CN108892226A - Film bubble formula is oxygenated biomembrane reaction component - Google Patents
Film bubble formula is oxygenated biomembrane reaction component Download PDFInfo
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- CN108892226A CN108892226A CN201810801887.2A CN201810801887A CN108892226A CN 108892226 A CN108892226 A CN 108892226A CN 201810801887 A CN201810801887 A CN 201810801887A CN 108892226 A CN108892226 A CN 108892226A
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- 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
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- 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
- C02F3/10—Packings; Fillings; Grids
- C02F3/102—Permeable membranes
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Life Sciences & Earth Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses film bubble formula be oxygenated biomembrane reaction component, structure include water intake end mouth, hollow-fibre membrane purification lattice, signal receiver, protect interlayer, be disposed outlet end；Protection interlayer is welded in hollow-fibre membrane purification end surface of the lattice far from water intake end mouth；Hollow-fibre membrane purification lattice include water flow pull unit, enter water flow moved end, heated barrier plate, mobile pressure pipe, receive signal heating device, device for exerting, guard shield, aerator, output circulation road, hollow-fibre membrane process layer；Mobile pressure pipe is located in same level with device for exerting, hollow-fibre membrane process layer is located between water flow moved end and output circulation road, for the prior art, the present invention is used when it was used to certain time, it it can send signal by outer bound pair and so that it be allowed to bring into operation the hollow-fibre membrane of its inside cleans it automatically, after cleaning, operational effect will not significantly be affected.
Description
Technical field
The present invention relates to biomembrane reaction fields, are oxygenated biomembrane reaction component particularly with regard to a kind of film bubble formula.
Background technique
Biofilm is a kind of waste water aerobic biologic treating technique arranged side by side with activated sludge process, is a kind of fixed embrane method,
It is the manual of sewage self-purification of water process and reinforcing, mainly removes deliquescent in waste water and colloidal organic pollutant,
Processing technique has biofilter (ordinary biofilter, high-loading logical filter, tower biological filter), biological rotating disk, biology to connect
Touching oxidation does not have standby and biological fluidized bed etc., and this method provides the oxygen that Institute of Micro-biology needs using aeration method identical with aeration tank
Amount, and play a part of to stir and mix, while adding filler in aeration tank, for attached growth of microorganisms, therefore, also known as
Contact aeration process is a kind of between activated sludge process and the biological treatment of biofilter between the two, is active sludge
The advantages of biofilm of method feature, it has both the two, the function of hollow fiber ultrafiltration membrane are that removal is included in doughnut liquid
Impurity, excellent and scintilla amount ultrafiltration membrane after long-time service, may be covered on film since impurity blocks various objectionable impurities
Surface even causes because of impurity blocking fenestra, and cleaning can return receiving as two methods substantially, be respectively physical method and
Chemical method, it is more difficult that tunica fibrosa manually cleans, certain time is unclear wash if, will more influence its using effect.
For the processing mode of current hollow-fibre membrane, tunica fibrosa is using to a certain extent and certain time
When, it will some impurity are accumulated, if impurity is not cleared up, are easier to cause the operation of itself to imitate if accumulating always
Fruit and efficiency.
Summary of the invention
In view of the deficiencies of the prior art, the present invention is to realize by the following technical solutions：Film bubble formula is oxygenated biomembrane
Reaction component, structure includes water intake end mouth, hollow-fibre membrane purification lattice, signal receiver, protection interlayer, be disposed outlet
End；
The horizontal saliva of water intake end mouth is flat to be embedded in hollow-fibre membrane purification lattice one end, during the outlet end that is disposed is installed on
Empty fiber membrane purifies one end inside of the lattice far from water intake end mouth and mutually connects, and the signal receiver is embedded in hollow-fibre membrane
It purifies inside lattice top, the protection interlayer is welded in hollow-fibre membrane purification end surface of the lattice far from water intake end mouth；
The hollow-fibre membrane purification lattice include water flow pull unit, enter water flow moved end, heated barrier plate, mobile pressure
Pipe receives signal heating device, device for exerting, guard shield, aerator, output circulation road, hollow-fibre membrane process layer；
The water flow pull unit is positioned horizontally in into inside water flow moved end and positioned at middle, and the heated barrier plate is set to
Enter above water flow moved end and one end is connected with signal heating device is received, the reception signal heating device is far from by thermal barrier properties
One end bottom of plate is connected with device for exerting, and the mobile pressure pipe is located in same level with device for exerting, the exposure
Device of air is set to inside of the guard shield far from heated barrier plate one end, and the output circulation road is embedded in guard shield close to exposure
The inside of device of air one end, the hollow-fibre membrane process layer are located between water flow moved end and output circulation road.
As advanced optimizing for the technical program, the heated barrier plate include fixed block, blocking plate, reset spring,
Stressed plate, by hot-slide, described two fixed blocks are welded in by two side of hot-slide side bottom end and symmetrical, the blocking plate
Bottom end is installed on stressed plate bottom middle, and described two reset springs are between fixed block and stressed plate and symmetrical,
The stressed plate is embedded in by hot-slide inside groove and flexible connection, and reception signal heating device one end is embedded in by hot-slide
Inside top.
As advanced optimizing for the technical program, the device for exerting includes pressure sliding rail, wiper block, linking circulation
Road, water storage lattice, leakage port, the wiper block are embedded in pressure sliding rail inside groove and flexible connection, and the leakage port is located at pressure
Sliding rail interior of shell, the linking circulation road are mutually connected with water storage lattice bottom end side, the pressure sliding rail be connected circulation road
It is installed in same level, the pressure sliding rail and mobile pressure pipe are located in same level, and the aerator includes
Battery, conducting wire, motor, linking swivel, weighted shaft, impeller, the motor is electrically connected to the battery via a wire, it is described by
Power shaft is embedded in inside motor through linking swivel and clearance fit, and the weighted shaft is installed on impeller internal and is located at same
On one axle center.
As advanced optimizing for the technical program, the mobile pressure pipe include drawstring, squeeze sliding block, port of losing heart,
Air pressure return rail, described drawstring one end are connected with sliding block is squeezed, and the discouraged port is embedded in air pressure return rail interior of shell,
The extruding sliding block is installed on air pressure return rail inside groove and flexible connection, and the air pressure return rail is installed on same with pressure sliding rail
In plane, the reception signal heating device includes heat carrier, PTC heating plate, signal receiver, leads energy body, delivery of energy column, described
Heat carrier is embedded in inside PTC heating plate side, and the energy body of leading is embedded in inside of the PTC heating plate far from heat carrier one end,
The signal receiver is installed on PTC heating plate top and electrical connection, and the delivery of energy column is embedded in PTC heating plate bottom close to leading
The inside of energy body one end, described heat carrier one end is embedded in inside heated rail tips.
As advanced optimizing for the technical program, the water flow pull unit includes magnetic field ball, stress magnetic field wheel, slides
Rail pulls rope, fixed ring, and the magnetic field ball and stress magnetic field wheel are located on same level center line, and the stress magnetic field wheel is embedding
Enter sliding rail inside groove and flexible connection, described pulling rope one end is connected with stress magnetic field wheel, and the pulling is restricted far from stress magnetic
Field wheel one end is connected with fixed ring.
As advanced optimizing for the technical program, the hollow-fibre membrane process layer includes hollow process layer, hollow fibre
Film, air output end, filtering backstop, biomembrane, cohesive end are tieed up, there are two doughnuts for the hollow process layer two sides installation
Film, the air output end are located above hollow-fibre membrane and mutually connect, the filtering backstop be installed on air output end and
Between hollow-fibre membrane, the cohesive end is mutually connected with hollow process layer, and the biomembrane passes through cohesive end and hollow processing
Layer is connected.
Beneficial effect
Inventive film bubble is oxygenated biomembrane reaction component, when water flows into interior by entering water flow moved end, will pass through water flow
Impulse force its stress magnetic field taken turns toward side give along sliding rail bullet, will pull extruding sliding block suitable during movement by drawstring
Air pressure return rail slide down, entered in hollow process layer by the filtering of micropore and purification, biomembrane will obtain sufficiently
Oxygen, rotated by its motor impeller, so that the water finished to its inter-process improves aeration, when hollow-fibre membrane uses
When a period of time, the consequence of accumulation will be generated, it is allowed quickly to heat, thus by thermal energy by heat carrier importing by hot-slide,
Keep its stressed plate dynamic along being slid down by hot-slide by the principle of heat expansion, until blocking plate is blocked, to pass through linking
Circulation road imports, and wiper block is slided by the principle of thermal expansion along pressure sliding rail down, makes pressure of its hot water by gas
Flow into hollow-fibre membrane in, the place flowed through by stoste is being flowed through, thus by its surface be rinsed completely, for
The removal effect of sticky substance and impurity is more obvious, to flow out.
For the prior art, the present invention is used when it was used to certain time, and can passing through outer bound pair, it sends letter
Number, so that it be allowed to bring into operation, the hollow-fibre membrane of its inside cleans it automatically, after cleaning, operation
Effect will not significantly be affected.
Detailed description of the invention
Upon reading the detailed description of non-limiting embodiments with reference to the following drawings, other feature of the invention,
Objects and advantages will become more apparent upon：
Fig. 1 is the structural schematic diagram that inventive film bubble is oxygenated biomembrane reaction component.
Fig. 2 is the schematic diagram of internal structure figure one that hollow-fibre membrane of the present invention purifies lattice.
Fig. 3 is the schematic diagram of internal structure figure two that hollow-fibre membrane of the present invention purifies lattice.
Fig. 4 is the schematic diagram of internal structure that hollow-fibre membrane of the present invention purifies lattice working condition.
Fig. 5 is the schematic diagram of internal structure of hollow-fibre membrane process layer of the present invention.
In figure：Water intake end mouth -1, signal receiver -3, protection interlayer -4, is disposed out at hollow-fibre membrane purification lattice -2
Mouth end -5, water flow pull unit -21 enter water flow moved end -22, heated barrier plate -23, mobile pressure pipe -24, reception signal heating
Device -25, device for exerting -26, guard shield -27, aerator -28, output circulation road -29, hollow-fibre membrane process layer -
210, fixed block -231, blocking plate -232, reset spring -233, stressed plate -234, by hot-slide -235, pressure sliding rail -261,
Wiper block -262, linking circulation road -263, water storage lattice -264, leakage port -265, battery -281, conducting wire -282, motor -
283, linking swivel -284, weighted shaft -285, impeller -286, drawstring -241, extruding sliding block -242, lose heart port -243, gas
It pushes back a rail -244, heat carrier -251, PTC heating plate -252, signal receiver -253, lead energy body -254, delivery of energy column -255, magnetic
Field ball -211, sliding rail -213, pulls rope -214, fixed ring -215, hollow process layer -2101, hollow fibre at stress magnetic field wheel -212
Tie up film -2102, air output end -2103, filtering backstop -2104, biomembrane -2105, cohesive end -2106.
Specific embodiment
To be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, below with reference to
Specific embodiment and Detailed description of the invention, the preferred embodiment that the present invention is further explained.
Embodiment
Please refer to Fig. 1-Fig. 5, the present invention provides film bubble formula and is oxygenated biomembrane reaction component, structure include water intake end mouth 1,
Hollow-fibre membrane purification lattice 2, signal receiver 3, protection interlayer 4, be disposed outlet end 5；
1 level of water intake end mouth is embedded in hollow-fibre membrane purification 2 one end of lattice, the installation of outlet end 5 that is disposed
It inside the one end of hollow-fibre membrane purification lattice 2 far from water intake end mouth 1 and mutually connects, during the signal receiver 3 is embedded in
Empty fiber membrane purifies inside 2 top of lattice, and the protection interlayer 4 is welded in one of hollow-fibre membrane purification lattice 2 far from water intake end mouth 1
End surfaces；
The hollow-fibre membrane purification lattice 2 include water flow pull unit 21, enter water flow moved end 22, heated barrier plate 23, move
Dynamic pressure pipe 24, receive signal heating device 25, device for exerting 26, guard shield 27, aerator 28, output circulation road 29,
Hollow-fibre membrane process layer 210；
The water flow pull unit 21 is positioned horizontally in into 22 inside of water flow moved end and is located at middle, the heated barrier plate
23 are set into the top of water flow moved end 22 and one end is connected with reception signal heating device 25, the reception signal heating device 25
One end bottom far from heated barrier plate 23 is connected with device for exerting 26, and the mobile pressure pipe 24 is located at device for exerting 26
In same level, the aerator 28 is set to inside of the guard shield 27 far from heated 23 one end of barrier plate, the output
Circulation road 29 is embedded in guard shield 27 close to the inside of 28 one end of aerator, and the hollow-fibre membrane process layer 210 is located at
Enter between water flow moved end 22 and output circulation road 29.
The heated barrier plate 23 includes fixed block 231, blocking plate 232, reset spring 233, stressed plate 234, heated cunning
Rail 235, described two fixed blocks 231 are welded in by 235 side bottom end of hot-slide, two side and symmetrical, the blocking plate 232
Bottom end is installed on 234 bottom middle of stressed plate, and described two reset springs 233 are between fixed block 231 and stressed plate 234
And it is symmetrical, the stressed plate 234 is embedded in by 235 inside groove of hot-slide and flexible connection, the reception signal heating device
25 one end are embedded in by inside 235 top of hot-slide.
The device for exerting 26 includes pressure sliding rail 261, wiper block 262, linking circulation road 263, water storage lattice 264, lets out
Port 265, the wiper block 262 are embedded in pressure 261 inside groove of sliding rail and flexible connection, and the leakage port 265 is located at pressure
261 interior of shell of sliding rail, the linking circulation road 263 are mutually connected with 264 bottom end side of water storage lattice, the pressure sliding rail 261
It is installed in same level with circulation road 263 is connected, the pressure sliding rail 261 is located at same level with mobile pressure pipe 24
On, the aerator 28 includes battery 281, conducting wire 282, motor 283, linking swivel 284, weighted shaft 285, impeller
286, the motor 283 is electrically connected by conducting wire 282 with battery 281, and the weighted shaft 285 is embedding through linking swivel 284
Enter 283 inside of motor and clearance fit, the weighted shaft 285 is installed on 286 inside of impeller and is located on same axle center.
The mobile pressure pipe 24 includes drawstring 241, squeezes sliding block 242, lose heart port 243, air pressure return rail 244, institute
It states 241 one end of drawstring and is connected with sliding block 242 is squeezed, the discouraged port 243 is embedded in 244 interior of shell of air pressure return rail,
The extruding sliding block 242 is installed on 244 inside groove of air pressure return rail and flexible connection, the air pressure return rail 244 and pressure sliding rail
261 are installed on same plane, and the reception signal heating device 25 includes heat carrier 251, PTC heating plate 252, signal reception
Device 253 leads energy body 254, delivery of energy column 255, and the heat carrier 251 is embedded in inside 252 side of PTC heating plate, and described lead can body
254 are embedded in inside of the PTC heating plate 252 far from 251 one end of heat carrier, and the signal receiver 253 is installed on PTC heating plate
252 tops and electrical connection, the delivery of energy column 255 are embedded in 252 bottom of PTC heating plate close to the inside for leading 254 one end of energy body, institute
251 one end of heat carrier is stated to be embedded in by inside 235 top of hot-slide.
The water flow pull unit 21 includes magnetic field ball 211, stress magnetic field wheel 212, sliding rail 213, pulls rope 214, is fixed
Ring 215, the magnetic field ball 211 are located on same level center line with stress magnetic field wheel 212,212 insertion of stress magnetic field wheel
In 213 inside groove of sliding rail and flexible connection, described pulling 214 one end of rope are connected with stress magnetic field wheel 212, the pulling rope 214
212 one end are taken turns far from stress magnetic field to be connected with fixed ring 215.
The hollow-fibre membrane process layer 210 includes hollow process layer 2101, hollow-fibre membrane 2102, air output end
2103, backstop 2104, biomembrane 2105, cohesive end 2106 are filtered, there are two hollow for hollow 2101 two sides of the process layer installation
Tunica fibrosa 2102, the air output end 2103 are located at 2102 top of hollow-fibre membrane and mutually connect, the filtering backstop
2104 are installed between air output end 2103 and hollow-fibre membrane 2102, the cohesive end 2106 and hollow 2101 phase of process layer
It mutually connects, the biomembrane 2105 is connected by cohesive end 2106 with hollow process layer 2101.
The principle of the present invention：When water flows into interior by entering water flow moved end 22, by by the impulse force of water flow by its stress magnetic
Field wheel 212 is sent toward side along 213 bullet of sliding rail, will be pulled by drawstring 241 during movement and be squeezed sliding block 242 along gas
It pushes back a rail 244 to slide down, its air is squeezed into inside water flow moved end 22, its water flow is squeezed into hollow-fibre membrane 2102
It is interior, entered in hollow process layer 2101 by the filtering and purification of micropore, biomembrane 2105 will obtain sufficient oxygen, to flow
The water of warp will be purified again, and extra air will be squeezed out by air output end 2103, by its motor 283 with movable vane
286 rotation of wheel, so that aeration is improved to the water that its inter-process finishes, it, will when hollow-fibre membrane 2102 is using a period of time
The consequence for generating accumulation sends signal by its signal receiver 253 of outer bound pair and allows so that its PTC heating plate 252 be opened
It is quickly heated, to being imported thermal energy by heat carrier 251 by hot-slide 235, making its original of the stressed plate 234 by heat expansion
It makes in order and is slided down by hot-slide 235, until blocking plate 232 is blocked, water will be added by thermal energy by leading energy body 254
Heat, to be imported by linking circulation road 263, wiper block 262 is slid down by the principle of thermal expansion along pressure sliding rail 261
It is dynamic, so that its air be squeezed into water flow moved end 22, flows into its hot water in hollow-fibre membrane 2102 by the pressure of gas, lead to
The place that stoste flows through is crossed, is being flowed through, to its surface is rinsed completely, for going for sticky substance and impurity
Except effect is more obvious, to flow out.
PTC heating plate 252 of the present invention is called ptc heater, is formed using PTC ceramics heater element and aluminum pipe,
The type PTC heater has the advantages that thermal resistance is small, heat exchange efficiency is high, is the electric heater of a kind of automatic constant-temperature, power saving, prominent special
Point is in security performance, and surface " rubescent " phenomenon such as electric heating tubing heater will not be generated under any applicable cases, from
And cause to scald, the security risks such as fire, the aerator 28, which refers to, forces the process shifted into liquid for the oxygen in air,
The purpose is to obtain enough dissolved oxygens, in addition, aeration also prevents suspended substance in pond from sinking, reinforce organic matter and micro- life in pond
Object and the purpose of dissolved oxygen contact, to guarantee that microorganism is under conditions of having sufficient dissolved oxygen in pond, to dirty Organic substance in water
Oxygenolysis
Problems solved by the invention is for the processing mode of current hollow-fibre membrane, and tunica fibrosa is used to one
When determining degree and certain time, it will accumulated some impurity, if impurity is not cleared up, be easier to lead if accumulating always
Itself operational effect and efficiency are caused, the present invention is combined with each other by above-mentioned component, and the present invention is used when it is used to one
When fixing time, it can send signal by outer bound pair and so that it be allowed to bring into operation the hollow-fibre membrane of its inside carries out it
Automatic cleaning, after cleaning, operational effect will not significantly be affected.
The basic principles, main features and advantages of the present invention have been shown and described above, the technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this
The principle of invention can not only be realized in other specific forms under the premise of not departing from spirit of that invention or essential characteristic
The present invention will also have various changes and improvements, these changes and improvements both fall within scope of the claimed invention, therefore this hair
Bright claimed range is defined by appended claims and its equivalent, rather than above description limits.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (8)
1. film bubble formula is oxygenated biomembrane reaction component, structure includes water intake end mouth (1), hollow-fibre membrane purification lattice (2), signal
Receiver (3), protection interlayer (4), the outlet end that is disposed (5), it is characterised in that：
Water intake end mouth (1) level is embedded in hollow-fibre membrane purification lattice (2) one end, the outlet end that is disposed (5) peace
One end inside and mutually connection loaded on hollow-fibre membrane purification lattice (2) far from water intake end mouth (1), the signal receiver (3)
It is embedded in inside hollow-fibre membrane purification lattice (2) top, it is remote that the protection interlayer (4) is welded in hollow-fibre membrane purification lattice (2)
End surface from water intake end mouth (1)；
Hollow-fibre membrane purification lattice (2) includes water flow pull unit (21), enters water flow moved end (22), heated barrier plate
(23), mobile pressure pipe (24), reception signal heating device (25), device for exerting (26), guard shield (27), aerator
(28), circulation road (29), hollow-fibre membrane process layer (210) are exported；
The water flow pull unit (21) is positioned horizontally in internal into water flow moved end (22) and is located at middle, the heated barrier plate
(23) it is set to and is connected into above water flow moved end (22) and one end with signal heating device (25) are received, the reception signal heating
Device (25) is connected far from one end bottom of heated barrier plate (23) with device for exerting (26), the mobile pressure pipe (24) and
Device for exerting (26) is located in same level, and the aerator (28) is set to guard shield (27) far from heated barrier plate
(23) inside of one end, output circulation road (29) are embedded in guard shield (27) close to the interior of aerator (28) one end
Side, the hollow-fibre membrane process layer (210) are located between water flow moved end (22) and output circulation road (29).
2. film bubble formula according to claim 1 is oxygenated biomembrane reaction component, it is characterised in that：The heated barrier plate
(23) include fixed block (231), blocking plate (232), reset spring (233), stressed plate (234), by hot-slide (235), it is described
Two fixed blocks (231) are welded in by two side of hot-slide (235) side bottom end and symmetrical, blocking plate (232) bottom end
It is installed on stressed plate (234) bottom middle, described two reset springs (233) are located at fixed block (231) and stressed plate (234)
Between and it is symmetrical, the stressed plate (234) is embedded in by hot-slide (235) inside groove and flexible connection, the reception signal
Heating device (25) one end is embedded in by inside hot-slide (235) top.
3. film bubble formula according to claim 1 is oxygenated biomembrane reaction component, it is characterised in that：The device for exerting (26)
It is described including pressure sliding rail (261), wiper block (262), linking circulation road (263), water storage lattice (264), leakage port (265)
Wiper block (262) is embedded in pressure sliding rail (261) inside groove and flexible connection, and the leakage port (265) is located at pressure sliding rail
(261) interior of shell, the linking circulation road (263) are mutually connected with water storage lattice (264) bottom end side, the pressure sliding rail
(261) be connected circulation road (263) and be installed in same level, the pressure sliding rail (261) and mobile pressure manage (24) position
In in same level.
4. film bubble formula according to claim 1 is oxygenated biomembrane reaction component, it is characterised in that：The aerator (28)
Including battery (281), conducting wire (282), motor (283), linking swivel (284), weighted shaft (285), impeller (286), institute
It states motor (283) to be electrically connected by conducting wire (282) with battery (281), the weighted shaft (285) is through linking swivel
(284) it is embedded in motor (283) inside and clearance fit, the weighted shaft (285) is installed on impeller (286) inside and is located at
On same axle center.
5. film bubble formula according to claim 1 or 3 is oxygenated biomembrane reaction component, it is characterised in that：The mobile pressure
Pipe (24) includes drawstring (241), squeezes sliding block (242), discouraged port (243), air pressure return rail (244), the drawstring (241)
One end is connected with sliding block (242) are squeezed, and the discouraged port (243) is embedded in air pressure return rail (244) interior of shell, described
It squeezes sliding block (242) and is installed on air pressure return rail (244) inside groove and flexible connection, the air pressure return rail (244) and pressure are slided
Rail (261) is installed on same plane.
6. film bubble formula according to claim 1 or 2 is oxygenated biomembrane reaction component, it is characterised in that：The reception signal
Heating device (25) includes heat carrier (251), PTC heating plate (252), signal receiver (253), leads energy body (254), delivery of energy column
(255), the heat carrier (251) is embedded in inside PTC heating plate (252) side, it is described lead can body (254) be embedded in PTC and add
Inside of the hot plate (252) far from heat carrier (251) one end, the signal receiver (253) are installed on PTC heating plate (252) top
End and electrical connection, the delivery of energy column (255) are embedded in the close inside for leading energy body (254) one end in PTC heating plate (252) bottom,
Described heat carrier (251) one end is embedded in by inside hot-slide (235) top.
7. film bubble formula according to claim 1 is oxygenated biomembrane reaction component, it is characterised in that：The water flow pull unit
(21) include magnetic field ball (211), stress magnetic field wheel (212), sliding rail (213), pull rope (214), fixed ring (215), the magnetic
Field ball (211) and stress magnetic field wheel (212) are located on same level center line, and the stress magnetic field wheel (212) is embedded in sliding rail
(213) inside groove and flexible connection, described pulling rope (214) one end are connected with stress magnetic field wheel (212), the pulling rope
(214) it is connected far from stress magnetic field wheel (212) one end with fixed ring (215).
8. film bubble formula according to claim 1 is oxygenated biomembrane reaction component, it is characterised in that：At the hollow-fibre membrane
Reason layer (210) includes hollow process layer (2101), hollow-fibre membrane (2102), air output end (2103), filtering backstop
(2104), biomembrane (2105), cohesive end (2106), there are two hollow-fibre membranes for hollow process layer (2101) the two sides installation
(2102), the air output end (2103) is located above hollow-fibre membrane (2102) and mutually connects, the filtering backstop
(2104) it is installed between air output end (2103) and hollow-fibre membrane (2102), the cohesive end (2106) and hollow processing
Layer (2101) is mutually connected, and the biomembrane (2105) is connected by cohesive end (2106) with hollow process layer (2101).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810801887.2A CN108892226A (en) | 2018-07-20 | 2018-07-20 | Film bubble formula is oxygenated biomembrane reaction component |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810801887.2A CN108892226A (en) | 2018-07-20 | 2018-07-20 | Film bubble formula is oxygenated biomembrane reaction component |
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| Publication Number | Publication Date |
|---|---|
| CN108892226A true CN108892226A (en) | 2018-11-27 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201810801887.2A Withdrawn CN108892226A (en) | 2018-07-20 | 2018-07-20 | Film bubble formula is oxygenated biomembrane reaction component |
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| CN (1) | CN108892226A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001200571A (en) * | 2000-01-20 | 2001-07-27 | Miyazawa Kogyo Kk | Method and device for cleaning and circulating sewage water for toilet |
| CN101663083A (en) * | 2007-05-22 | 2010-03-03 | 旭化成化学株式会社 | Hollow fiber membrane module, process for manufacturing the same, hollow fiber membrane module assembly and method of purifying suspended water with use thereof |
| CN206126948U (en) * | 2016-10-20 | 2017-04-26 | 北京中科众联新能源技术服务有限公司 | Rotation type MABR reactor |
-
2018
- 2018-07-20 CN CN201810801887.2A patent/CN108892226A/en not_active Withdrawn
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001200571A (en) * | 2000-01-20 | 2001-07-27 | Miyazawa Kogyo Kk | Method and device for cleaning and circulating sewage water for toilet |
| CN101663083A (en) * | 2007-05-22 | 2010-03-03 | 旭化成化学株式会社 | Hollow fiber membrane module, process for manufacturing the same, hollow fiber membrane module assembly and method of purifying suspended water with use thereof |
| CN206126948U (en) * | 2016-10-20 | 2017-04-26 | 北京中科众联新能源技术服务有限公司 | Rotation type MABR reactor |
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Application publication date: 20181127 |