WO2017121106A1 - 一种自动离线气水联合冲洗的mbr膜生物反应器 - Google Patents

一种自动离线气水联合冲洗的mbr膜生物反应器 Download PDF

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Publication number
WO2017121106A1
WO2017121106A1 PCT/CN2016/093057 CN2016093057W WO2017121106A1 WO 2017121106 A1 WO2017121106 A1 WO 2017121106A1 CN 2016093057 W CN2016093057 W CN 2016093057W WO 2017121106 A1 WO2017121106 A1 WO 2017121106A1
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Prior art keywords
mbr
water
flushing
gas
mbr membrane
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PCT/CN2016/093057
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English (en)
French (fr)
Inventor
陈欣义
温尚龙
石键韵
张艳芳
张浩纯
Original Assignee
广州市广深环保科技有限公司
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Application filed by 广州市广深环保科技有限公司 filed Critical 广州市广深环保科技有限公司
Priority to US15/504,289 priority Critical patent/US10487303B2/en
Priority to MYPI2018001281A priority patent/MY189036A/en
Publication of WO2017121106A1 publication Critical patent/WO2017121106A1/zh

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M47/00—Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
    • C12M47/18—Gas cleaning, e.g. scrubbers; Separation of different gases
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14—Ultrafiltration; Microfiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14—Ultrafiltration; Microfiltration
    • B01D61/18—Apparatus therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14—Ultrafiltration; Microfiltration
    • B01D61/22—Controlling or regulating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
    • B01D65/025—Removal of membrane elements before washing
    • 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
    • C02F3/1273—Submerged membrane bioreactors
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2311/00—Details relating to membrane separation process operations and control
    • B01D2311/26—Further operations combined with membrane separation processes
    • B01D2311/2642—Aggregation, sedimentation, flocculation, precipitation or coagulation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/04—Backflushing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/18—Use of gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/282—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling by spray flush or jet flush
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/40—Automatic control of cleaning processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/44—Specific cleaning apparatus
    • 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
    • C02F2303/16—Regeneration of sorbents, filters
    • 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

Definitions

  • the invention is used in the technical field of sewage treatment, in particular to an MBR membrane bioreactor which automatically combines off-line gas-water combined washing.
  • Membrane bioreactor is an emerging water treatment technology that combines traditional wastewater biological treatment processes with membrane separation technology and has been successfully applied to wastewater treatment.
  • Membrane bioreactors generally consist of a membrane separation module and a bioreactor.
  • the membrane bioreactor is a membrane module placed in a bioreactor. By isolating high concentrations of activated sludge, high COD removal can usually be achieved. rate.
  • Membrane bioreactors are designed with a focus on a highly efficient membrane cleaning system.
  • Alternative methods include water backwashing, gas washing, and chemical cleaning.
  • problems in the offline cleaning of the MBR membrane bioreactor the cumbersome manual operation, the incomplete cleaning, and the poor recovery performance.
  • the present invention provides an MBR membrane bioreactor which is simple in operation, thorough in cleaning, and reduces manual operation load by automatic off-line gas-water combined rinsing.
  • an MBR membrane bioreactor with automatic off-line gas-water combined flushing comprising a PLC automatic control cabinet, an MBR reactor, and an MBR membrane module disposed in the MBR reactor.
  • a rotating cover disposed on the top of the MBR reactor the top of the MBR reactor is provided with an annular guide rail, the rotating cover is rotatably mounted on the annular guide rail, and the MBR reactor is provided above
  • the MBR membrane assembly is lifted and lifted to a lifting device inside the rotating cover, and the inner wall of the rotating cover is provided with a flushing pipe network, and the flushing pipe net is provided with an outer interface on the outer side of the rotating cover, and the outer interface passes through the three-way
  • the reversing valve is connected to the gas flushing pipe and the water flushing pipe, and the gas flushing pipe is externally connected to the air pump, the water flushing pipe is externally connected to the water pump, and the three-way reversing valve is an electromagnetic reversing valve
  • a microporous aerator is disposed in the MBR reactor below the MBR membrane module.
  • a sludge pipe is disposed at a bottom of the MBR reactor, and a sludge pump is disposed on the sludge pipe outside the MBR reactor, and the sludge pump is connected to the PLC automatic control cabinet. .
  • the bottom of the MBR reactor forms a tapered sludge tank.
  • the MBR membrane module is externally connected with a production water pipe, and the production water pipe is provided with a production water pump outside the MBR reactor, and the production water pump is connected with the PLC automatic control cabinet.
  • a negative pressure pressure gauge is arranged on the water production pipe between the MBR membrane component and the production water pump, and a water production flowmeter is provided on the production water pipe externally connected to the production water pump, and the negative pressure pressure gauge and the PLC automatic control Control cabinet connection.
  • a liquid level gauge is provided in the MBR reactor.
  • the lifting device comprises a hoisting machine, a reversing pulley disposed above the MBR reactor, and a traction cable connected to the MBR membrane assembly after being taken out by the hoisting machine and bypassing the reversing pulley.
  • the bottom of the reversing pulley is provided with a travel switch, and the winch and the travel switch are all connected with the PLC automatic control cabinet.
  • the invention has the beneficial effects that the invention adopts the whole PLC automatic control system control, and the PLC automatic control system controls and controls the lifting device to lift the MBR membrane assembly in the MBR reactor upwards into the automatic offline high-pressure washing stage; the MBR membrane assembly is lifted into the rotating cover, Stop rising, at this time, the PLC automatic control cabinet feedback to the pressure flushing pump (air pump, water pump), flexible adjustment of the gas or water to the flushing pipe network through the reversing three-way valve, when the nozzle sprays gas or water, in the recoil force Under the action of the rotating cover, the rotating cover automatically rotates, so that the sprayed gas or water flushes the MBR membrane module without dead angle, and the flushing is complete; the design adopts the air flushing and the water flushing combined flushing, and the flushing method can firstly be flushed, flushed and rehydrated.
  • the pressure flushing pump air pump, water pump
  • Gas combined rushing can also be the first water rushing, gas rushing and then water and gas combined rushing, or water and gas combined flushing and then water and gas separately flushing, the order is not limited, the final rinse is subject to.
  • the device is equipped with an automatic cleaning device in the traditional MBR membrane bioreactor, which realizes automatic flushing without manual operation, fully automatic flushing and reduces manual operation load; the flushing device adopts automatic rotating device to realize 360 degree without dead angle omnidirectional flushing; Combined backflushing method, flexible combination of multiple flushing methods.
  • Figure 1 is a schematic view of the structure of the present invention.
  • FIG. 1 there is shown a specific structure of a preferred embodiment of the present invention.
  • the structural features of the various elements of the present invention will be described in detail below, and if there is a description to the direction ( The upper, lower, left, right, front, and rear are described with reference to the structure shown in FIG. 1, but the actual use direction of the present invention is not limited thereto.
  • the present invention provides an MBR membrane bioreactor for automatic off-line gas-water combined rinsing, comprising an MBR reactor 1, an MBR membrane module 2 disposed in the MBR reactor 1, and a top portion of the MBR reactor 1
  • the cover 3 is rotated, and a liquid level gauge 4 is disposed in the MBR reactor 1, and a microporous aerator 5 is disposed in the MBR reactor 1 below the MBR membrane module 2.
  • the top of the MBR reactor 1 is provided with an annular guide rail 6.
  • the rotating cover 3 is rotatably mounted on the annular guide rail 6.
  • a rotating or lubricating oil film is arranged between the rotating cover 3 and the annular guide rail 6.
  • the inner wall of the rotating cover 3 is provided with a flushing pipe net 9, and the flushing pipe net 9 is provided with an outer interface on the outer side of the rotating cover 3, and the outer interface is connected to the air punching pipe and the water flush through the three-way switching valve 10.
  • the water pump is externally connected to the air pump, and the water flushing tube is externally connected to the water pump.
  • the flushing pipe network 9 is provided with a plurality of nozzles which are inclined to point inside the rotating cover, and the nozzles can generate a rotating rotating cover 3 when the gas or water is sprayed.
  • the recoil of the ring guide 6 (counterclockwise or clockwise).
  • the bottom of the MBR reactor 1 forms a tapered sludge tank 11 in which sludge generated by water treatment is deposited.
  • a sludge pipe 12 is disposed at the bottom of the MBR reactor 1, and a sludge pump 13 is disposed on the sludge pipe 12 outside the MBR reactor 1, and the sludge pump 13 continuously or intermittently places the sludge tank 11 therein. Sludge is discharged.
  • the MBR membrane module 2 is externally connected to a production water pipe 14, on which a production water pump 15 is provided outside the MBR reactor 1.
  • a water pressure gauge 16 is disposed on the water production pipe 14 between the MBR membrane module 2 and the production water pump 15, and a water production flow meter 17 is disposed on the water production pipe 14 external to the production water pump 15.
  • the three-way reversing valve 10 is an electromagnetic reversing valve, and further includes a PLC automatic control cabinet 18 and a stroke switch disposed at the bottom of the diverting pulley 7, the hoisting machine, the negative pressure pressure gauge 16, the production water pump 15, and the sewage
  • the mud pump 13, the stroke switch, the air pump, the water pump and the three-way reversing valve 10 are all connected to the PLC automatic control cabinet 18.
  • the device is controlled by a full PLC automatic control system.
  • the signal of the negative pressure pressure gauge 16 is linked with the hoist of the lifting device, and the production pump 15 works.
  • the alarm 19 automatically alarms, and the shutdown is performed at this time.
  • MBR other auxiliary equipment such as production pump 15, sludge pump 13, etc.
  • negative pressure gauge 16 signal feedback to PLC automatic control cabinet 18, automatic control system signal feedback to the lifting device, into the automatic offline high-pressure washing stage; winch will MBR membrane
  • the component 2 is lifted to a certain height, touches the travel switch, and stops rising.
  • the travel switch feedback signal is sent to the PLC automatic control cabinet 18, and the PLC automatic control cabinet 18 feeds back to the pressure flushing pump (air pump, water pump) to start the pressurization.
  • the pressure flushing pump air pump, water pump
  • the flushing is completed without any dead angle, and the flushing is thorough; the design adopts the air flushing and water flushing combined flushing procedure, and the flushing method can be combined with air flushing, water flushing and water and gas flushing. It may be the first flush, water and gas joint air impact then red, water vapor can also be co-rinse and then rinse water and gas are separated, is not limited in various orders, subject to the final rinse.
  • the PLC automatic control cabinet starts the lifting device according to the setting program, and the MBR membrane module 2 is lowered, so that the system can be re-run.
  • the invention adopts PLC programming setting, the system flushing is completed by the PLC automatic control program, and the human error is reduced; the system control is performed by the negative pressure pressure gauge 16 transmission and the liquid level gauge 4 joint control execution, reducing the program error; the alarm 19 can be Realize the alarms of various operating procedures of the system, remind the operator to pay attention to the operating status of the system, and solve the emergency problems in time.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Microbiology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Health & Medical Sciences (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Zoology (AREA)
  • Biotechnology (AREA)
  • Wood Science & Technology (AREA)
  • General Engineering & Computer Science (AREA)
  • Genetics & Genomics (AREA)
  • Sustainable Development (AREA)
  • Biomedical Technology (AREA)
  • General Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

一种自动离线气水联合冲洗的MBR膜生物反应器，包括PLC自控控制柜(18)、MBR反应器(1)、MBR膜组件(2)以及转动罩(3)，MBR反应器(1)的顶部设有环形导轨(6)，转动罩(3)装在环形导轨(6)上，MBR反应器(1)上方设有升降装置，转动罩(3)的内壁上设有冲洗管网(9)，冲洗管网(9)设有外接口，外接口通过三通换向阀(10)连接气冲管和水冲管，气冲管外接气泵，水冲管外接水泵，三通换向阀(10)为电磁换向阀，气泵、水泵以及三通换向阀均与PLC自控控制柜(18)连接，冲洗管网(9)上设有若干喷口，喷口喷出气或水时可产生推动转动罩(3)沿环形导轨(6)转动的反冲力。

Description

一种自动离线气水联合冲洗的MBR膜生物反应器
技术领域
本发明用于污水处理技术领域，特别是涉及一种自动离线气水联合冲洗的MBR膜生物反应器。
背景技术
膜生物反应器（Membrane Bioreactor-MBR）的处理工艺是一项新兴的水处理技术，是传统污水生物处理工艺与膜分离技术的有机结合，已成功地应用于污水处理。膜生物反应器一般由膜分离组件及生物反应器两部分组成，一般膜生物反应器是将膜组件置于生物反应器内，通过隔离高浓度的活性污泥，通常能够达到较高的COD去除率。
膜生物反应器的设计重点是一套高效率的膜清洗系统，可选择的方法包括水反冲洗、气洗、化学药剂清洗等。现有技术中对MBR膜生物反应器离线清洗存在困难、人工操作繁琐、清洗不彻底、恢复性能不佳等问题。
发明内容
为解决上述问题，本发明提供一种操作简单、清洗彻底，减少人工操作负荷的自动离线气水联合冲洗的MBR膜生物反应器。
本发明解决其技术问题所采用的技术方案是：一种自动离线气水联合冲洗的MBR膜生物反应器，包括PLC自控控制柜、MBR反应器、设在所述MBR反应器内的MBR膜组件以及设在所述MBR反应器顶部的转动罩，所述MBR反应器的顶部设有环形导轨，所述转动罩可转动的装在所述环形导轨上，所述MBR反应器上方设有可将MBR膜组件吊起并提升至转动罩内部的升降装置，所述转动罩的内壁上设有冲洗管网，所述冲洗管网在转动罩的外侧设有外接口，所述外接口通过三通换向阀连接气冲管和水冲管，气冲管外接气泵，所述水冲管外接水泵，所述三通换向阀为电磁换向阀，气泵、水泵以及三通换向阀均与所述PLC自控控制柜连接，所述冲洗管网上设有若干倾斜指向转动罩内部的喷口，所述喷口喷出气或水时可产生推动转动罩沿环形导轨转动的反冲力。
进一步作为本发明技术方案的改进，所述MBR反应器内在MBR膜组件的下方设有微孔曝气器。
进一步作为本发明技术方案的改进，所述MBR反应器的底部设有污泥管，所述污泥管上在MBR反应器外部设有污泥泵，污泥泵与所述PLC自控控制柜连接。
进一步作为本发明技术方案的改进，所述MBR反应器的底部形成锥形的污泥槽。
进一步作为本发明技术方案的改进，MBR膜组件外接产水管，所述产水管上在MBR反应器外部设有产水泵，产水泵与所述PLC自控控制柜连接。
进一步作为本发明技术方案的改进，MBR膜组件与产水泵间的产水管上设有负压压力表，产水泵外接的产水管上设有产水流量计，负压压力表与所述PLC自控控制柜连接。
进一步作为本发明技术方案的改进，所述MBR反应器内设有液位计。
进一步作为本发明技术方案的改进，所述升降装置包括卷扬机、设在MBR反应器上方的换向滑轮以及由卷扬机引出后绕过所述换向滑轮后与所述MBR膜组件连接的牵引索，所述换向滑轮的底部设有行程开关，所述卷扬机、行程开关均与所述PLC自控控制柜连接。
本发明的有益效果：本发明采用全PLC自控系统控制，PLC自控系统控制控制升降装置将MBR反应器内的MBR膜组件向上提起，进入自动离线高压冲洗阶段；MBR膜组件提升至转动罩内，停止上升，此时，PLC自控控制柜反馈至加压冲洗泵（气泵、水泵），通过换向三通阀灵活调整向冲洗管网注入气或水，喷口喷出气或水时，在反冲力的作用下转动罩自动旋转，使得喷出的气或水对MBR膜组件冲洗无死角，冲洗彻底；本设计采用气冲、水冲联合冲洗，冲洗的方式既可以先气冲、水冲再水气联合冲，也可以是先水冲、气冲再水气联合冲，也可以是水气联合冲洗再水气分开冲洗，各种次序不做限制，以最终冲洗干净为准。本装置在传统的MBR膜生物反应器增设自动清洗装置，实现自动冲洗不用人工操作，全自动化冲洗，减少人工操作负荷；冲洗装置采用自动旋转装置，实现360度无死角全方位冲洗；采用气水联合反冲方式，实现多种冲洗方式灵活组合。
附图说明
下面结合附图对本发明作进一步说明：
图1是本发明结构示意图。
具体实施方式
参照图1，其显示出了本发明之较佳实施例的具体结构。以下将详细说明本发明各元件的结构特点，而如果有描述到方向( 上、下、左、右、前及后) 时，是以图1所示的结构为参考描述，但本发明的实际使用方向并不局限于此。
本发明提供了一种自动离线气水联合冲洗的MBR膜生物反应器，包括MBR反应器1、设在所述MBR反应器1内的MBR膜组件2以及设在所述MBR反应器1顶部的转动罩3，所述MBR反应器1内设有液位计4，所述MBR反应器1内在MBR膜组件2的下方设有微孔曝气器5。所述MBR反应器1的顶部设有环形导轨6，所述转动罩3可转动的装在所述环形导轨6上，转动罩3与环形导轨6间设有轮组或润滑油膜，所述MBR反应器1上方设有可将MBR膜组件2吊起并提升至转动罩3内部的升降装置，所述升降装置包括卷扬机、设在MBR反应器1上方的换向滑轮7以及由卷扬机引出后绕过所述换向滑轮7后与所述MBR膜组件2连接的牵引索8，卷扬机可通过牵引索8提起或降下MBR膜组件2。所述转动罩3的内壁上设有冲洗管网9，所述冲洗管网9在转动罩3的外侧设有外接口，所述外接口通过三通换向阀10连接气冲管和水冲管，气冲管外接气泵，所述水冲管外接水泵，所述冲洗管网9上设有若干倾斜指向转动罩内部的喷口，所述喷口喷出气或水时可产生推动转动罩3沿环形导轨6（逆时针或顺时针）转动的反冲力。
所述MBR反应器1的底部形成锥形的污泥槽11，水处理产生的污泥沉积在污泥槽11内。所述MBR反应器1的底部设有污泥管12，所述污泥管12上在MBR反应器1外部设有污泥泵13，污泥泵13连续或间歇的将污泥槽11内的污泥排出。
MBR膜组件2外接产水管14，所述产水管14上在MBR反应器1外部设有产水泵15。MBR膜组件2与产水泵15间的产水管14上设有负压压力表16，产水泵15外接的产水管14上设有产水流量计17。
所述三通换向阀10为电磁换向阀，还包括PLC自控控制柜18和设在所述换向滑轮7底部的行程开关，所述卷扬机、负压压力表16、产水泵15、污泥泵13、行程开关、气泵、水泵以及三通换向阀10均与所述PLC自控控制柜18连接。
本装置采用全PLC自控系统控制，负压压力表16信号与升降装置的卷扬机联动，产水泵15工作，负压压力表16压力数据达到设定值时，报警器19自动报警，此时关停MBR其他附属设备(如产水泵15、污泥泵13等)，负压压力表16信号反馈到PLC自控控制柜18，自控系统信号反馈到升降装置，进入自动离线高压冲洗阶段；卷扬机将MBR膜组件2提升至一定高度，触碰到行程开关，停止上升，此时，行程开关反馈信号至PLC自控控制柜18，PLC自控控制柜18反馈至加压冲洗泵（气泵、水泵），启动加压冲洗泵，开始自动反冲洗程序，自动反冲洗水洗8min，水泵停，开启自动气冲洗2min，时间均可以灵活调整；喷口喷出气或水时，在反冲力的作用下转动罩3自动旋转，使到冲洗无死角，冲洗彻底；本设计采用气冲、水冲联合冲洗程序，冲洗的方式既可以先气冲、水冲再水气联合冲，也可以是先水冲、气冲再水气联合冲，也可以是水气联合冲洗再水气分开冲洗，各种次序不做限制，以最终冲洗干净为准。
冲洗完毕后，PLC自控控制柜反按照设定程序启动升降装置，将MBR膜组件2下放，可以实现系统重新运行。本发明采用PLC编程设定，系统冲洗完成由PLC自动控制程序执行，减少人为误差；本系统控制由负压压力表16传输及液位计4联合控制执行，减少程序误差；报警器19可以是实现系统各个运作程序的警报，起到提醒操作人员注意系统的运行状态，及时解决应急问题。
当然，本发明创造并不局限于上述实施方式，熟悉本领域的技术人员在不违背本发明精神的前提下还可作出等同变形或替换，这些等同的变型或替换均包含在本申请权利要求所限定的范围内。

Claims (8)

  1. 一种自动离线气水联合冲洗的MBR膜生物反应器，其特征在于：包括PLC自控控制柜、MBR反应器、设在所述MBR反应器内的MBR膜组件以及设在所述MBR反应器顶部的转动罩，所述MBR反应器的顶部设有环形导轨，所述转动罩可转动的装在所述环形导轨上，所述MBR反应器上方设有可将MBR膜组件吊起并提升至转动罩内部的升降装置，所述转动罩的内壁上设有冲洗管网，所述冲洗管网在转动罩的外侧设有外接口，所述外接口通过三通换向阀连接气冲管和水冲管，气冲管外接气泵，所述水冲管外接水泵，所述三通换向阀为电磁换向阀，气泵、水泵以及三通换向阀均与所述PLC自控控制柜连接，所述冲洗管网上设有若干倾斜指向转动罩内部的喷口，所述喷口喷出气或水时可产生推动转动罩沿环形导轨转动的反冲力。
  2. 根据权利要求1所述的自动离线气水联合冲洗的MBR膜生物反应器，其特征在于：所述MBR反应器内在MBR膜组件的下方设有微孔曝气器。
  3. 根据权利要求1所述的自动离线气水联合冲洗的MBR膜生物反应器，其特征在于：所述MBR反应器的底部设有污泥管，所述污泥管上在MBR反应器外部设有污泥泵，污泥泵与所述PLC自控控制柜连接。
  4. 根据权利要求3所述的自动离线气水联合冲洗的MBR膜生物反应器，其特征在于：所述MBR反应器的底部形成锥形的污泥槽。
  5. 根据权利要求1所述的自动离线气水联合冲洗的MBR膜生物反应器，其特征在于：MBR膜组件外接产水管，所述产水管上在MBR反应器外部设有产水泵，产水泵与所述PLC自控控制柜连接。
  6. 根据权利要求5所述的自动离线气水联合冲洗的MBR膜生物反应器，其特征在于：MBR膜组件与产水泵间的产水管上设有负压压力表，产水泵外接的产水管上设有产水流量计，负压压力表与所述PLC自控控制柜连接。
  7. 根据权利要求1所述的自动离线气水联合冲洗的MBR膜生物反应器，其特征在于：所述MBR反应器内设有液位计。
  8. 根据权利要求1所述的自动离线气水联合冲洗的MBR膜生物反应器，其特征在于：所述升降装置包括卷扬机、设在MBR反应器上方的换向滑轮以及由卷扬机引出后绕过所述换向滑轮后与所述MBR膜组件连接的牵引索，所述换向滑轮的底部设有行程开关，所述卷扬机、行程开关均与所述PLC自控控制柜连接。
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