CN1153738C - Sewage treating plant with double-area gravity-elution membrane bioreactor - Google Patents
Sewage treating plant with double-area gravity-elution membrane bioreactor Download PDFInfo
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- CN1153738C CN1153738C CNB011205865A CN01120586A CN1153738C CN 1153738 C CN1153738 C CN 1153738C CN B011205865 A CNB011205865 A CN B011205865A CN 01120586 A CN01120586 A CN 01120586A CN 1153738 C CN1153738 C CN 1153738C
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- container
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- upflow reactor
- upflow
- membrane
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- 239000012528 membrane Substances 0.000 title claims abstract description 56
- 238000010828 elution Methods 0.000 title description 7
- 239000010865 sewage Substances 0.000 title description 6
- 239000007788 liquid Substances 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 238000005842 biochemical reaction Methods 0.000 claims abstract description 14
- 238000005273 aeration Methods 0.000 claims abstract description 13
- 238000000926 separation method Methods 0.000 claims abstract description 10
- 230000005484 gravity Effects 0.000 claims abstract description 6
- 238000004065 wastewater treatment Methods 0.000 claims abstract 2
- 238000005192 partition Methods 0.000 claims 1
- 239000010802 sludge Substances 0.000 abstract description 18
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 5
- 239000002351 wastewater Substances 0.000 abstract description 5
- 238000006073 displacement reaction Methods 0.000 description 19
- 239000011259 mixed solution Substances 0.000 description 13
- 239000007789 gas Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 230000004907 flux Effects 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 238000010008 shearing Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000005374 membrane filtration Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 244000005706 microflora Species 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Images
Classifications
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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
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Activated Sludge Processes (AREA)
Abstract
本发明属于利用生化技术和膜分离技术处理废水的设备，特别涉及一种双区重力出流式膜生物反应器废水处理设备。该设备由升流式反应器和容器组成；所述的升流式反应器为生化反应区，在升流式反应器中安装有一中心管，在反应器的上部侧壁开有进水口；所述的容器为固液分离区，在容器内安装有膜组件，膜组件的底部布设有曝气管；在容器的上部侧壁开有进气口和出水口，下部开有混合液进入口，升流式反应器的底端与容器相通；穿过升流式反应器的侧壁，安装有将容器与升流式反应器的中心管连通的连通管。本发明不需要抽吸设备，固液分离区顶部与生物反应区中心管连通，被分离的污泥在气体的携带下进入生物反应区，实现曝气量高效利用，可降低运行能耗。
The invention belongs to equipment for treating waste water by using biochemical technology and membrane separation technology, in particular to a double-zone gravity outflow membrane bioreactor waste water treatment equipment. The equipment consists of an upflow reactor and a container; the upflow reactor is a biochemical reaction zone, and a central pipe is installed in the upflow reactor, and a water inlet is opened on the upper side wall of the reactor; The above-mentioned container is a solid-liquid separation area, and a membrane module is installed in the container, and an aeration pipe is arranged at the bottom of the membrane module; an air inlet and a water outlet are opened on the upper side wall of the container, and a mixed liquid inlet is opened on the lower part. The bottom end of the upflow reactor communicates with the container; through the side wall of the upflow reactor, a connecting pipe is installed to connect the container with the central pipe of the upflow reactor. The invention does not require suction equipment, the top of the solid-liquid separation area is connected to the central pipe of the biological reaction area, and the separated sludge enters the biological reaction area under the air, so that the efficient utilization of aeration can be realized and the energy consumption of operation can be reduced.
Description
Technical field
The invention belongs to and utilize biochemical technology and membrane separation technique to handle the equipment of waste water, particularly a kind of double-area gravity-elution membrane bioreactor sewage treatment equipment.
Background technology
Membrane bioreactor is a kind of water technology that is replaced secondary sedimentation basins and sand filter in traditional biochemical processing by membrane filtration.The appearance of membrane bioreactor has improved mud-water separation efficient, simultaneously because the appearance of special efficacy bacterium (particularly dominant microflora) in the increase of activated sludge concentration and the mud in the aeration tank has improved biochemical reaction rate.Simultaneously, reduce the excess sludge generation, thereby solved the outstanding problem that the traditional biological facture exists substantially by reducing sludge loading.
Early stage separate type membrane bioreactor (see figure 4) all adopts cross-flow membrane module, promptly is filtered fluid and is parallel to filtering surface, flows with filtrate is staggered, and consequent shearing force or turbulent flows are with the thickness of restriction cake layer.In order to keep stable permeability rate, crossflow velocity is generally greater than 2m/s, and this just needs higher quantity of circulating water, causes higher unit to produce water consumption.In order to solve membrane bioreactor energy consumption problem of higher, people have researched and developed the integral type film biological reactor (see figure 5), and in integral type film biological reactor, membrane module is directly inserted in the bio-reactor, suction by vacuum pump or other types pump obtains filtered liquid; The cross-flow on film surface is produced by air agitation, aerator be arranged on membrane module under; Mixed solution upwards flows with air-flow, produces shearing force on the film surface, and under the effect of shearing force, minimizing sludge suspension particle adheres to the film surface, allows water see through.
Sludge concentration is the important parameter of membrane bioreactor system, one of key character of membrane bioreactor is a sludge concentration of utilizing the concentrated property raising bio-reactor of height of membrane sepn, thereby increase the organic matter removal ability of bio-reactor, but higher sludge concentration produces negative influence to membrane flux.Under certain condition, sludge concentration is high more, and membrane flux is lower.
Therefore, there is following shortcoming in existing integral type film biological reactor: (1) higher sludge concentration is bigger to the membrane flux influence of membrane bioreactor, has caused the processing waste water ability of membrane bioreactor to reduce; (2) higher sludge concentration is easily made film forming pollution, in order to reduce the pollution of film, needs higher aeration rate, and therefore the aeration power consumption of the unit's of processing water yield is higher; (3) membrane module is positioned at the inside of bio-reactor, not easy cleaning and maintenance.
Summary of the invention
The objective of the invention is to overcome the defective that above-mentioned integral type film biological reactor exists, provide a kind of easy and simple to handle and energy consumption is low, utilize the double-area gravity-elution membrane bioreactor sewage treatment equipment of the gravity head water outlet on membrane module top.
Equipment of the present invention is made up of upflow-type reactor and the container that is installed on the upflow-type reactor.
Described upflow-type reactor is a biochemical reaction zone, and a pipe core is installed in upflow-type reactor, between pipe core and the reactor wall space is arranged, and has water-in in the upper portion side wall of reactor.Water in the pipe core is upward flow, and to stream, mixed solution circulates inside and outside pipe core the water outside the pipe for down.
Described container is a solid-liquid displacement zone, and membrane module is installed in container, and the bottom of membrane module is laid with aeration tube; Upper portion side wall at container has inlet mouth and water outlet, and the bottom has the mixed solution admission port, and the bottom of upflow-type reactor communicates with container; Pass the sidewall of upflow-type reactor, the communicating pipe that container is communicated with the pipe core of upflow-type reactor is installed.Solid-liquid displacement zone is on the outer side wall of biochemical reaction zone bottom.
The bottom of membrane module is laid with aeration tube, and in order to wash away the film surface, the film water outlet drives continuous effluent by the gravity head of membrane module top, saves the control unit of water outlet suction pump with the water outlet at intermittence of conventional film bio-reactor.The isolating solid of tunicle under the carrying of gas by entering the pipe core of bio-reaction zone communicating pipe.
Described communicating pipe is installed in the top of container.
Between the outer wall of described membrane module and upflow-type reactor dividing plate is arranged.
Described inlet mouth is below water outlet.
Solid-liquid displacement zone of the present invention is in a container, solid-liquid separation can occur in the space below the membrane module in container, make with mixed solution that film contacts in sludge concentration reduce, alleviate the influence of sludge concentration to membrane flux.Solid-liquid displacement zone can have following two kinds of structure formations: structure one, no iris type solid-liquid displacement zone; Structure two has the iris type solid-liquid displacement zone.
The working method of double-area gravity-elution membrane bioreactor of the present invention is: city domestic sewage or trade effluent at first enter the biochemical reaction zone top that microbial population (active sludge) is housed by water-in, under the disturbance of gas with the microbial population thorough mixing; Then, mixed solution flows downward in the pipe core outside, when arriving reactor bottom, under the castering action of gas, enters pipe core, and upwards flows: at biochemical reaction zone, pollutent can be decomposed and remove.
Partially mixed liquid enters from the mixed solution admission port of solid-liquid displacement zone bottom and carries out the solid-liquid initial gross separation the solid-liquid displacement zone, reducing the solids concn of the liquid that contacts with film, thereby reduces resistance, the work period of prolongation film.
Aeration tube is laid in the bottom of membrane module, and air constantly washes away and the vibration membrane surface, and mud can not be adhered on it.
With the liquid of water inlet equivalent under the gravity head above the membrane module drives, through the membrane filtration continuous effluent, separated mud then under the rolling action of gas, by entering the pipe core of biochemical reaction zone communicating pipe, so moves in circles, waste water is purified.
Equipment of the present invention has following advantage:
1. system saves the traditional water outlet suction pump and the control unit of water outlet intermittently, and compact construction, structure is succinct, floor space is little, operation with safeguard simply, manual request is few, easily is automated control.
2. membrane module is positioned at solid-liquid displacement zone, reduces the sludge concentration of membrane separation zone and the pollution of film, improves the processing power of film.
3. solid-liquid displacement zone is communicated with the pipe core of biochemical reaction zone, realizes washing away the efficient utilization of membrane module tolerance, has improved the utilization ratio of oxygen, the required aeration rate of the normal operation of reduction system, thereby the operation energy consumption of reduction system.
4. membrane module is installed in the side of solid-liquid displacement zone, is easy to install, dismantle, and helps the maintenance and the cleaning of film.
Description of drawings
Fig. 1. the synoptic diagram of present device;
Fig. 2. the present invention is not with the solid-liquid displacement zone synoptic diagram of dividing plate;
Fig. 3. the solid-liquid displacement zone synoptic diagram of band dividing plate of the present invention;
Fig. 4. existing separate type membrane bioreactor synoptic diagram;
Fig. 5. existing integral type film biological reactor.
Reference numeral
1 water-in, 2 biochemical reaction zones, 3 pipe cores, 4 inlet mouths, 5 water outlets
6 membrane modules, 7 communicating pipe 8 mixed solution admission port
9 solid-liquid displacement zone, 10 dividing plates, 11 pumps
12 returned sluges, 13 containers, 14 upflow-type reactors
Embodiment
Embodiment 1:
One two-region gravity-elution membrane bioreactor sewage treatment equipment is made up of upflow-type reactor 14 and container 13.
Described upflow-type reactor is a biochemical reaction zone 2, and a pipe core 3 is installed in upflow-type reactor, has water-in 1 in the upper portion side wall of reactor.
Described container is a solid-liquid displacement zone 9, and membrane module 6 is installed in container 13, and the bottom of membrane module 6 is laid with aeration tube, and dividing plate 10 is arranged between the outer wall of membrane module and upflow-type reactor; Upper portion side wall at container has inlet mouth 4, on the top of inlet mouth water outlet 5 is arranged, and has mixed solution admission port 8 in the bottom of container, and the bottom of upflow-type reactor communicates with container; At the top of container, pass the sidewall of upflow-type reactor, the communicating pipe 7 that container is communicated with the pipe core of upflow-type reactor is installed, the top of solid-liquid displacement zone is communicated with pipe core in the bio-reaction zone.
To contain COD is 160-250mg/l, and SS is 40-100mg/l, and colourity 50-120 dyeing waste water doubly enters double-area gravity-elution membrane bioreactor by water-in, spoil disposal not in the whole service process, sludge concentration is 500-3000mg/l, and water temperature is 10-30 ℃, and pH is 6-9.
Wash away membrane module tolerance and enter pipe core, mud mixed liquid is mixed in biochemical reaction zone fully, and the mixed solution of whole bio-reactor all has been oxygen condition, and organism is degraded fully.Partially mixed liquid enters solid-liquid displacement zone from the inlet of solid-liquid displacement zone, and mixed solution obtains precipitate and separate preferably in the solid-liquid district, and precipitating sludge is back to the pipe core of biochemical reaction zone under the rolling action of gas.
COD is 18-48mg/l in the water outlet, and SS is not for detecting, and colourity is lower than 30 times, reaches national miscellaneous domestic water quality standard.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011205865A CN1153738C (en) | 2001-07-24 | 2001-07-24 | Sewage treating plant with double-area gravity-elution membrane bioreactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011205865A CN1153738C (en) | 2001-07-24 | 2001-07-24 | Sewage treating plant with double-area gravity-elution membrane bioreactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1398796A CN1398796A (en) | 2003-02-26 |
| CN1153738C true CN1153738C (en) | 2004-06-16 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB011205865A Expired - Fee Related CN1153738C (en) | 2001-07-24 | 2001-07-24 | Sewage treating plant with double-area gravity-elution membrane bioreactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1153738C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11851300B2 (en) | 2018-08-20 | 2023-12-26 | Kornit Digital Ltd. | Loading mechanism for shirts |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100337938C (en) * | 2003-06-25 | 2007-09-19 | 中国科学院沈阳应用生态研究所 | Bioreactor for water treatment |
| CN1317207C (en) * | 2003-10-21 | 2007-05-23 | 中国科学院生态环境研究中心 | Baffled aeration pressurized gravity outflow membrane bioreactor sewage treatment equipment |
| CN100429160C (en) * | 2005-11-28 | 2008-10-29 | 中国科学院生态环境研究中心 | Circular flow membrane bioreactor wastewater treatment equipment and wastewater treatment method |
| CN102642922A (en) * | 2012-04-27 | 2012-08-22 | 浙江大学 | External anaerobic membrane bioreactor |
| CN107129034A (en) * | 2017-03-07 | 2017-09-05 | 广东工业大学 | A kind of membrane bioreactor system from culture granule sludge |
| CN107311309B (en) * | 2017-08-02 | 2023-06-06 | 哈尔滨工业大学 | Upflow internal circulation microaerobic bioreactor and its aeration method and application method for enhancing mass transfer |
-
2001
- 2001-07-24 CN CNB011205865A patent/CN1153738C/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11851300B2 (en) | 2018-08-20 | 2023-12-26 | Kornit Digital Ltd. | Loading mechanism for shirts |
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| Publication number | Publication date |
|---|---|
| CN1398796A (en) | 2003-02-26 |
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