoxic, and microbial flora will be insoluble
Hydrolysis of organic matter is dissolved matter, meanwhile, under the synergistic effect of acid-producing bacteria, by the substance of macromolecular and bio-refractory,
Such as various chemical dyes and surfactant transitions are the small-molecule substance for being easy to degrade, and remove part COD, to improve
The ratio of BOD/COD.
On the basis of the above embodiments, the first aeration zone 200, the second aeration zone 300,600 and of the first catalytic oxidation area
Completely identical in structure aerator 900 is equipped in second catalytic oxidation area 700.
Wherein, the structure of aerator 900 can be there are many form, and specific introduction is following several, but is not limited to following
Specific constructive form.
The first: aerator 900 includes spiral type pipe, and spiral type pipe is equipped with multiple aeration plates, each aeration
Multiple ventholes are equipped on disk.
Wherein, aerator 900, can be to the sewage of different depth in the region using the arrangement form of spiral type pipe
Uniform air is provided, so that the dissolved oxygen amount in the region is more uniform, to improve the treatment effect of sewage.
Second: aerator 900 includes multilayer aerated conduit 910, the multiple aerations being arranged on aerated conduit 910
Hole and flow for adjusting air mass flow in aerated conduit 910 adjust component 920.
As shown in figure 3, it includes air blower 9201, solenoid valve 9202, for detecting aeration zone (that flow, which adjusts component 920,
One aeration zone 200, the second aeration zone 300, the first catalytic oxidation area 600 or the second catalytic oxidation area 700) interior sewage quantity liquid level
Sensor 9203.
Specifically, one end of every layer of aerated conduit 910 is communicated with branch flow pipe, is equipped with electromagnetism on every branch flow pipe
Valve 9202, more branch flow pipes are connected to same main flow conduit, and air blower 9201 is connected on main flow conduit；Liquid level sensor 9203
Number it is equal with the number of plies of aerated conduit 910, a liquid level sensor 9203 is correspondingly arranged at one layer of aerated conduit 910
Top, liquid level sensor 9203 and solenoid valve 9202 are electrically connected with control unit.
On the basis of the above embodiments, the structure type of aerated conduit 910 can there are many, now introduce it is following several,
But it is not limited to structure type in detail below.
Such as: as shown in figure 4, aerated conduit 910 includes circular aerated conduit, the inner circumferential of circular aerated conduit towards
Inside it is communicated with more linear aerated conduits.
For another example: as shown in figure 5, aerated conduit 910 includes the cyclic annular aerated conduit in side, the inside of Fang Huanzhuan aerated conduit towards
Inside it is communicated with more linear aerated conduits.
Wherein, Fig. 4 and Fig. 5 is shown has opened up multiple solarization air caps on aerated conduit 910.
In order to further increase aeration effect, an aeration spray head can be connected at each solarization air cap, to improve outlet
Amount.
It is introduced for second of aerator is set in the first aeration zone 200.
Specifically, the fixed frame for installing multilayer aerated conduit 910 is equipped in the first aeration zone 200；Wherein, fixed frame
It is fixedly connected with the first aeration zone 200 to be detachable, in order to the dismounting and replacement of aerated conduit 910 and fixed frame.
On the basis of the above embodiments, the structure type of fixed frame can there are many, but be not limited to tie in detail below
Configuration formula.
Specifically, fixed frame includes the first fixed frame and the second fixed frame being oppositely arranged；First fixed frame and second is consolidated
Determine to be equipped with multiple grooves for being clamped multilayer aerated conduit 910 at frame opposite position.
Specifically, the first fixed frame is connected in first partition, and the second fixed frame is connected on second partition.
On the basis of the above embodiments, agitating device is equipped in the first aeration zone 200 or the second aeration zone 300；Or
It is to be equipped with agitating device in the first aeration zone 200 and the second aeration zone 300.
Specifically, agitating device includes motor, the agitating shaft being connected to the motor and the stirring blade being arranged on agitating shaft.
In the embodiment, it is provided with coagulation reaction tank before entering sedimentation basin, flocculant is added in the pond, to improve
Dehydration efficiency is conducive to the desiccation degree of dehydration.
In the embodiment, the water after sedimentation basin precipitates sequentially enters ultrasonic sterilization pond and disinfection by ultraviolet light pond.
Wherein, ultrasonic sterilization pond and disinfection by ultraviolet light pond can be wholely set；Or it is separately separately provided.
Embodiment two
The present embodiment two provides a kind of industrial water circulatory system, comprising: above-mentioned fiber industrial water circulator.
Above-mentioned fiber industrial water circulator is set in the industrial water circulatory system, wherein fiber production
It has been described in detail in above-mentioned text with the specific structure of water circle device, connection relationship and beneficial effect etc.,
This is repeated no more.
Finally, it should be noted that the above various embodiments is only to illustrate the technical solution of the utility model, rather than it is limited
System；Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should
Understand: it is still possible to modify the technical solutions described in the foregoing embodiments, or to some or all of
Technical characteristic is equivalently replaced；And these are modified or replaceed, it does not separate the essence of the corresponding technical solution, and this is practical new
The range of each embodiment technical solution of type.
Claims (10)
1. a kind of fiber industrial water circulator characterized by comprising the filtering ponds being connected to Sewage outlet, it is described
Grid component is equipped in filtering ponds, it is anti-that the filtering ponds have been sequentially communicated conditioning tank, anaerobic pond, multi-stage biological processing pond, coagulation
Ying Chi, sedimentation basin, sterilization pool, flotation tank and reuse tank；
Multiple high concentration aerators are equipped in the conditioning tank；The anaerobic pond uses opposing seal structure, and is equipped with and uses in it
In the multiple baffle plates for increasing dwell time of sewage；
The multi-stage biological processing pond includes the aeration zone being sequentially communicated, a heavy area, catalytic oxidation area and two heavy areas；
The sedimentation basin, a heavy area and the two heavy area are all connected with same sludge treatment equipment, clear in the reuse tank
Water is back in cotton manufacturing procedure.
2. fiber industrial water circulator according to claim 1, which is characterized in that the multi-stage biological processing pond packet
Pond body and setting are included in the intracorporal multiple partitions in the pond, the pond body is successively divided into the by partition described in muti-piece from left to right
One contact zone (100), the first aeration zone (200), the second aeration zone (300), first buffering area, the second contact zone (500), first
Catalytic oxidation area (600), the second catalytic oxidation area (700) and second buffering area；
First contact zone (100), first aeration zone (200) and second aeration zone (300) constitute the aeration
Area, is equipped with a heavy pond in the first buffering area, and the first buffering area and a heavy pond constitute a heavy area, and described the
Two contact zones (500), first catalytic oxidation area (600) and second catalytic oxidation area (700) constitute the contact oxygen
Change area, secondary settling tank is equipped in the second buffering area, the second buffering area and the secondary settling tank constitute the two heavy area；
Partition described in muti-piece from left to right successively include first partition, second partition, third partition, the 4th partition, the 5th partition,
6th partition and the 7th partition.
3. fiber industrial water circulator according to claim 2, which is characterized in that first contact zone (100)
Equipped with sewage inlet, between the first partition and the bottom face of the pond body be equipped with the first communication port, the second partition with
It is equipped with the second communication port between the top end face of the pond body, third is equipped between the second partition and the bottom face of the pond body
Communication port is equipped with the first sludge reflux mouth, the third partition and institute between the third partition and the top end face of the pond body
It states and is equipped with the 4th communication port between the bottom face of pond body；
The one heavy pond (400) is respectively equipped with the first sludge reflux channel, the first sludge flow pass and a heavy pond outlet of sewer.
4. fiber industrial water circulator according to claim 3, which is characterized in that the 4th partition and the pond
Described one heavy pond outlet of sewer is constituted between the top end face of body, second contact zone (500) is gone out by described one heavy pond sewage
Mouth is connected to described one heavy pond (400), and the 5th communication port is equipped between the 5th partition and the bottom face of the pond body, described
Be equipped with the 6th communication port between 6th partition and the top end face of the pond body, the bottom face of the 6th partition and the pond body it
Between be equipped with the 7th communication port, be equipped with the second sludge reflux mouth between the 7th partition and the top end face of the pond body, described the
Eight connectivity mouth is equipped between seven partitions and the bottom face of the pond body；
The secondary settling tank (800) is respectively equipped with the second sludge reflux channel, the second sludge flow pass and secondary settling tank outlet of sewer.
5. fiber industrial water circulator according to claim 4, which is characterized in that first aeration zone (200)
Bottom end be equipped with the first lifting device, first lifting device can will the sewage in first aeration zone (200) lead to
It crosses second communication port and pushes to second aeration zone (300), be equipped with the second lifting device, institute in the first buffering area
The sewage in the first buffering area can be pushed to described one heavy pond (400) by stating the second lifting device；
The top end part of second aeration zone (300) is equipped with third lifting device, and the third lifting device can push described
Sewage in second aeration zone (300) flows downward, so that foul water fraction flows into first aeration zone (200), another part
Flow into the first buffering area.
6. fiber industrial water circulator according to claim 5, which is characterized in that first catalytic oxidation area
(600) bottom end is equipped with the 4th lifting device, the 4th lifting device can will first catalytic oxidation area (600) it is interior
Sewage second catalytic oxidation area (700) is pushed to by the 6th communication port, the is equipped in the second buffering area
Five lifting devices, the 5th lifting device can push to the sewage in the second buffering area secondary settling tank (800)；
The top end part in second catalytic oxidation area (700) is equipped with the 6th lifting device, and the 6th lifting device can push
Sewage in second catalytic oxidation area (700) flows downward, so that foul water fraction flows into first catalytic oxidation area
(600), another part flows into the second buffering area.
7. fiber industrial water circulator according to claim 1, which is characterized in that be equipped with temperature adjustment in the conditioning tank
Device, the register include temperature sensor, temperature reducing unit and control unit, and the temperature sensor and the cooling are single
Member is electrically connected with the control unit.
8. fiber industrial water circulator according to claim 1, which is characterized in that the anaerobic pond, which is connected with, to be used for
The chemicals dosing plant of nitrogen, phosphorus recycling is added.
9. fiber industrial water circulator according to claim 1, which is characterized in that the sludge treatment equipment includes
Sludge storage pool and sludge dehydration device；
Shut-off valve, the first sludge pump and electrolysis machine are connected on pipeline between the sludge storage pool and the sedimentation basin, it is described
The sludge outlet of sludge storage pool connects the inlet port of the sludge dehydration device；
The second sludge pump is connected on pipeline between the sludge storage pool and the sludge dehydration device.
10. a kind of fiber industrial water circulatory system characterized by comprising the described in any item fibres of the claims 1-9
Tie up industrial water circulator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820351216.6U CN208586173U (en) | 2018-03-14 | 2018-03-14 | Fiber industrial water circulator and system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820351216.6U CN208586173U (en) | 2018-03-14 | 2018-03-14 | Fiber industrial water circulator and system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208586173U true CN208586173U (en) | 2019-03-08 |
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ID=65531909
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| CN201820351216.6U Expired - Fee Related CN208586173U (en) | 2018-03-14 | 2018-03-14 | Fiber industrial water circulator and system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108218145A (en) * | 2018-03-14 | 2018-06-29 | 哈密绿天使纤维科技有限公司 | Fiber industrial water circulator and system |
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2018
- 2018-03-14 CN CN201820351216.6U patent/CN208586173U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108218145A (en) * | 2018-03-14 | 2018-06-29 | 哈密绿天使纤维科技有限公司 | Fiber industrial water circulator and system |
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Granted publication date: 20190308 |