CN107089775A - Container-type variable volume integrated effluent disposal system - Google Patents
Container-type variable volume integrated effluent disposal system Download PDFInfo
- Publication number
- CN107089775A CN107089775A CN201710427488.XA CN201710427488A CN107089775A CN 107089775 A CN107089775 A CN 107089775A CN 201710427488 A CN201710427488 A CN 201710427488A CN 107089775 A CN107089775 A CN 107089775A
- Authority
- CN
- China
- Prior art keywords
- container
- processing unit
- box type
- pond
- sewage
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000010865 sewage Substances 0.000 claims abstract description 117
- 239000012528 membrane Substances 0.000 claims abstract description 72
- 238000012545 processing Methods 0.000 claims abstract description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 48
- 239000010802 sludge Substances 0.000 claims abstract description 28
- 230000001105 regulatory effect Effects 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 31
- 238000004140 cleaning Methods 0.000 claims description 17
- 239000000126 substance Substances 0.000 claims description 17
- 230000008569 process Effects 0.000 claims description 16
- 230000000694 effects Effects 0.000 claims description 12
- 238000012423 maintenance Methods 0.000 claims description 11
- 238000005273 aeration Methods 0.000 claims description 5
- 239000000945 filler Substances 0.000 claims description 4
- 239000003814 drug Substances 0.000 claims description 2
- 229940079593 drug Drugs 0.000 claims 1
- 230000033228 biological regulation Effects 0.000 abstract description 6
- 230000008859 change Effects 0.000 description 11
- 238000000926 separation method Methods 0.000 description 9
- 238000006073 displacement reaction Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 5
- 238000007254 oxidation reaction Methods 0.000 description 5
- 238000004065 wastewater treatment Methods 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000011953 bioanalysis Methods 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 238000010010 raising Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000108664 Nitrobacteria Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000003905 agrochemical Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 238000002306 biochemical method Methods 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000002363 herbicidal effect Effects 0.000 description 1
- 239000004009 herbicide Substances 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 230000007102 metabolic function Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000004162 soil erosion Methods 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1268—Membrane bioreactor systems
Abstract
The invention discloses container-type variable volume integrated effluent disposal system, including box type sewage processing unit and the equipment room that is connected with box type sewage processing unit（11）, at least two pieces sideboards are provided with the box type sewage processing unit（5）, and two pieces of sideboards（5）Box type sewage processing unit is separated into the anaerobic pond for being capable of regulating reservoir amount of capacity（4）, Aerobic Pond（7）And membrane cisterna（9）；Using the box type sewage processing unit with the high container-like structure of structural strength, and box type sewage processing unit is separated into the anaerobic pond, Aerobic Pond and membrane cisterna of variable capacity size using sideboard, so as to reach residence time of the regulation sewage in each pond, to reach the organic loading for changing sewage disposal according to water quality treatment situation, activated sludge concentration can be quickly controlled, sewage treating efficiency is improved.
Description
Technical field
It is at container-type variable volume integrated sewage water specifically the present invention relates to fields such as sewage disposal technologies
Reason system.
Background technology
Sewage disposal (sewage treatment, wastewater treatment)：To reach sewage, draining is a certain
The process that water body or the water quality requirement reused are purified to it.Sewage disposal is widely used in building, agricultural, hands over
The every field such as logical, the energy, petrochemical industry, environmental protection, urban landscape, medical treatment, food and drink, also comes into the daily of common people more and more
Life.
Classify by sewage source, sewage disposal is generally divided into production wastewater treatment and sanitary sewage disposal.Production waste bag
Include trade effluent, rural sewage and medical sewage etc.；And sanitary sewage is exactly the sewage that daily life is produced, refer to various shapes
The inorganic matter of formula and the complex mixture of organic matter, including：1. the size solid particle for floating and suspending；2. gluey and gel
Diffusate；3. pure solution.
Divide by the dirty matter of water, the pollution of water there are two classes：One class is natural pollution；Another kind of is artificial pollution.Currently
Larger to water body harm is artificial pollution.Water pollution can be broadly divided into chemical contamination, thing according to the difference of pollution impurity
Rationality pollutes and biologic contamination three major types.Pollutant mainly has：(1) it is unprocessed and discharge industrial wastewater；(2) it is unprocessed
And the sanitary sewage discharged；(3) it is a large amount of to use chemical fertilizer, agricultural chemicals, the farmland sewage of herbicide；(4) industrial waste by the river is stacked
Thing and house refuse；(5) soil erosion；(6) mine system engineering.
Sewage disposal can be divided into three kinds of Physical, bioanalysis and chemical method according to its effect.
1. Physical：The main non-solubility material separated using physical action in sewage, is not changed in processing procedure
Chemical property.Conventional has Gravity Separation, centrifugation, counter-infiltration, air supporting etc..Physical processing structures are relatively simple, economical,
For villages and small towns water body capacity to be big, self-purification capacity is strong, the less demanding situation of sewage disposal degree.
2. bioanalysis：Using the metabolic function of microorganism, by the organic matter point in sewage in dissolving or colloidal state
Solution is oxidized to stable inorganic substances, is purified sewage.Conventional active sludge and biomembrance process.Biochemical method
Degree is higher than Physical.
3. chemical method：It is that dissolving material or the side of colloidal substance to handle or reclaim sewage are acted on using chemical reaction
Method, is used for industrial wastewater.Conventional has Coagulation Method, neutralisation, oxidation-reduction method, ion-exchange etc..At method of chemical treatment
Reason effect is good, costly, the water outlets being used as after biochemical treatment more, further processes, improves effluent quality.
The content of the invention
It is an object of the invention to design container-type variable volume integrated effluent disposal system, using with structure
The box type sewage processing unit of the high container-like structure of intensity, and be separated into box type sewage processing unit using sideboard
Anaerobic pond, Aerobic Pond and the membrane cisterna of variable capacity size, so that residence time of the regulation sewage in each pond is reached, to reach root
Change the organic loading of sewage disposal according to water quality treatment situation, can quickly control activated sludge concentration, improve sewage disposal effect
Rate.
The present invention is achieved through the following technical solutions：Container-type variable volume integrated effluent disposal system, including case
Formula sewage-treatment plant and the equipment room being connected with box type sewage processing unit, are set in the box type sewage processing unit
There are at least two pieces sideboards, and box type sewage processing unit is separated into and is capable of regulating reservoir amount of capacity by two pieces of sideboards
Anaerobic pond, Aerobic Pond and membrane cisterna.
It is further for the present invention is better achieved, can be according to sewage treatment process by box type sewage processing unit
It is in anaerobic pond, Aerobic Pond and membrane cisterna to separate in order, and promotes sideboard to carry out displacement using rotating push rod device, so as to change
Become each pond（Anaerobic pond, Aerobic Pond and membrane cisterna）Amount of capacity, and then play and change residence time of the sewage in each pond,
Sewage disposal organic loading is changed according to water quality treatment situation with this, especially using following setting structures：At the box type sewage
Manage device and equipment room and all use container-type casing, the casing of the box type sewage processing unit and the casing of equipment room are all wrapped
Base is included, container flanging wall is provided with base；At least two pieces sideboards are according to sewage treatment process order by case
The casing of formula sewage-treatment plant is separated into anaerobic pond, Aerobic Pond and membrane cisterna successively；It is provided with box type sewage processing unit
At least two sets rotating push rod devices, and single set rotating push rod device is connected with independent one piece of sideboard respectively.
It is further for the present invention is better achieved, can be good at effectively completely cutting off each pond, it is to avoid pond and
Cross pollution is formed between pond, so as to avoid influenceing wastewater treatment efficiency, while facilitating rotating push rod device and sideboard
Connection so that the capacity in convenient each pond of regulation, especially using following setting structures：Set in the middle and upper part of the sideboard
There is water hole, all set on the side that the side and sideboard being in contact in sideboard with container flanging wall are in contact with base
Seal is put, and is provided with sideboard screwed hole；It is preferred that the seal use rubber strip.
Further is that the present invention is better achieved, and screw putter can be driven using rotating push rod motor, so as to drive
Sideboard carries out displacement, and then plays the purpose for changing each pond capacity, especially using following setting structures：The rotation is pushed away
Lever apparatus includes rotating push rod motor and the screw putter being connected on rotating push rod motor, and screw putter is arranged on screwed hole
It is upper to be connected with sideboard.
Further is that the present invention is better achieved, and can promote one piece of active catch using at least a set of rotating push rod device
Plate carries out displacement, so that amount of capacity is uncoordinated between avoiding the occurrence of each pond, the situation of water quality treatment is influenceed, especially using following
Setting structure：It is oppositely arranged according to the screw putter of two sets of rotating push rod devices of sewage treatment process order with screw putter,
And two rotating push rod motors are separately positioned on the container flanging wall of outside the container flanging wall of anaerobic pond side and membrane cisterna side
2 sets or 3 sets or 4 sets of rotating push rod devices are set on outside, the sideboard between anaerobic pond and Aerobic Pond preferably, good
2 sets or 3 sets or 4 sets of rotating push rod devices are set on the sideboard between oxygen pond and membrane cisterna.
It is further to carry out oxygen exchange to Aerobic Pond for the present invention is better achieved, so as to reach at raising sewage
The purpose of effect is managed, especially using following setting structures：Aerating system, the aerating system bag are provided with the Aerobic Pond
Include aerated conduit system, be provided with filler and aeration head in aerated conduit system, the aerated conduit system by pipeline with
The air blower outside Aerobic Pond is arranged on to be connected.
It is further that the processing of sewage can be carried out using MBR sewage disposal technologies for the present invention is better achieved, so that
The purpose of the deep purifying of sewage is realized, especially using following setting structures：MBR membrane biological reactions are provided with the membrane cisterna
Device and MLSS sludge concentration instrument, and MBR membrane bioreactors are connected by pipeline with equipment room.
It is further to realize and MBR membrane bioreactors are cleaned for the present invention is better achieved, and can be by
Discharge into water after processing is improved is gone out, while can carry out dosing to membrane cisterna processing links or dosing is carried out when cleaning
Processing, also facilitates maintenance person to enter equipment room and carries out inspection operation, especially using following setting structures：Set in the equipment room
There are water pump, cleaning pump and chemicals dosing plant, go out water pump and cleaning pump and be connected with MBR membrane bioreactors, and going out on water pump
Outlet pipe is provided with, the port of export of outlet pipe is arranged on outside equipment room, maintenance door, and maintenance are additionally provided with the equipment room
Door is opened in the side away from membrane cisterna.
Further is that the present invention is better achieved, and chemicals dosing plant carries out dosing by cleaning pump respectively, under especially using
State setting structure：The chemicals dosing plant closely cleans pump side setting.
Further is that the present invention is better achieved, and easily box type sewage processing unit and equipment room can be moved
It is dynamic, especially using following setting structures：The box type sewage processing unit casing and equipment room casing container folding
Hanger is provided with the top of side wall.
The present invention compared with prior art, with advantages below and beneficial effect：
（1）The present invention utilizes active catch using the box type sewage processing unit with the high container-like structure of structural strength
Box type sewage processing unit is separated into the anaerobic pond, Aerobic Pond and membrane cisterna of variable capacity size by plate, so as to reach regulation sewage
Residence time in each pond, to reach the organic loading for changing sewage disposal according to water quality treatment situation, can quickly it control
Activated sludge concentration, improves sewage treating efficiency.
（2）The casing of box type sewage processing unit of the present invention and equipment room has container-like structure intensity high, batch production
Manufacture, device may move, the characteristics of recycling.
（3）The present invention carries out the separation of anaerobic pond, Aerobic Pond and membrane cisterna using sideboard, changes each by sideboard
The volume in pond, so as to the control residence time in real time.
（4）The present invention has load using biological contact oxidation method and MBR membrane bioreactor combination raisings, strengthens shock resistance
Load.
（5）The present invention uses MBR membrane reactors, and good processed water quality, efficiency high saves box type sewage processing unit and takes up an area face
Product, because sludge age can be very long, so as to greatly improve the degradation efficiency of hardly degraded organic substance, MBR membrane reactors are in high volume
Run under load, low sludge loading, long sludge age, excess sludge production is extremely low, due to sludge age can endless, zero can be realized in theory
Mud discharging.
（6）Equipment room set by the present invention is manufactured using container-type, saves the construction period.
Brief description of the drawings
Fig. 1 is structural upright schematic diagram of the present invention.
Fig. 2 is structural plan schematic diagram of the present invention.
Fig. 3 is sideboard structural representation of the present invention.
Wherein, 1- containers flanging wall；2- rotating push rod motors；3- hangers；4- anaerobic ponds；5- sideboards；6- fillers；
7- Aerobic Ponds；8-MBR membrane bioreactors；9- membrane cisternas；10- bases；11- equipment rooms；12- maintenance doors；13- screw putters；14-
Go out water pump；15- outlet pipes；16- cleaning pumps；17- chemicals dosing plants；18- screwed holes；19- seals；20- aeration heads；21- air blast
Machine；22- water holes；23-MLSS sludge concentration instrument.
Embodiment
The present invention is described in further detail with reference to embodiment, but the implementation of the present invention is not limited to this.
Embodiment 1：
The present invention proposes container-type variable volume integrated effluent disposal system, using with the high container of structural strength
The box type sewage processing unit of formula structure, and box type sewage processing unit is separated into variable capacity size using sideboard
Anaerobic pond, Aerobic Pond and membrane cisterna, so that residence time of the regulation sewage in each pond is reached, to reach according to water quality treatment situation
Change the organic loading of sewage disposal, can quickly control activated sludge concentration, improve sewage treating efficiency, as shown in Figure 1, Figure 2, scheme
Shown in 3, especially using following setting structures：Including box type sewage processing unit and with setting that box type sewage processing unit is connected
11 between standby, at least two pieces sideboards 5 are provided with the box type sewage processing unit, and two pieces of sideboards 5 will be box
Sewage-treatment plant is separated into the anaerobic pond 4 for being capable of regulating reservoir amount of capacity, Aerobic Pond 7 and membrane cisterna 9.
Sewage-treatment plant is integrated in by container-type variable volume integrated effluent disposal system proposed by the invention
Separate in one container and using 2 pieces and more than 2 pieces of sideboard 5 in some each independent ponds（Anaerobic pond 4, Aerobic Pond 7
And membrane cisterna 9）, so that pending sewage is detested in high integration, the box type sewage processing unit of high structural strength
Oxidation processes, good oxidation processes and membranization processing；And between cooperating equipment, realize the purified treatment of sewage.
Embodiment 2：
The present embodiment is further optimized on the basis of above-described embodiment, further for the present invention is better achieved, can
Box type sewage processing unit is separated in anaerobic pond, Aerobic Pond and membrane cisterna in order according to sewage treatment process, and utilized
Rotating push rod device promotes sideboard to carry out displacement, so as to change each pond（Anaerobic pond, Aerobic Pond and membrane cisterna）Capacity it is big
It is small, and then play the residence time for changing sewage in each pond, it is organic according to the change sewage disposal of water quality treatment situation with this
Load, as shown in Figure 1, Figure 2, Figure 3 shows, especially using following setting structures：The box type sewage processing unit and equipment room 11 are all
Using container-type casing, the casing of the box type sewage processing unit and the casing of equipment room 11 all include base 10, the bottom of at
Container flanging wall 1 is provided with seat 10；At least two pieces sideboards 5 are according to sewage treatment process order by box type sewage
The casing of reason device is separated into anaerobic pond 4, Aerobic Pond 7 and membrane cisterna 9 successively；At least two are provided with box type sewage processing unit
Rotating push rod device is covered, and single set rotating push rod device is connected with independent one piece of sideboard 5 respectively.
When setting, box type sewage processing unit and equipment room 11 all being taken using container-type casing preferably
Build, and the inner space of box type sewage processing unit is separated into the anaerobic pond being sequentially connected by least two pieces sideboards 5
4th, Aerobic Pond 7 and membrane cisterna 9, and the flow arrangement of anaerobic pond 4, Aerobic Pond 7 and membrane cisterna 9 also according to sewage treatment process, in anaerobism
At least a set of rotating push rod device is set on the sideboard 5 between pond 4 and Aerobic Pond 7, between Aerobic Pond 7 and membrane cisterna 9
At least a set of rotating push rod device is set on sideboard 5.
Embodiment 3：
The present embodiment is further optimized on the basis of any of the above-described embodiment, further for the present invention is better achieved,
It can be good at effectively completely cutting off each pond, it is to avoid form cross pollution between pond and pond, so as to avoid influence dirty
Water treatment efficiency, while facilitating rotating push rod device to be connected with sideboard so that the capacity in convenient each pond of regulation, such as Fig. 1,
Shown in Fig. 2, Fig. 3, especially using following setting structures：The middle and upper part of the sideboard 5 is provided with water hole 22, in activity
Seal is all set on the side that the side and sideboard 5 that baffle plate 5 is in contact with container flanging wall 1 are in contact with base 10
19, and it is provided with sideboard 5 screwed hole 18；It is preferred that the seal 19 use rubber strip.
When setting, the middle and upper part in sideboard 5 preferably sets strip or circular hole or elliptoid water hole 22,
And water hole is is arranged in 1/5 region on sideboard top by optimal set-up mode, while being set on sideboard 5
Screwed hole 18, preferably be threaded hole 18 at 4 jiaos of sideboard 5, set two screwed holes 18 in top when, preferably set
It is set to the top of water hole 22 or flushes position；Set simultaneously in the both sides of sideboard 5 and bottom using rubber material manufacture
Seal 19 carry out the sealing of sideboard 5 and 1, container flanging wall and base 10.
Embodiment 4：
The present embodiment is further optimized on the basis of any of the above-described embodiment, further for the present invention is better achieved,
Screw putter can be driven using rotating push rod motor, so as to drive sideboard to carry out displacement, and then play each pond of change
The purpose of capacity, as shown in Figure 1, Figure 2, Figure 3 shows, especially using following setting structures：The rotating push rod device is pushed away including rotation
Bar motor 2 and the screw putter 13 being connected on rotating push rod motor 2, and screw putter 13 is arranged on screwed hole 18 and activity
Baffle plate 5 is connected.
When setting, a set of rotating push rod device preferably includes a rotating push rod motor 2 and a screw putter 13,
And screw putter 13 is screwed onto on screwed hole 18 and is connected with sideboard 5.
Embodiment 5：
The present embodiment is further optimized on the basis of any of the above-described embodiment, further for the present invention is better achieved,
Using at least a set of rotating push rod device one piece of sideboard can be promoted to carry out displacement, so as to avoid the occurrence of capacity between each pond
Size is uncoordinated, the situation of water quality treatment is influenceed, as shown in Figure 1, Figure 2, Figure 3 shows, especially using following setting structures：At sewage
The screw putter 13 of reason two sets of rotating push rod devices of processing flow sequence is oppositely arranged with screw putter 13, and two rotating push rods
Motor 2 is separately positioned on outside the container flanging wall 1 of the outside of container flanging wall 1 of the side of anaerobic pond 4 and the side of membrane cisterna 9, preferably
The sideboard 5 between anaerobic pond 4 and Aerobic Pond 7 on set 2 sets or 3 sets or 4 sets of rotating push rod devices, in Aerobic Pond 7
2 sets or 3 sets or 4 sets of rotating push rod devices are set on the sideboard 5 between membrane cisterna 9.
When setting, preferred arrangement is：In container flanging wall 1 of the anaerobic pond 4 with respect to the flat outer of sideboard 5
Place sets rotating push rod motor 2, and connects the sideboard 5 between anaerobic pond 4 and Aerobic Pond 7 by screw putter 13；Simultaneously
Rotating push rod motor 2 is set at container flanging wall 1 of the membrane cisterna 9 with respect to the flat outer of sideboard 5, and passes through screw putter
Sideboard 5 between 13 connection membrane cisternas 9 and Aerobic Pond 7；When setting, the screw thread on the side sideboard 5 of membrane cisterna 9 preferably is pushed away
Bar 13 is oppositely arranged with the screw putter 13 on the side sideboard 5 of anaerobic pond 4.
Embodiment 6：
The present embodiment is further optimized on the basis of any of the above-described embodiment, further for the present invention is better achieved,
Oxygen exchange can be carried out to Aerobic Pond, so as to reach the purpose for improving wastewater treatment efficiency, as shown in Figure 1, Figure 2, Figure 3 shows, especially
Using following setting structures：Aerating system is provided with the Aerobic Pond 7, the aerating system includes aerated conduit system,
Filler 6 and aeration head 20 are provided with aerated conduit system, the aerated conduit system is by pipeline and is arranged on Aerobic Pond 7
Outside air blower 21 is connected.
Embodiment 7：
The present embodiment is further optimized on the basis of any of the above-described embodiment, further for the present invention is better achieved,
The processing of sewage can be carried out using MBR sewage disposal technologies, so that the purpose of the deep purifying of sewage is realized, as shown in Figure 1, Figure 2,
Shown in Fig. 3, especially using following setting structures：MBR membrane bioreactors 8 are provided with the membrane cisterna 9 and MLSS sludge is dense
Instrument 23 is spent, and MBR membrane bioreactors 8 are connected by pipeline with equipment room 11.
Its operation principle of the invention and sewage treatment process are：Using biological contact oxidation method and MBR membrane bioreactions
Answer and two and more than two sideboards 5 are provided with the handling process that device is combined, sewage disposal container, each activity
Baffle plate 5 is provided with 4 screwed holes 18, and the both sides of sideboard 5 and base are equipped with caulking gum（Seal 19）, according to each technique work(
Some independent ponds can be divided into（Anaerobic pond 4, Aerobic Pond 7 and membrane cisterna 9）, sideboard 5 is adjusted by rotating push rod device
Position, rotating push rod device is provided with rotating push rod motor 2, screw putter 13, is preferably arranged to every set rotating push rod motor 2 and adopts
With synchronous motor, so as to change residence time of the sewage in anaerobic pond 4, Aerobic Pond 7 and membrane cisterna 9, according to water quality treatment situation
Change the organic loading of sewage disposal, can quickly control activated sludge in the system of MBR membrane bioreactors（MLSS）Concentration,
Improve sewage treating efficiency.
Embodiment 8：
The present embodiment is further optimized on the basis of any of the above-described embodiment, further for the present invention is better achieved,
It can realize and MBR membrane bioreactors are cleaned, and the discharge into water handled after improving can be gone out, while can be right
Membrane cisterna processing links carry out dosing or agent-feeding treatment are carried out when being cleaned, and also facilitate maintenance person to be overhauled into equipment room
Operation, as shown in Figure 1, Figure 2, Figure 3 shows, especially using following setting structures：Water pump 14, cleaning are provided with out in the equipment room 11
Pump 16 and chemicals dosing plant 17, go out water pump 14 and cleaning pump 16 is connected with MBR membrane bioreactors 8, and are set going out on water pump 14
Outlet pipe 15 is equipped with, the port of export of outlet pipe 15 is arranged on outside equipment room 11, and maintenance door is additionally provided with the equipment room 11
12, and maintenance door 12 is opened in the side away from membrane cisterna 9.
When setting, be provided with maintenance door 12 on equipment room 11, preferably maintenance door 12 is arranged far from box dirt
On the container flanging wall 1 of water treatment facilities side, it is provided with equipment room 11 respectively with MBR membrane bioreactors 8 by pipe
Cleaning pump 16 that road is connected and go out water pump 14, and outlet pipe 15 is connected with water pump 14 going out, and by the water outlet of outlet pipe 15
Mouth is arranged on outside equipment room, and going out water pump 14 can be by the water body pump after MBR membrane bioreactors 8 are handled, cleaning pump
16 can play the purpose of added water when carrying out membrane cisterna 9 and the cleaning of MBR membrane bioreactors 8 cleaning and dosing cleaning.
Embodiment 9：
The present embodiment is further optimized on the basis of any of the above-described embodiment, further for the present invention is better achieved,
Chemicals dosing plant carries out dosing by cleaning pump respectively, as shown in Figure 1, Figure 2, Figure 3 shows, especially using following setting structures：It is described to add
The nearly side of cleaning pump 16 of medicine device 17 is set.
Embodiment 10：
The present embodiment is further optimized on the basis of any of the above-described embodiment, further for the present invention is better achieved,
Easily box type sewage processing unit and equipment room can be moved, as shown in Figure 1, Figure 2, Figure 3 shows, especially be set using following
Put structure：The box type sewage processing unit casing and equipment room 11 casing container flanging wall 1 top on set
Hanger 3 is equipped with, when setting, the casing that hanger 3 is arranged on to box type sewage processing unit and the casing of equipment room 11 preferably
4 jiaos of the top of container flanging wall 1 on.
Sewage is in reactor（MBR membrane bioreactors）The middle residence time is hydraulic detention time, refers to treatment sewage and exists
The average reaction time of microbial action in mean residence time in reactor, that is, sewage and bioreactor.
Organic loading：Refer to pond in unit volume water within the unit interval institute energy organics removal amount.
Sewage aerobic biochemical process：It is divided into contact oxidation method and activated sludge process.
MBR membrane bioreactors（Membrane Bio-Reactor）For membrane separation technique and the organic knot of biologic treating technique
The novel state Waste Water Treatment of conjunction.Hollow-fibre membrane is used in the present invention.With membrane module substitution traditional biological treatment technology end
Second pond is held, high activity sludge concentration is kept in MBR membrane bioreactors, biological treatment organic loading is improved, so as to reduce
Sewage treatment facility floor space, and by keeping low sludge loading to reduce surplus sludge volume.Main utilize is immersed in aerobic life
The activated sludge and larger molecular organicses in membrane separation plant entrapping tank in thing pond.It is active in MBR membrane bioreactor systems
Sludge（MLSS）Concentration can be promoted to 8000 ~ 10000mg/L, even more high；Sludge age (SRT) can extend to more than 30 days.MBR
Membrane bioreactor can retain generation cycle longer microorganism, can be achieved net to sewage deep because of its effective crown_interception
Change, Simultaneous Nitrification bacterium can fully breed in system, substantially, deep phosphorous removal denitrogenation is provided may for its nitrification effect.
MBR is the efficient combination of membrane separation technique and biological treatment, and it is dirty with membrane separation technique substitution activity that it, which originates from,
Second pond in mud method, carries out separation of solid and liquid.This technique has not only effectively achieved the purpose of mud-water separation, and with dirt
The incomparable advantage of water tertiary treatment traditional handicraft：
1st, separation of solid and liquid is efficiently carried out, its separating effect is much better than traditional sedimentation basin, effluent quality is good, goes out aqueous suspension
With turbidity close to zero, can direct reuse, realize sewage recycling.
2nd, the efficient crown_interception of film, makes microorganism be completely trapped in bioreactor, realizes reactor hydraulic retention
Time (HRT) and sludge age (SRT's) is kept completely separate, and operation control is flexibly stable.
3rd, because the MBR aeration tanks for handling traditional wastewater and second pond unite two into one, and it instead of the complete of tertiary treatment
Portion's process facility, therefore floor space can be greatly decreased, save construction investment.
4th, beneficial to the retention and breeding of nitrobacteria, system nitrification efficiency is high.Can also have de- by the change of the method for operation
Ammonia and phosphorus removal functional.
5th, because sludge age can be very long, so as to greatly improve the degradation efficiency of hardly degraded organic substance.
6th, reactor is run under high volumetric loading, low sludge loading, long sludge age, and excess sludge production is extremely low, due to mud
Age can endless, zero sludge discharge can be realized in theory.
7th, system realizes PLC controls, convenient operation and management.
It is described above, be only presently preferred embodiments of the present invention, any formal limitation not done to the present invention, it is every according to
According to the present invention technical spirit above example is made any simple modification, equivalent variations, each fall within the present invention protection
Within the scope of.
Claims (10)
1. container-type variable volume integrated effluent disposal system, it is characterised in that：Including box type sewage processing unit and with
The equipment room that box type sewage processing unit is connected（11）, at least two pieces activities are provided with the box type sewage processing unit
Baffle plate（5）, and two pieces of sideboards（5）Box type sewage processing unit is separated into the anaerobic pond for being capable of regulating reservoir amount of capacity
（4）, Aerobic Pond（7）And membrane cisterna（9）.
2. container-type variable volume integrated effluent disposal system according to claim 1, it is characterised in that：The case
Formula sewage-treatment plant and equipment room（11）All use container-type casing, the casing and equipment of the box type sewage processing unit
Between（11）Casing all include base（10）, in base（10）On be provided with container flanging wall（1）；At least two pieces sideboards
（5）The casing of box type sewage processing unit is separated into anaerobic pond successively according to sewage treatment process order（4）, Aerobic Pond
（7）And membrane cisterna（9）；At least two sets rotating push rod devices are provided with box type sewage processing unit, and single set rotation is pushed away
Lever apparatus respectively with independent one piece of sideboard（5）It is connected.
3. container-type variable volume integrated effluent disposal system according to claim 2, it is characterised in that：Described
Sideboard（5）Middle and upper part be provided with water hole（22）, in sideboard（5）With container flanging wall（1）The side being in contact
Side and sideboard（5）With base（10）Seal is all set on the side being in contact（19）, and in sideboard（5）On be provided with
Screwed hole（18）.
4. container-type variable volume integrated effluent disposal system according to claim 3, it is characterised in that：The rotation
Turning push rod device includes rotating push rod motor（2）And it is connected to rotating push rod motor（2）On screw putter（13）, and screw thread pushes away
Bar（13）It is arranged on screwed hole（18）Upper and sideboard（5）It is connected.
5. container-type variable volume integrated effluent disposal system according to claim 4, it is characterised in that：According to sewage
The screw putter of processing technological flow two sets of rotating push rod devices of order（13）With screw putter（13）It is oppositely arranged, and two rotations
Turn push-rod electric machine（2）It is separately positioned on anaerobic pond（4）The container flanging wall of side（1）Outside and membrane cisterna（9）The container folding of side
Side wall（1）It is outside.
6. the container-type variable volume integrated effluent disposal system according to Claims 2 or 3 or 4 or 5, its feature exists
In：In the Aerobic Pond（7）Aerating system is inside provided with, the aerating system includes aerated conduit system, in aerated conduit body
Fasten and be provided with filler（6）And aeration head（20）, the aerated conduit system is by pipeline and is arranged on Aerobic Pond（7）Outside
Air blower（21）It is connected.
7. the container-type variable volume integrated effluent disposal system according to Claims 2 or 3 or 4 or 5, its feature exists
In：In the membrane cisterna（9）Inside it is provided with MBR membrane bioreactors（8）And MLSS sludge concentration instrument（23）, and MBR membrane bioreactions
Answer device（8）Pass through pipeline and equipment room（11）It is connected.
8. container-type variable volume integrated effluent disposal system according to claim 7, it is characterised in that：It is described to set
Between standby（11）Inside it is provided with out water pump（14）, cleaning pump（16）And chemicals dosing plant（17）, go out water pump（14）And cleaning pump（16）With
MBR membrane bioreactors（8）It is connected, and is going out water pump（14）On be provided with outlet pipe（15）, outlet pipe（15）The port of export
It is arranged on equipment room（11）Outside, in the equipment room（11）On be additionally provided with maintenance door（12）, and maintenance door（12）It is opened in remote
From membrane cisterna（9）Side.
9. container-type variable volume integrated effluent disposal system according to claim 8, it is characterised in that：It is described to add
Medicine device（17）Nearly cleaning pump（16）Side is set.
10. according to claim 2-5, the container-type variable volume integrated effluent disposal system described in 8,9 any one, it is special
Levy and be：In the casing and equipment room of the box type sewage processing unit（11）Casing container flanging wall（1）Top
On be provided with hanger（3）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710427488.XA CN107089775A (en) | 2017-06-08 | 2017-06-08 | Container-type variable volume integrated effluent disposal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710427488.XA CN107089775A (en) | 2017-06-08 | 2017-06-08 | Container-type variable volume integrated effluent disposal system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107089775A true CN107089775A (en) | 2017-08-25 |
Family
ID=59640026
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710427488.XA Pending CN107089775A (en) | 2017-06-08 | 2017-06-08 | Container-type variable volume integrated effluent disposal system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107089775A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111115820A (en) * | 2020-01-20 | 2020-05-08 | 青岛思普润水处理股份有限公司 | Changeable sewage treatment system of pond volume |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011094768A1 (en) * | 2010-02-01 | 2011-08-04 | Van Cach Nguyen | Adjustable tank incorporated five functions for biological treatment of waste water |
| CN202265481U (en) * | 2011-09-16 | 2012-06-06 | 湖南永清水务有限公司 | Sewage treatment integrated device based on hydrolysis-membrane bioreactor (HMBR) |
| CN103319059A (en) * | 2013-07-23 | 2013-09-25 | 江苏金山环保工程集团有限公司 | Novel constant water-level sequencing batch type sewage treatment device |
| CN103787498A (en) * | 2013-11-03 | 2014-05-14 | 北京工业大学 | Rapid starting method of low-temperature low C/N sewage improvement A2/O process |
| CN204569546U (en) * | 2015-04-28 | 2015-08-19 | 滨州学院 | A kind of have the movable modified version waste disposal plant separated |
| CN206799388U (en) * | 2017-06-08 | 2017-12-26 | 四川长河阳光建设工程有限公司 | Container-type variable volume integrated effluent disposal system |
-
2017
- 2017-06-08 CN CN201710427488.XA patent/CN107089775A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011094768A1 (en) * | 2010-02-01 | 2011-08-04 | Van Cach Nguyen | Adjustable tank incorporated five functions for biological treatment of waste water |
| CN202265481U (en) * | 2011-09-16 | 2012-06-06 | 湖南永清水务有限公司 | Sewage treatment integrated device based on hydrolysis-membrane bioreactor (HMBR) |
| CN103319059A (en) * | 2013-07-23 | 2013-09-25 | 江苏金山环保工程集团有限公司 | Novel constant water-level sequencing batch type sewage treatment device |
| CN103787498A (en) * | 2013-11-03 | 2014-05-14 | 北京工业大学 | Rapid starting method of low-temperature low C/N sewage improvement A2/O process |
| CN204569546U (en) * | 2015-04-28 | 2015-08-19 | 滨州学院 | A kind of have the movable modified version waste disposal plant separated |
| CN206799388U (en) * | 2017-06-08 | 2017-12-26 | 四川长河阳光建设工程有限公司 | Container-type variable volume integrated effluent disposal system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111115820A (en) * | 2020-01-20 | 2020-05-08 | 青岛思普润水处理股份有限公司 | Changeable sewage treatment system of pond volume |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN213112948U (en) | Integrated circulating culture system | |
| CN209778575U (en) | Integrated equipment for treating high-concentration organic domestic sewage | |
| CN107555600A (en) | A kind of sewage disposal system | |
| CN210764843U (en) | Rural sewage treatment plant | |
| CN111762974A (en) | COD (chemical oxygen demand) and ammonia nitrogen treatment method and system in culture wastewater | |
| CN205061690U (en) | Anaerobism - good oxygen integrative sewage treatment device | |
| CN205133343U (en) | Rubbish transfer station sewage treatment system | |
| CN206799388U (en) | Container-type variable volume integrated effluent disposal system | |
| CN208747891U (en) | A kind of old-age group's percolate from garbage filling field processing unit | |
| CN208649040U (en) | A kind of proprietary processing unit of high concentration antibiotic organic wastewater | |
| CN110720420A (en) | Take water farming systems of anaerobism denitrification facility | |
| CN207811509U (en) | A kind of Bleaching and dyeing sewage processing unit | |
| CN105693036A (en) | Intelligent sewage treatment system | |
| CN107089775A (en) | Container-type variable volume integrated effluent disposal system | |
| CN206494810U (en) | A kind of marine sewage treatment system | |
| CN205528266U (en) | Reuse of reclaimed water sewage treatment device | |
| CN209242757U (en) | A kind of safety-type membrane biological reaction apparatus | |
| CN201512450U (en) | Sewage treatment system in pharmaceutical factory | |
| CN210261475U (en) | Rural domestic sewage rewet processing apparatus | |
| CN211847575U (en) | Integrated sewage treatment system | |
| CN209740919U (en) | Excrement recycling device for high-density aquaculture | |
| CN207811366U (en) | A kind of sewage disposal system | |
| CN203346179U (en) | Oxygen-increasing device, self-flow oxygen-increasing biological filter, self-flow oxygen-enriching ecological bed and sewage treatment system | |
| CN206799387U (en) | Total closed type green ecological circulating sewage processing system | |
| CN202519126U (en) | Square aerated biofilter reactor integrating denitrification dephosphorization functions |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170825 |