CN207645904U - Sludge zero discharge MBR sewage-treatment plants - Google Patents
Sludge zero discharge MBR sewage-treatment plants Download PDFInfo
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- CN207645904U CN207645904U CN201721625916.1U CN201721625916U CN207645904U CN 207645904 U CN207645904 U CN 207645904U CN 201721625916 U CN201721625916 U CN 201721625916U CN 207645904 U CN207645904 U CN 207645904U
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- 239000010802 sludge Substances 0.000 title claims abstract description 80
- 239000010865 sewage Substances 0.000 title claims abstract description 38
- 239000012528 membrane Substances 0.000 claims abstract description 56
- 230000029087 digestion Effects 0.000 claims abstract description 19
- 238000010992 reflux Methods 0.000 claims abstract description 16
- 239000006228 supernatant Substances 0.000 claims abstract description 13
- 238000005273 aeration Methods 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 239000007788 liquid Substances 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 238000004140 cleaning Methods 0.000 claims description 8
- 230000000712 assembly Effects 0.000 claims description 6
- 238000000429 assembly Methods 0.000 claims description 6
- 230000001276 controlling effect Effects 0.000 claims description 4
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 6
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 10
- 238000000034 method Methods 0.000 description 10
- 229910052698 phosphorus Inorganic materials 0.000 description 10
- 239000011574 phosphorus Substances 0.000 description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 4
- 229910002651 NO3 Inorganic materials 0.000 description 4
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- WHBMMWSBFZVSSR-UHFFFAOYSA-N 3-hydroxybutyric acid Chemical compound CC(O)CC(O)=O WHBMMWSBFZVSSR-UHFFFAOYSA-N 0.000 description 1
- JVMRPSJZNHXORP-UHFFFAOYSA-N ON=O.ON=O.ON=O.N Chemical compound ON=O.ON=O.ON=O.N JVMRPSJZNHXORP-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000001079 digestive effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 230000004807 localization Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001546 nitrifying effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 125000001477 organic nitrogen group Chemical group 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Activated Sludge Processes (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本实用新型公开一种污泥零排放MBR污水处理装置,它包括依次连接的污泥消化池、缺氧池、MBR膜池和设备间;污泥消化池远离缺氧池一侧外壁上自上而下并联安装有多个剩余污泥上清液排放管,缺氧池远离MBR池一侧外壁底部设置有污水进水管;污泥消化池和缺氧池内均设有搅拌器;缺氧池与MBR膜池之间通过缺氧溢流管连通;MBR膜池内设置有MBR膜装置,MBR膜装置上方设置有气提回流装置,气提回流装置顶部设置有回流管,回流管伸入缺氧池底部,靠近设备间一侧的MBR膜装置外壁底部上设置有余污泥排放管,污泥排放管另一端设置在污泥消化池一侧外壁底部。该装置具有污水处理效果好、节能降耗、实现污泥零排放的优点。
The utility model discloses a sludge zero-discharge MBR sewage treatment device, which comprises a sludge digestion tank, an anoxic tank, an MBR membrane tank and an equipment room connected in sequence; A plurality of excess sludge supernatant discharge pipes are installed in the lower parallel connection, and a sewage inlet pipe is provided at the bottom of the outer wall of the anoxic pool away from the MBR pool; agitators are installed in the sludge digestion tank and the anoxic pool; the anoxic pool and the anoxic pool The MBR membrane tanks are connected through anoxic overflow pipes; MBR membrane devices are installed in the MBR membrane tanks, and an air lift and reflux device is installed above the MBR membrane devices. , the bottom of the outer wall of the MBR membrane device near the equipment room is provided with an excess sludge discharge pipe, and the other end of the sludge discharge pipe is arranged at the bottom of the outer wall of the sludge digestion tank. The device has the advantages of good sewage treatment effect, energy saving and consumption reduction, and zero discharge of sludge.
Description
技术领域technical field
本实用新型涉及污水处理设备技术领域,具体涉及一种污泥零排放MBR污水处理装置。The utility model relates to the technical field of sewage treatment equipment, in particular to an MBR sewage treatment device with zero sludge discharge.
背景技术Background technique
膜生物反应器(Membrane Bio-reactor,MBR)技术是先进的水处理技术,其出水品质高,技术成熟,且随着关键产品-膜产品的国产化率越来越高和市场应用越来越普及,MBR膜的投资成本和运行成本逐渐下降。MBR膜生物反应器是膜和活性污泥相结合的工艺。微生物将膜截留下来的污染物进行深一步的降解。MBR通过定期排泥,从而使系统内部污泥浓度维持平衡。目前,MBR技术广泛用于城镇污水处理领域,其出水可以达到《城镇污水处理厂污染物排放标准》GB18918-2002中的一级A标准以上,达到回用水标准或地表水Ⅳ类标准,被广泛应用于排水标准高的项目或提标改造项目。Membrane Bioreactor (Membrane Bio-reactor, MBR) technology is an advanced water treatment technology with high effluent quality and mature technology. With the increasing localization rate and market application of key products - membrane products With popularization, the investment cost and operating cost of MBR membranes have gradually decreased. MBR membrane bioreactor is a process combining membrane and activated sludge. Microorganisms further degrade the pollutants retained by the membrane. MBR regularly discharges sludge to maintain the balance of sludge concentration inside the system. At present, MBR technology is widely used in the field of urban sewage treatment, and its effluent can reach the first-class A standard in the "Pollutant Discharge Standards for Urban Wastewater Treatment Plants" GB18918-2002, and meet the reuse water standard or surface water Class IV standard. It is widely used Applied to projects with high drainage standards or upgrading projects.
但是,现有一体化MBR污水处理系统还存在以下缺陷:However, the existing integrated MBR sewage treatment system also has the following defects:
1.脱氮除磷效果不好。现有一体化MBR污水处理设备,大多以 AO+MBR工艺(缺氧、好氧+MBR工艺)或AAO+MBR工艺(厌氧、缺氧、好氧+MBR工艺),AO+MBR工艺不能同时实现脱氮除磷效果; AAO+MBR工艺因为工艺紧凑,一方面回流到缺氧区的混合液常导致缺氧区溶解氧浓度过高,影响脱氮效果,另一方面,回流到厌氧区的混合液因含有硝酸盐影响除磷效果;1. The effect of nitrogen and phosphorus removal is not good. Most of the existing integrated MBR sewage treatment equipment uses the AO+MBR process (anoxic, aerobic + MBR process) or AAO+MBR process (anaerobic, anoxic, aerobic + MBR process), and the AO+MBR process cannot be simultaneously Realize the effect of nitrogen and phosphorus removal; AAO+MBR process is compact because of the compact process. On the one hand, the mixed liquid flowing back to the anoxic zone often causes the dissolved oxygen concentration in the anoxic zone to be too high, which affects the denitrification effect. On the other hand, it flows back to the anoxic zone. The mixed solution contains nitrate, which affects the phosphorus removal effect;
2.运行电耗较高。因设备选型不合理,设备较多等,导致运行电耗高居不下;2. High power consumption during operation. Due to the unreasonable selection of equipment and the large number of equipment, etc., the running power consumption remains high;
3.设备不够紧凑,占地面积较大。3. The equipment is not compact enough and occupies a large area.
4.剩余污泥无法及时处理。一体化MBR污水处理系统通过排出剩余污泥达到去除污水中磷的目的。但一般情况下一体化MBR污水处理系统处理规模较小,实行无人值守,产生的污泥一般无法及时处理,导致系统运行效果不好。4. The remaining sludge cannot be disposed of in time. The integrated MBR sewage treatment system achieves the purpose of removing phosphorus in sewage by discharging excess sludge. However, in general, the integrated MBR sewage treatment system has a small scale of treatment and is unattended, and the generated sludge cannot be treated in time, resulting in poor system operation.
发明内容Contents of the invention
本实用新型的目的在于克服现有技术的不足,提供了一种污泥零排放MBR污水处理装置。该装置具有污水处理效果好、节能降耗、实现污泥零排放的优点。The purpose of the utility model is to overcome the deficiencies of the prior art and provide a sludge zero discharge MBR sewage treatment device. The device has the advantages of good sewage treatment effect, energy saving and consumption reduction, and zero discharge of sludge.
为实现上述目的,本实用新型所设计一种污泥零排放MBR污水处理装置,它包括依次连接的污泥消化池、缺氧池、MBR膜池和设备间;所述污泥消化池远离缺氧池一侧外壁上自上而下并联安装有多个剩余污泥上清液排放管,所述污泥消化池底面上设置有消化池曝气头组件,所述消化池曝气头组件通过管线与设备间内的鼓风机相连,所述缺氧池远离MBR膜池一侧外壁底部设置有污水进水管;所述污泥消化池和缺氧池内均设有搅拌器;所述缺氧池与MBR膜池之间通过缺氧溢流管连通;所述MBR膜池底面上设置有多组曝气头组件,所述曝气头组件均通过管线与设备间内的鼓风机相连,In order to achieve the above-mentioned purpose, the utility model designs a kind of sludge zero-discharge MBR sewage treatment device, and it comprises the sludge digestion pond, anoxic pond, MBR film pond and equipment room that are connected successively; A plurality of residual sludge supernatant discharge pipes are installed in parallel on one side of the oxygen tank from top to bottom, and a digester aeration head assembly is arranged on the bottom surface of the sludge digestion tank, and the digestion tank aeration head assembly passes through The pipeline is connected with the blower in the equipment room, and the bottom of the outer wall of the anoxic pool is far away from the MBR membrane pool. The MBR membrane pools are connected through the anoxic overflow pipe; the bottom surface of the MBR membrane pool is provided with multiple sets of aeration head assemblies, and the aeration head assemblies are connected to the blower in the equipment room through pipelines.
所述MBR膜池内设置有MBR膜装置,所述MBR膜装置上方设置有气提回流装置,所述气提回流装置顶部设置有回流管,所述回流管伸入缺氧池底部,靠近设备间一侧在MBR膜装置的侧壁上设置有产水管;靠近设备间一侧的MBR膜装置外壁底部上设置有污泥排放管,污泥排放管另一端设置在污泥消化池一侧外壁底部。An MBR membrane device is arranged in the MBR membrane pool, an air lift reflux device is arranged above the MBR membrane device, and a reflux pipe is arranged on the top of the air lift reflux device, and the reflux pipe extends into the bottom of the anoxic pool, close to the equipment room One side is provided with a water production pipe on the side wall of the MBR membrane device; a sludge discharge pipe is provided on the bottom of the outer wall of the MBR membrane device near the equipment room, and the other end of the sludge discharge pipe is provided at the bottom of the outer wall of the sludge digestion tank .
进一步地,所述MBR膜装置包括MBR膜组件,所述MBR膜组件四周设置有导流板,所述产水管穿过导流板与MBR膜组件连通,靠近所述缺氧池一侧的导流板顶部设置有向下倾斜的倾斜导流板。Further, the MBR membrane device includes an MBR membrane module, and a deflector is arranged around the MBR membrane module. The top of the flow plate is provided with an inclined flow guide plate inclined downward.
再进一步地,所述倾斜导流板倾斜角度为1~15°。Still further, the inclination angle of the inclined deflector is 1-15°.
再进一步地,所述消化池曝气头组件和曝气头组件与鼓风机连接的管线上均对应设置有控制消化池曝气头组件和曝气头组件的电磁阀。Still further, the aeration head assembly of the digestion tank and the pipeline connecting the aeration head assembly and the blower are correspondingly provided with electromagnetic valves for controlling the aeration head assembly and the aeration head assembly of the digestion tank.
再进一步地,所述回流管上还设置有流量调节阀。Still further, the return pipe is also provided with a flow regulating valve.
再进一步地,所述设备间内还设置有清洗组件,所述清洗组件包括并联设置有清水箱和加药箱和控制电磁阀,所述清水箱和加药箱均与产水管连接。Still further, a cleaning assembly is provided in the equipment room, and the cleaning assembly includes a clean water tank, a medicine adding box and a control solenoid valve arranged in parallel, and the clean water tank and the medicine adding box are both connected to the water production pipe.
再进一步地,所述污泥排放管上设有污泥泵。Still further, a sludge pump is provided on the sludge discharge pipe.
再进一步地,所述剩余污泥上清液排放管上均设置有清液球阀,所述剩余污泥上清液排放管另一端均连接有供水管。Still further, the excess sludge supernatant discharge pipes are provided with clear liquid ball valves, and the other ends of the excess sludge supernatant liquid discharge pipes are connected to water supply pipes.
本实用新型的有益效果:The beneficial effects of the utility model:
1)本实用新型污水和回流混合液一起进入缺氧区经充分混合后;污泥中的硝酸盐,在反硝化菌的作用下进行反硝化反应,将硝酸盐转化为氮气,实现脱氮。1) The sewage and the reflux mixture of the utility model enter the anoxic zone together and are fully mixed; the nitrate in the sludge undergoes denitrification reaction under the action of denitrifying bacteria, and the nitrate is converted into nitrogen to realize denitrification.
2)本实用新型中剩余污泥上清液富含磷,收集用于绿化,实现生磷资源的循环利用。2) In the utility model, the remaining sludge supernatant is rich in phosphorus, which is collected for greening and realizes the recycling of phosphorus resources.
3)本实用新型中剩余污泥进入污泥消化池,在消化池中进行厌氧和好氧消化,实现了污泥零排放。3) In the utility model, the remaining sludge enters the sludge digester, where anaerobic and aerobic digestion are performed, and zero discharge of sludge is realized.
4)本实用新型利用膜曝气产生的水头进行内回流,省去了回流泵,节省能量。4) The utility model utilizes the water head generated by membrane aeration to carry out internal backflow, which saves energy by eliminating the backflow pump.
附图说明Description of drawings
图1为本实用新型污泥零排放MBR污水处理装置的俯视图;Fig. 1 is the top view of the utility model sludge zero discharge MBR sewage treatment device;
图2为本实用新型污泥零排放MBR污水处理装置的主视图;Fig. 2 is the front view of the utility model sludge zero discharge MBR sewage treatment device;
图中,污泥消化池1、污泥上清液排放管1.1、曝气头组件1.2、缺氧池2、缺氧溢流管2.1、MBR膜池3、曝气头组件3.1、设备间4、鼓风机4.1、污水进水管5、搅拌器6、MBR膜装置7、产水管7.1、 MBR膜组件7.2、导流板7.3、倾斜导流板7.4、气提回流装置8、回流管8.1、回流调节阀8.2、污泥回流管9、污泥回流泵9.1、电磁阀10、清洗组件11、清水箱11.1、加药箱11.2、清洗控制电磁阀11.3、清液球阀12。In the figure, sludge digestion tank 1, sludge supernatant discharge pipe 1.1, aeration head assembly 1.2, anoxic tank 2, anoxic overflow pipe 2.1, MBR membrane pool 3, aeration head assembly 3.1, equipment room 4 , blower 4.1, sewage inlet pipe 5, agitator 6, MBR membrane device 7, water production pipe 7.1, MBR membrane module 7.2, deflector 7.3, inclined deflector 7.4, air lift return device 8, return pipe 8.1, return adjustment Valve 8.2, sludge return pipe 9, sludge return pump 9.1, solenoid valve 10, cleaning assembly 11, clean water tank 11.1, dosing box 11.2, cleaning control solenoid valve 11.3, clear liquid ball valve 12.
具体实施方式Detailed ways
下面结合附图和具体实施例对本实用新型作进一步的详细描述,以便本领域技术人员理解。The utility model will be further described in detail below in conjunction with the accompanying drawings and specific embodiments, so that those skilled in the art can understand.
如图1~2所示的污泥零排放MBR污水处理装置,它包括依次连接的污泥消化池1、缺氧池2、MBR膜池3和设备间4;污泥消化池 1远离缺氧池2一侧外壁上自上而下并联安装有7个剩余污泥上清液排放管1.1,每个剩余污泥上清液排放管1.1上均设置有清液球阀12;The sludge zero-discharge MBR sewage treatment device shown in Figures 1-2 includes sludge digestion tank 1, anoxic tank 2, MBR membrane tank 3 and equipment room 4 connected in sequence; sludge digestion tank 1 is far away from anoxic On the outer wall of one side of the pool 2, there are seven excess sludge supernatant discharge pipes 1.1 installed in parallel from top to bottom, and each excess sludge supernatant liquid discharge pipe 1.1 is equipped with a clear liquid ball valve 12;
污泥消化池1底面上设置有消化池曝气头组件1.2,消化池曝气头组件1.2通过管线与设备间4内的鼓风机4.1相连,消化池曝气头组件1.2与鼓风机4.1连接的管线上均对应设置有控制消化池曝气头组件1.2的电磁阀10。The bottom surface of the sludge digester 1 is provided with a digester aeration head assembly 1.2, which is connected to the blower 4.1 in the equipment room 4 through pipelines, and the pipeline connecting the digester aeration head assembly 1.2 and the blower 4.1 All are correspondingly provided with a solenoid valve 10 for controlling the aeration head assembly 1.2 of the digestion tank.
缺氧池2远离MBR膜池3一侧外壁底部设置有污水进水管5;污泥消化池1和缺氧池2内均设有搅拌器6;缺氧池2与MBR膜池 3之间通过缺氧溢流管2.1连通;MBR膜池3底面上设置有2组曝气头组件3.1,2组曝气头组件3.1均通过管线与设备间4内的鼓风机 4.1相连,每组曝气头组件3.1与鼓风机4.1连接的管线上均对应设置有曝气头组件3.1的电磁阀10。The bottom of the outer wall of the anoxic pool 2 away from the MBR membrane pool 3 is provided with a sewage inlet pipe 5; the sludge digester 1 and the anoxic pool 2 are equipped with agitators 6; the anoxic pool 2 and the MBR membrane pool 3 pass through The anoxic overflow pipe 2.1 is connected; two sets of aeration head assemblies 3.1 are arranged on the bottom surface of the MBR membrane pool 3, and the two sets of aeration head assemblies 3.1 are connected to the blower 4.1 in the equipment room 4 through pipelines, and each set of aeration head assemblies 3.1 The electromagnetic valve 10 of the aeration head assembly 3.1 is correspondingly arranged on the pipeline connected with the blower 4.1.
MBR膜池3内设置有MBR膜装置7,MBR膜装置7包括MBR 膜组件7.2,MBR膜组件7.2四周设置有导流板7.3,产水管7.1穿过导流板7.3与MBR膜组件7.2连通,靠近缺氧池2一侧的导流板7.3 顶部设置有向下倾斜角度为1~15°的倾斜导流板7.4。MBR membrane tank 3 is provided with MBR membrane device 7, MBR membrane device 7 includes MBR membrane module 7.2, MBR membrane module 7.2 is surrounded by deflector 7.3, and water production pipe 7.1 passes through deflector 7.3 to communicate with MBR membrane module 7.2, The top of the deflector 7.3 near the side of the anoxic pool 2 is provided with an inclined deflector 7.4 with a downward slope angle of 1-15°.
MBR膜装置7上方设置有气提回流装置8,气提回流装置8顶部设置有回流管8.1,回流管8.1上还设置有流量调节阀8.2;An air lift reflux device 8 is arranged above the MBR membrane device 7, a reflux pipe 8.1 is arranged on the top of the air lift reflux device 8, and a flow regulating valve 8.2 is also arranged on the reflux pipe 8.1;
回流管8.1伸入缺氧池2底部,靠近设备间4一侧在MBR膜装置7的侧壁上设置有产水管7.1;靠近设备间4一侧的MBR膜装置7 外壁底部上设置有污泥排放管9,污泥排放管9另一端设置在污泥消化池1一侧外壁底部。污泥排放管9上设有污泥泵9.1The return pipe 8.1 extends into the bottom of the anoxic pool 2, and the side wall of the MBR membrane device 7 near the equipment room 4 is provided with a water production pipe 7.1; the bottom of the outer wall of the MBR membrane device 7 near the equipment room 4 is provided with sludge The discharge pipe 9 and the other end of the sludge discharge pipe 9 are arranged at the bottom of the outer wall of one side of the sludge digestion tank 1 . Sludge discharge pipe 9 is provided with sludge pump 9.1
设备间4内还设置有清洗组件11,清洗组件11包括并联设置有清水箱11.1和加药箱11.2和控制电磁阀11.3,清水箱11.1和加药箱 11.2均与产水管7.1连接。A cleaning assembly 11 is also provided in the equipment room 4, and the cleaning assembly 11 includes a clean water tank 11.1, a dosing box 11.2 and a control solenoid valve 11.3 arranged in parallel, and the clean water tank 11.1 and the dosing box 11.2 are connected to the water production pipe 7.1.
上述污泥零排放MBR污水处理装置工作过程:The working process of the above sludge zero discharge MBR sewage treatment plant:
1)污水通过污水进水管5进入缺氧池1,与来自MBR膜池3消化液混合,反硝化细菌在缺氧池1中利用污水中的碳源进行反硝化反应实现脱氮;同时聚磷微生物在缺氧池2中将污水中优质的碳源转化为聚β-羟基丁酸等储能物质,释放体内储存的磷;然后混合液通过缺氧溢流管2.1进入MBR膜池3,在曝气的条件下,聚磷菌吸收污水中的磷,储存在体内,硝化菌将污水中的有机氮转化为硝酸盐和亚硝酸盐氮,剩余的有机物被微生物进一步降解;剩余的污泥通过污泥管9排入污泥消化池1,静置澄清后通过污泥上清液排放管1.1排出富含磷元素上清液,通过控制电磁阀10来实现对污泥消化池1中的剩余污泥实现好氧和厌氧消化,消化掉剩余污泥。1) Sewage enters the anoxic pool 1 through the sewage inlet pipe 5, and mixes with the digestive liquid from the MBR membrane pool 3, and the denitrifying bacteria use the carbon source in the sewage to perform denitrification in the anoxic pool 1 to achieve denitrification; In the anoxic pool 2, the microbes convert the high-quality carbon source in the sewage into energy storage substances such as poly-β-hydroxybutyric acid, and release the phosphorus stored in the body; then the mixed solution enters the MBR membrane pool 3 through the anoxic overflow pipe 2.1, and in the Under the condition of aeration, the phosphorus accumulating bacteria absorb the phosphorus in the sewage and store it in the body, the nitrifying bacteria convert the organic nitrogen in the sewage into nitrate and nitrite nitrogen, and the remaining organic matter is further degraded by microorganisms; the remaining sludge is passed through The sludge pipe 9 is discharged into the sludge digester 1, and after standing for clarification, the phosphorus-rich supernatant is discharged through the sludge supernatant discharge pipe 1.1, and the residual liquid in the sludge digester 1 is realized by controlling the solenoid valve 10. The sludge realizes aerobic and anaerobic digestion, and digests the remaining sludge.
2)净化后的污水随着产水管7.1流出,回流混合液通过气提回流装置8和回流管8.1回流至缺氧池2;2) The purified sewage flows out with the water production pipe 7.1, and the reflux mixed liquid flows back to the anoxic pool 2 through the air lift reflux device 8 and the reflux pipe 8.1;
3)工作完毕后,清水箱11.1和加药箱11.2的液体通过产水管 7.1回流清洗MBR膜装置7。3) After the work is completed, the liquid in the clean water tank 11.1 and the dosing tank 11.2 passes through the water production pipe 7.1 to return to clean the MBR membrane device 7.
其它未详细说明的部分均为现有技术。尽管上述实施例对本实用新型做出了详尽的描述,但它仅仅是本实用新型一部分实施例,而不是全部实施例,人们还可以根据本实施例在不经创造性前提下获得其他实施例,这些实施例都属于本实用新型保护范围。Other parts not specified in detail are prior art. Although the foregoing embodiments have described the utility model in detail, it is only a part of the embodiments of the utility model, rather than all embodiments, and people can also obtain other embodiments according to the present embodiment without inventive step, these The embodiments all belong to the protection scope of the present utility model.
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