CN206328210U - Movable container formula integration CMBR membrane biological reaction sewage-treatment plants - Google Patents
Movable container formula integration CMBR membrane biological reaction sewage-treatment plants Download PDFInfo
- Publication number
- CN206328210U CN206328210U CN201621494539.8U CN201621494539U CN206328210U CN 206328210 U CN206328210 U CN 206328210U CN 201621494539 U CN201621494539 U CN 201621494539U CN 206328210 U CN206328210 U CN 206328210U
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- Prior art keywords
- pipe
- sewage
- membrane
- water
- membrane module
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- Expired - Fee Related
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- 239000012528 membrane Substances 0.000 title claims abstract description 97
- 239000010865 sewage Substances 0.000 title claims abstract description 62
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 50
- 230000010354 integration Effects 0.000 title claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 90
- 238000005273 aeration Methods 0.000 claims abstract description 44
- 239000012530 fluid Substances 0.000 claims abstract description 11
- 238000004140 cleaning Methods 0.000 claims description 28
- 230000037452 priming Effects 0.000 claims description 24
- 239000000945 filler Substances 0.000 claims description 19
- 239000010802 sludge Substances 0.000 claims description 17
- 239000000126 substance Substances 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 11
- 241000282326 Felis catus Species 0.000 claims description 8
- 230000001954 sterilising effect Effects 0.000 claims description 8
- 238000004659 sterilization and disinfection Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 7
- 238000012856 packing Methods 0.000 claims description 7
- 239000006228 supernatant Substances 0.000 claims description 5
- 239000004744 fabric Substances 0.000 claims 1
- 238000010276 construction Methods 0.000 abstract description 5
- 238000013461 design Methods 0.000 abstract description 5
- 230000015572 biosynthetic process Effects 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 4
- 239000005416 organic matter Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000000249 desinfective effect Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000002262 irrigation Effects 0.000 description 2
- 238000003973 irrigation Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000006396 nitration reaction Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000012876 topography Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a kind of movable container formula integration CMBR membrane biological reaction sewage-treatment plants；The device is provided with bio-reaction zone and battery limits, and sewage is by a series of biological respinses of Anoxic/Aerobic in bio-reaction zone, and organic matter is able to degraded and removed；The device is provided with membrane module, membrane module deflector, Aeration fan, air supply pipe, aeration tube in bio-reaction zone, aeration tube is aerated into water, make sewage under aeration effect, along membrane module deflector formation from bottom to top be thoroughly mixed fluid, realize the alternate cycles environment of sewage Anoxic/Aerobic Anoxic/Aerobic；Meanwhile, the aeration source of the gas of the device is provided by an Aeration fan, is equipped with PLC control cabinet control, being capable of the intelligent achievable unattended operation of operation；The device is designed using packaged type, novel in design, high degree of automation, and operating cost is low, construction is simple, and dilatation is convenient, flexible, there is the popularization and application and popularization using rural domestic sewage treatment.
Description
Technical field
The utility model is related to movable container formula integration CMBR membrane biological reaction sewage-treatment plants, belongs to sewage
Processing equipment technical field.
Background technology
With the continuous propulsion of Rural Urbanization Construction, life of farmers level is improved constantly, and flush toilet starts in peasant household
Popularization, washing, shower water increase.Because rural residence environment is complicated, the Living Style of people more disperses and not collected relatively
In, sewage network is not formed, sewage is in uncontrollable discharge, and not only the production and life to local resident and surrounding enviroment are caused
Influence, be just directly discharged into rivers and lakes, pond waters moreover, most of domestic sewage in rural areas are unprocessed to a certain degree,
Cause the environment such as river, underground drinking water source, rainwash, agricultural land soil by different degrees of pollution.
For country sewage problem at this stage, treatment technology is also varied, by geographical environment and topography and geomorphology ring
Border influences, and large area laying sewage network difficulty of construction is larger, with the raising of countryside sewage treating discharge standard, relatively success
Efficient process technology AO+MBR membrane treatment process applied in field of Environment Protection than wide, water outlet quality better, but its technique stream
Journey is longer, and operating cost is of a relatively high, and energy-saving effect is poor, adds overall economic input and operating cost；Meanwhile, for agriculture
The special areas such as village tourist attractions, scenic spot, station terminal, civil engineering is difficult, and equipment installs dumb, and to sudden water
Contamination accident can not tackle processing.
Utility model content
The purpose of this utility model is integrated there is provided a kind of movable container formula in order to solve the above problems
CMBR membrane biological reaction sewage-treatment plants；The device is provided with bio-reaction zone and battery limits two parts, in bio-reaction zone
Interior sewage is by a series of biological respinses of anaerobic-aerobic, and organic matter is able to degraded and removed；Moreover, the device is in bio-reaction zone
Interior to be provided with membrane module, membrane module deflector, Aeration fan, air supply pipe, aeration tube, aeration tube is aerated into water, sewage is existed
Aeration effect under, along membrane module deflector formation from bottom to top be thoroughly mixed fluid, realize sewage anaerobic-aerobic-lack
The alternate cycles environment of oxygen-aerobic；Meanwhile, the aeration source of the gas of the device is provided by an Aeration fan, is equipped with PLC control cabinet control
System, being capable of the intelligent achievable unattended operation of operation；In addition, the device is designed using packaged type, not only novel in design,
High degree of automation, also operating cost are low, construction is simple, due to using modularized design, and dilatation is convenient, flexible, effluent quality
Landscape planting, field irrigation, aqiuculrue, carwash can be back to nearby the purposes such as to flush the toilet, and utilize rural domestic sewage treatment
Popularization and application and popularization.
In order to achieve the above object, the utility model is realized by following technological means.
A kind of movable container formula integration CMBR membrane biological reaction sewage-treatment plants, it by Membrane cleaning chemical feed pipe,
Recoil water pipe, Membrane cleaning grug feeding jar, Membrane cleaning dosing pump, ultraviolet sterilization instrument, backwash water pump, self-priming water pump outlet pipe, aeration wind
Machine, overflow returning pipe, self priming pump suction tube, blowoff valve, water inlet pipe, hair filter, sewage water inlet pipe, overflow pipe, water inlet are worn
Hole water distributor, membrane module, membrane module deflector, dividing plate, bio-reaction zone, filler support, air supply pipe, self priming pump, aeration tube, film
Fluid level controller, biologic packing material bed part are constituted, it is characterized in that：Casing top surrounding is provided with guardrail, and casing top is provided with
Two membrane module holes for hoist, passage, manholes, casing side are provided with outer cat ladder, if casing front end be provided with power supply introduction hole,
Equipment room, bio-reaction zone are provided with dry blowoff valve, casing；
Described equipment room, bio-reaction zone are spaced by dividing plate, interior cat ladder are provided with dividing plate, equipment room upper end is set
It is equipped with vent window, equipment room and is provided with Aeration fan, self priming pump, PLC control cabinet, self priming pump one end passes through pipeline, ultraviolet
Disinfecting instrument is connected with self-priming water pump outlet pipe, and the self priming pump other end passes through film water producing pipe and two respectively by self priming pump suction tube
Membrane module is connected, and Membrane cleaning chemical feed pipe, recoil water pipe are respectively arranged with self priming pump suction tube, and Membrane cleaning chemical feed pipe passes through film
Cleaning dosing pump is connected with Membrane cleaning grug feeding jar, and recoil water pipe is connected by backwash water pump, accurate filter with backwash water tank
Connect, Aeration fan is connected by air supply pipe with aeration tube, some circular holes are provided with aeration tube；
Film liquid level controller, three groups of filler supports are provided with described bio-reaction zone, if being provided with filler support
Dry biologic packing material bed, filler support upper end is provided with overflow returning pipe, and overflow returning pipe is fixed on by overflow back water pipe holder
In casing, filler support lower end is provided with into water and perforated water distributor, is provided with membrane module between filler support, membrane module both sides are set
Membrane module deflector is equipped with, membrane module deflector is fixed in casing by bearing, and membrane module lower end is provided with aeration tube, sewage
Water inlet pipe one end is connected through casing with water inlet perforation water distributor, and the sewage water inlet pipe other end passes through hair filter and water inlet
Pipe is connected, and the water inlet pipe other end is connected through anoxic pond with two elevator pumps, and fluid level controller is provided with anoxic pond, lacks
Oxygen pond side is provided with comprehensive adjustment pond, and comprehensive adjustment pond side is connected by conduit with grid canal, and comprehensive adjustment pond passes through
Overflow pipe is connected with overflow returning pipe, and comprehensive adjustment pond is connected by supernatant return duct with sludge concentration tank, and sludge is dense
Contracting pond is connected by sludge sludge pipe with blowoff valve.
Described ultraviolet sterilization instrument, Aeration fan, self priming pump, film liquid level controller, fluid level controller, elevator pump pass through
Wire is connected with PLC control cabinet, power supply.
Operation principle：First, sewage enters grid pond through sewage water inlet pipe, and sewage is retained through the grid in grid pond and suspended
Thing enters after comprehensive adjustment pond, oil removal sand setting, and into anoxic pond, boosted pump, hair filter enter bio-reaction zone, aeration
Blower fan is aerated by air supply pipe, aeration tube into sewage, make sewage along membrane module deflector formation from bottom to top completely mix
Collaborate body, sewage is carried out degradation of organic substances in membrane module, the alternate cycles by anoxic-good foster-anaerobic-aerobic environment are anti-
Should, it nitrify and anti-nitration reaction, ammonia nitrogen in sewage polluter is converted into N2 and removed, the CMBR films area in bio-reaction zone
In domain, the microorganism that CMBR membrane modules are relied on microbial reaction is separated from sewage, and microorganism is able in CMBR films
Remained in reaction tank, organic concentration content is high in sewage, it is biodegradable complete；Then, started certainly by PLC control cabinet
Sucking pump, the water outlet of CMBR membrane cisternas is discharged through pipeline, ultraviolet ray disinfector to self-priming water pump outlet pipe.
Meanwhile, when the sewage water surface in bio-reaction zone exceedes the height of overflow returning pipe, sewage is through overflow returning pipe
Flow into and enter anoxic zone in comprehensive adjustment area, complete anti-nitration reaction.The sludge of the precipitation produced in bio-reaction zone is through blowdown
Valve is discharged into sludge concentration tank, and sludge periodically draws clearly outward transport after digestion process, and supernatant is back to comprehensive adjustment pond, moreover,
The operation maintenance of CMBR membrane modules is rinsed using water and decoction cleans two kinds of forms, and water backwashing passes through backwash water tank, accurate mistake
Filter, back suction water pump carry out periodic cleaning to membrane module, and Membrane cleaning liquid is soaked using the backwash of sodium hypochlorite liquid, obtains membrane flux
To recover, decoction supplies CMBR membrane modules by Membrane cleaning grug feeding jar, Membrane cleaning dosing pump, Membrane cleaning chemical feed pipe and entered in membrane tube
Portion.
The utility model mainly has the advantages that：
1st, the device is provided with bio-reaction zone and battery limits two parts, and sewage passes through anoxic-good in bio-reaction zone
A series of biological respinses of oxygen, organic matter is able to degraded and removed.
2nd, the device is provided with membrane module, membrane module deflector, Aeration fan, air supply pipe, aeration in bio-reaction zone
Pipe, aeration tube is aerated into water, makes sewage under aeration effect, along membrane module deflector formation being thoroughly mixed from bottom to top
Fluid, realizes the alternate cycles environment of sewage anaerobic-aerobic-anaerobic-aerobic.
3rd, the aeration source of the gas of the device is provided by an Aeration fan, is equipped with PLC control cabinet control, intelligent can be run
Unattended operation can be achieved.
4th, the device is designed using packaged type, not only novel in design, high degree of automation, and also operating cost is low, construct
Simply, due to using modularized design, dilatation is convenient, flexibly, effluent quality can be back to nearby landscape planting, field irrigation,
Aqiuculrue, carwash such as are flushed the toilet at the purposes, there is the popularization and application and popularization using rural domestic sewage treatment.
Brief description of the drawings
Accompanying drawing 1 is the inside of the utility model movable container formula integration CMBR membrane biological reaction sewage-treatment plants
Overlooking the structure diagram.
Accompanying drawing 2 is the outside of the utility model movable container formula integration CMBR membrane biological reaction sewage-treatment plants
Overlooking the structure diagram.
Accompanying drawing 3 is the D-D of the utility model movable container formula integration CMBR membrane biological reaction sewage-treatment plants
To cross-sectional view.
Accompanying drawing 4 is the A-A of the utility model movable container formula integration CMBR membrane biological reaction sewage-treatment plants
To cross-sectional view.
Accompanying drawing 5 is the B-B of the utility model movable container formula integration CMBR membrane biological reaction sewage-treatment plants
To cross-sectional view.
Accompanying drawing 6 is the C-C of the utility model movable container formula integration CMBR membrane biological reaction sewage-treatment plants
To cross-sectional view.
Accompanying drawing 7 is the left view of the utility model movable container formula integration CMBR membrane biological reaction sewage-treatment plants
Structural representation.
Accompanying drawing 8 is that the right side of the utility model movable container formula integration CMBR membrane biological reaction sewage-treatment plants is regarded
Structural representation.
Accompanying drawing 9 is the facade of the utility model movable container formula integration CMBR membrane biological reaction sewage-treatment plants
Structural representation.
Accompanying drawing 10 is the film of the utility model movable container formula integration CMBR membrane biological reaction sewage-treatment plants
Modular construction schematic diagram.
As Figure 1-10 shows, each group of above-mentioned movable container formula integration CMBR membrane biological reaction sewage-treatment plants
Represented into part by following Arabic numerals：
Casing -1, Membrane cleaning chemical feed pipe -2, recoil water pipe -3, Membrane cleaning grug feeding jar -4, Membrane cleaning dosing pump -5, ultraviolet
Disinfecting instrument -6, backwash water pump -7, accurate filter -8, backwash water tank -9, self-priming water pump outlet pipe -10, PLC control cabinet -11, aeration
Blower fan -12, overflow returning pipe -13, self priming pump suction tube -14, blowoff valve -15, outer cat ladder -16, water inlet pipe -17, hair filtering
It is device -18, sewage water inlet pipe -19, overflow pipe -20, water inlet perforation water distributor -21, membrane module -22, membrane module deflector -23, logical
Stomata -24, membrane module hole for hoist -25, manhole -26, dividing plate -27, vent window -28, equipment m- 29, bio-reaction zone -30, shield
Column -31, filler support -32, air supply pipe -33, self priming pump -34, aeration tube -35, film liquid level controller -36, biologic packing material bed -
37th, interior cat ladder -38, film water producing pipe -39, overflow back water pipe holder -40, power supply introduction hole -41, fluid level controller -42, grid
Canal -43, comprehensive adjustment pond -44, anoxic pond -45, elevator pump -46, supernatant return duct -47, sludge concentration tank -48, sludge collection
Mud pipe -49.
With reference to example and Figure of description, the utility model is described in further detail：
Embodiment
Embodiment
As Figure 1-10 shows, a kind of movable container formula integration CMBR membrane biological reaction sewage-treatment plants, it by
Membrane cleaning chemical feed pipe 2, recoil water pipe 3, Membrane cleaning grug feeding jar 4, Membrane cleaning dosing pump 5, ultraviolet sterilization instrument 6, backwash water pump 7,
Self-priming water pump outlet pipe 10, Aeration fan 12, overflow returning pipe 13, self priming pump suction tube 14, blowoff valve 15, water inlet pipe 17, hair
Filter 18, sewage water inlet pipe 19, overflow pipe 20, water inlet perforation water distributor 21, membrane module 22, membrane module deflector 23, dividing plate
27th, bio-reaction zone 30, filler support 32, air supply pipe 33, self priming pump 34, aeration tube 35, film liquid level controller 36, biologic packing material
37 parts of bed composition, it is characterized in that：The top surrounding of casing 1 is provided with guardrail 31, and the top of casing 1 is provided with two membrane module liftings
Hole 25, passage 24, manhole 26, the side of casing 1 are provided with outer cat ladder 16, and the front end of casing 1 is provided with power supply introduction hole 41, some
Equipment room 29, bio-reaction zone 30 are provided with blowoff valve 15, casing 1；
Described equipment room 29, bio-reaction zone 30 are spaced by dividing plate 27, and interior cat ladder 38 is provided with dividing plate 27, if
29 upper ends are provided with vent window 28, equipment room (29) and are provided with Aeration fan 12, self priming pump 34, PLC control cabinet 11 between standby, from
The one end of sucking pump 34 is connected by pipeline, ultraviolet sterilization instrument 6 with self-priming water pump outlet pipe 10, and the other end of self priming pump 34 passes through self-priming
Pumping suction pipe 14 is connected by film water producing pipe 39 with two membrane modules 22 respectively, and film is respectively arranged with self priming pump suction tube 14
Chemical feed pipe 2, recoil water pipe 3 are cleaned, Membrane cleaning chemical feed pipe 2 is connected by Membrane cleaning dosing pump 5 with Membrane cleaning grug feeding jar 4, instead
Jet water spout 3 is connected by backwash water pump 7, accurate filter 8 with backwash water tank 9, and Aeration fan 12 is by air supply pipe 33 with exposing
Tracheae 35 is connected, and some circular holes are provided with aeration tube 35；
It is provided with described bio-reaction zone 30 on film liquid level controller 36, three groups of filler supports 32, filler support 32
Some biologic packing material beds 37 are provided with, the upper end of filler support 32 is provided with overflow returning pipe 13, and overflow returning pipe 13 passes through overflow
Backwater pipe holder 40 is fixed in casing 1, and the lower end of filler support 32 is provided with into water and perforated water distributor 21, between filler support 32
Membrane module 22 is provided with, the both sides of membrane module 22 are provided with membrane module deflector 23, and membrane module deflector 23 is fixed on by bearing
In casing 1, the lower end of membrane module 22 is provided with aeration tube 35, and the one end of sewage water inlet pipe 19 passes through casing 1 and water inlet perforation water distributor
21 are connected, and the other end of sewage water inlet pipe 19 is connected by hair filter 18 with water inlet pipe 17, and the other end of water inlet pipe 17 is worn
Cross anoxic pond 45 with two elevator pumps 46 to be connected, fluid level controller 42 is provided with anoxic pond 45, the side of anoxic pond 45 is set
There is comprehensive adjustment pond 44, the side of comprehensive adjustment pond 44 is connected by conduit with grid canal 43, and comprehensive adjustment pond 44 passes through overflow
Pipe 20 is connected with overflow returning pipe 13, and comprehensive adjustment pond 44 is connected by supernatant return duct 47 with sludge concentration tank 48,
Sludge concentration tank 48 is connected by sludge sludge pipe 49 with blowoff valve 15.
Described ultraviolet sterilization instrument 6, Aeration fan 12, self priming pump 34, film liquid level controller 36, fluid level controller 42,
Elevator pump 46 is connected by wire with PLC control cabinet 11, power supply.
Claims (4)
1. a kind of movable container formula integration CMBR membrane biological reaction sewage-treatment plants, it by Membrane cleaning chemical feed pipe (2),
Recoil water pipe (3), Membrane cleaning grug feeding jar (4), Membrane cleaning dosing pump (5), ultraviolet sterilization instrument (6), backwash water pump (7), self-priming
Water pump outlet pipe (10), Aeration fan (12), overflow returning pipe (13), self priming pump suction tube (14), blowoff valve (15), water inlet pipe
(17), hair filter (18), sewage water inlet pipe (19), overflow pipe (20), water inlet perforation water distributor (21), membrane module (22),
Membrane module deflector (23), dividing plate (27), bio-reaction zone (30), filler support (32), air supply pipe (33), self priming pump (34),
Aeration tube (35), film liquid level controller (36), biologic packing material bed (37) part are constituted, it is characterized in that：Casing (1) top surrounding is set
Guardrail (31) is equipped with, casing (1) top is provided with two membrane module holes for hoist (25), passage (24), manhole (26), casing
(1) side is provided with outer cat ladder (16), and casing (1) front end is provided with power supply introduction hole (41), some blowoff valves (15), casing
(1) equipment room (29), bio-reaction zone (30) are provided with.
2. a kind of movable container formula integration CMBR membrane biological reaction sewage-treatment plants according to claim 1,
It is characterized in that：Equipment room (29), bio-reaction zone (30) are spaced by dividing plate (27), and dividing plate is provided with interior cat ladder on (27)
(38), equipment room (29) upper end is provided with vent window (28), equipment room (29) and is provided with Aeration fan (12), self priming pump
(34), PLC control cabinet (11), self priming pump (34) one end passes through pipeline, ultraviolet sterilization instrument (6) and self-priming water pump outlet pipe (10) phase
Connection, self priming pump (34) other end passes through film water producing pipe (39) and two membrane modules (22) respectively by self priming pump suction tube (14)
It is connected, Membrane cleaning chemical feed pipe (2), recoil water pipe (3), Membrane cleaning chemical feed pipe is respectively arranged with self priming pump suction tube (14)
(2) it is connected by Membrane cleaning dosing pump (5) with Membrane cleaning grug feeding jar (4), recoil water pipe (3) passes through backwash water pump (7), precision
Filter (8) is connected with backwash water tank (9), and Aeration fan (12) is connected by air supply pipe (33) with aeration tube (35), exposes
Tracheae is provided with some circular holes on (35).
3. a kind of movable container formula integration CMBR membrane biological reaction sewage-treatment plants according to claim 1,
It is characterized in that：, film liquid level controller (36), three groups of filler supports (32), filler support are provided with bio-reaction zone (30)
(32) some biologic packing material beds (37) are provided with, filler support (32) upper end is provided with overflow returning pipe (13), overflow back water
Pipe (13) is fixed in casing (1) by overflow back water pipe holder (40), and filler support (32) lower end is provided with into water perforation cloth
Membrane module (22) is provided between water pipe (21), filler support (32), membrane module (22) both sides are provided with membrane module deflector
(23), membrane module deflector (23) is fixed in casing (1) by bearing, and membrane module (22) lower end is provided with aeration tube (35),
Sewage water inlet pipe (19) one end is connected through casing (1) with water inlet perforation water distributor (21), sewage water inlet pipe (19) other end
It is connected by hair filter (18) with water inlet pipe (17), water inlet pipe (17) other end is lifted through anoxic pond (45) with two
Pump (46) is connected, and fluid level controller (42) is provided with anoxic pond (45), and anoxic pond (45) side is provided with comprehensive adjustment pond
(44), comprehensive adjustment pond (44) side is connected by conduit with grid canal (43), and comprehensive adjustment pond (44) pass through overflow pipe
(20) it is connected with overflow returning pipe (13), comprehensive adjustment pond (44) pass through supernatant return duct (47) and sludge concentration tank (48)
It is connected, sludge concentration tank (48) is connected by sludge sludge pipe (49) with blowoff valve (15).
4. a kind of movable container formula integration CMBR membrane biological reaction sewage-treatment plants according to claim 1,
It is characterized in that：Ultraviolet sterilization instrument (6), Aeration fan (12), self priming pump (34), film liquid level controller (36), fluid level controller
(42), elevator pump (46) is connected by wire with PLC control cabinet (11), power supply.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621494539.8U CN206328210U (en) | 2016-12-25 | 2016-12-25 | Movable container formula integration CMBR membrane biological reaction sewage-treatment plants |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621494539.8U CN206328210U (en) | 2016-12-25 | 2016-12-25 | Movable container formula integration CMBR membrane biological reaction sewage-treatment plants |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206328210U true CN206328210U (en) | 2017-07-14 |
Family
ID=59294057
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621494539.8U Expired - Fee Related CN206328210U (en) | 2016-12-25 | 2016-12-25 | Movable container formula integration CMBR membrane biological reaction sewage-treatment plants |
Country Status (1)
| Country | Link |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107226522A (en) * | 2017-07-20 | 2017-10-03 | 金科水务工程(北京)有限公司 | A kind of split type air lift membrane reactor processing unit |
| CN109052831A (en) * | 2018-08-27 | 2018-12-21 | 广东景天环境科技股份有限公司 | A kind of intelligent mobile lavatory water treatment facilities |
-
2016
- 2016-12-25 CN CN201621494539.8U patent/CN206328210U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107226522A (en) * | 2017-07-20 | 2017-10-03 | 金科水务工程(北京)有限公司 | A kind of split type air lift membrane reactor processing unit |
| CN109052831A (en) * | 2018-08-27 | 2018-12-21 | 广东景天环境科技股份有限公司 | A kind of intelligent mobile lavatory water treatment facilities |
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