CN115477439A - Integrated MBR sewage treatment equipment - Google Patents
Integrated MBR sewage treatment equipment Download PDFInfo
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- 239000010865 sewage Substances 0.000 title claims abstract description 93
- 239000012528 membrane Substances 0.000 claims abstract description 120
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 117
- 239000010802 sludge Substances 0.000 claims abstract description 40
- 230000001105 regulatory effect Effects 0.000 claims abstract description 36
- 238000005273 aeration Methods 0.000 claims description 61
- 238000004140 cleaning Methods 0.000 claims description 44
- 238000004519 manufacturing process Methods 0.000 claims description 16
- 239000000126 substance Substances 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 8
- 238000010992 reflux Methods 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 238000005070 sampling Methods 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 3
- 230000001546 nitrifying effect Effects 0.000 claims description 3
- 238000011045 prefiltration Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 10
- 239000002245 particle Substances 0.000 abstract description 3
- 239000007787 solid Substances 0.000 abstract description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 9
- 229910052698 phosphorus Inorganic materials 0.000 description 9
- 239000011574 phosphorus Substances 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
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- 229910052757 nitrogen Inorganic materials 0.000 description 3
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- 238000005261 decarburization Methods 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 229920000388 Polyphosphate Polymers 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005262 decarbonization Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
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- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000004009 herbicide Substances 0.000 description 1
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- 239000002440 industrial waste Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
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- 239000000575 pesticide Substances 0.000 description 1
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- 239000001205 polyphosphate Substances 0.000 description 1
- 235000011176 polyphosphates Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000004162 soil erosion Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/302—Nitrification and denitrification treatment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/308—Biological phosphorus removal
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/105—Phosphorus compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
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Abstract
本发明涉及污水处理技术领域,公开了集成式一体化MBR污水处理设备,包括集成式箱体,所述集成式箱体内设有格栅井、调节池区、污泥池区、清水池区、缺氧区、厌氧区、好氧区、膜池区以及设备区,所述格栅井与调节池区相连通,所述调节池区内设有潜水泵,所述潜水泵的输出端连接有调节池出水管,所述调节池出水管上连接有回流管,由格栅井对进入的污水进行初步过滤,去除生活污水中的软性缠绕物、较大固颗粒杂物及飘浮物,调节潜水搅拌器用于对不同时间或不同来源的污水进行混合,使流出的水质比较均匀,以避免后续处理设施承受过大的冲击负荷,并对污水进行均和调节处理,使其水量和水质都比较稳定,以便于进行后续工序的处理。
The invention relates to the technical field of sewage treatment, and discloses integrated integrated MBR sewage treatment equipment, including an integrated box body, and the integrated box body is provided with a grid well, a regulating pool area, a sludge pool area, and a clear water pool area , anoxic area, anaerobic area, aerobic area, membrane pool area and equipment area, the grid well is connected with the adjustment pool area, a submersible pump is arranged in the adjustment pool area, and the output end of the submersible pump It is connected with the outlet pipe of the regulating pool, and the outlet pipe of the regulating pool is connected with a return pipe, and the incoming sewage is preliminarily filtered by the grid well to remove soft entanglements, large solid particles and floating objects in the domestic sewage , Adjusting the submersible mixer is used to mix sewage at different times or from different sources, so that the quality of the outflowing water is relatively uniform, so as to avoid excessive impact loads on the subsequent treatment facilities, and perform equalization and adjustment treatment on the sewage to ensure that the water quantity and quality All relatively stable, in order to carry out the processing of follow-up procedure.
Description
技术领域technical field
本发明涉及污水处理技术领域,具体为集成式一体化MBR污水处理设备。The invention relates to the technical field of sewage treatment, in particular to integrated integrated MBR sewage treatment equipment.
背景技术Background technique
污水处理:为使污水达到排入某一水体或再次使用的水质要求对其进行净化的过程,污水处理被广泛应用于建筑、农业、交通、能源、石化、环保、城市景观、医疗、餐饮等各个领域。Sewage treatment: the process of purifying sewage to meet the water quality requirements of being discharged into a certain water body or reused. Sewage treatment is widely used in construction, agriculture, transportation, energy, petrochemical, environmental protection, urban landscape, medical treatment, catering, etc. each field.
按污水来源分类,污水处理一般分为生产污水处理和生活污水处理。生产污水包括工业污水、农业污水以及医疗污水等,而生活污水就是日常生活产生的污水,是指各种形式的无机物和有机物的复杂混合物,包括:漂浮和悬浮的大小固体颗粒;胶状和凝胶状扩散物;纯溶液,按水污的质性来分,水的污染有两类:一类是自然污染;另一类是人为污染,当前对水体危害较大的是人为污染,水污染可根据污染杂质的不同而主要分为化学性污染、物理性污染和生物性污染三大类,污染物主要有:未经处理而排放的工业废水;未经处理而排放的生活污水;大量使用化肥、农药、除草剂的农田污水;堆放在河边的工业废弃物和生活垃圾;水土流失;矿山污水,处理污水的方法很多,一般可归纳为物理法、化学法和生物法等。According to the classification of sewage sources, sewage treatment is generally divided into production sewage treatment and domestic sewage treatment. Production sewage includes industrial sewage, agricultural sewage and medical sewage, etc., while domestic sewage is sewage produced in daily life, which refers to a complex mixture of various forms of inorganic and organic substances, including: floating and suspended solid particles of large and small sizes; colloidal and Gel-like diffuser; pure solution, according to the nature of water pollution, there are two types of water pollution: one is natural pollution; the other is man-made pollution. At present, man-made pollution is the most harmful to water bodies. Pollution can be divided into chemical pollution, physical pollution and biological pollution according to different impurities. Pollutants mainly include: industrial wastewater discharged without treatment; domestic sewage discharged without treatment; Farmland sewage using chemical fertilizers, pesticides, and herbicides; industrial waste and domestic garbage piled up by the river; soil erosion; mine sewage. There are many methods of sewage treatment, which can generally be summarized as physical methods, chemical methods, and biological methods.
目前,市面上的污水处理设备占地较大,对污水的处理工序繁琐,投入成本较高,并且现有的污水处理设备对污水中的氮磷污染物去除的效果不佳,直接影响到对污水的处理,对此我们提出集成式一体化MBR污水处理设备。At present, the sewage treatment equipment on the market occupies a large area, the sewage treatment process is cumbersome, and the input cost is high, and the existing sewage treatment equipment is not effective in removing nitrogen and phosphorus pollutants in sewage, which directly affects the For the treatment of sewage, we propose an integrated integrated MBR sewage treatment equipment.
发明内容Contents of the invention
本发明目的是提供集成式一体化MBR污水处理设备,以解决现有技术中污水处理设备占地较大,对污水的处理工序繁琐,投入成本较高,并且现有的污水处理设备对污水中的氮磷污染物去除的效果不佳,直接影响到对污水的处理的问题。The purpose of the present invention is to provide an integrated integrated MBR sewage treatment equipment to solve the problem that the sewage treatment equipment occupies a large area in the prior art, the sewage treatment process is cumbersome, the input cost is high, and the existing sewage treatment equipment has a large impact on the sewage. The removal effect of nitrogen and phosphorus pollutants is not good, which directly affects the problem of sewage treatment.
为实现上述目的,本发明提供如下技术方案:集成式一体化MBR污水处理设备,包括集成式箱体,所述集成式箱体内设有格栅井、调节池区、污泥池区、清水池区、缺氧区、厌氧区、好氧区、膜池区以及设备区,所述格栅井与调节池区相连通,所述调节池区内设有潜水泵,所述潜水泵的输出端连接有调节池出水管,所述调节池出水管上连接有回流管,所述回流管与调节池区相连通,所述调节池出水管与缺氧区相连通,所述缺氧区与厌氧区相连通,所述厌氧区与好氧区相连通,所述好氧区与膜池区相连通,所述缺氧区、厌氧区、好氧区以及膜池区均与污泥池区相连通,所述膜池区与清水池区相连通;In order to achieve the above object, the present invention provides the following technical solutions: integrated integrated MBR sewage treatment equipment, including an integrated box body, the integrated box body is provided with a grid well, a regulating pool area, a sludge pool area, a clean water Pool area, anoxic area, anaerobic area, aerobic area, membrane pool area and equipment area, the grid well is connected with the adjustment pool area, and a submersible pump is arranged in the adjustment pool area, and the submersible pump The output end is connected with the outlet pipe of the regulating pool, and the outlet pipe of the regulating pool is connected with a return pipe, and the return pipe is connected with the regulating pool area, and the outlet pipe of the regulating pool is connected with the anoxic area, and the anoxic area It is connected with the anaerobic area, and the anaerobic area is connected with the aerobic area, and the aerobic area is connected with the membrane pool area, and the anoxic area, the anaerobic area, the aerobic area and the membrane pool area are all connected with the membrane pool area. The sludge pool area is connected, and the membrane pool area is connected with the clear water pool area;
所述缺氧区上连接有碳源加药管,所述缺氧区以及厌氧区内均设有混合搅拌器,所述缺氧区底部设有污泥回流管,且污泥回流管依次与厌氧区、好氧区以及膜池区相连通,所述污泥池区连接有进泥管,所述进泥管与污泥回流管相连通;The anoxic zone is connected with a carbon source dosing pipe, the anoxic zone and the anaerobic zone are equipped with mixing agitators, and the bottom of the anoxic zone is provided with a sludge return pipe, and the sludge return pipe is sequentially It communicates with the anaerobic area, the aerobic area and the membrane pool area, and the sludge pool area is connected with a mud inlet pipe, and the mud inlet pipe is connected with the sludge return pipe;
所述设备区内设有两个曝气风机,两个所述曝气风机分别连接有好氧池曝气管以及膜池曝气管,所述膜池曝气管与膜池区相连通,且所述膜池区内设有MBR膜组件,所述MBR膜组件与膜池曝气管相连,所述MBR膜组件上连接有膜产水管,所述膜池区内设有清水区,膜产水管与清水区相连通,所述清水区外分别设有清水区出水管以及清水区进水管,所述清水区进水管与清水池区相连通,所述清水池区上连接有设备排水管,所述设备排水管与清水区进水管相连,所述清水池区上连接有溢流管,所述清水区出水管与膜池清洗组件相连,所述好氧池曝气管与好氧区相连通,且好氧区内设有曝气管,所述曝气管与好氧池曝气管相连,所述污泥池区底部还设有穿孔曝气管,所述穿孔曝气管与膜池曝气管相连通,所述好氧区的上方连接有加药管;Two aeration fans are arranged in the equipment area, and the two aeration fans are respectively connected with an aeration pipe of an aerobic tank and an aeration pipe of a membrane pool, and the aeration tube of the membrane pool is connected with the membrane pool area, And the MBR membrane module is provided in the membrane pool area, the MBR membrane module is connected with the aeration pipe of the membrane pool, the membrane water production pipe is connected to the MBR membrane module, the clear water area is provided in the membrane pool area, the membrane The water production pipe is connected to the clean water area, and the clean water area outlet pipe and the clean water area inlet pipe are respectively arranged outside the clean water area, and the clean water area inlet pipe is connected to the clean water pool area, and the equipment drain pipe is connected to the clean water pool area , the equipment drain pipe is connected to the water inlet pipe of the clear water area, the overflow pipe is connected to the clear water pool area, the outlet pipe of the clear water area is connected to the membrane pool cleaning component, and the aeration pipe of the aerobic pool is connected to the aerobic area connected to each other, and an aeration pipe is provided in the aerobic area, and the aeration pipe is connected with the aeration pipe of the aerobic tank, and a perforated aeration pipe is also provided at the bottom of the sludge pond area, and the perforated aeration pipe is connected with the aeration pipe of the aerobic tank. The aeration pipes of the membrane pool are connected, and a dosing pipe is connected above the aerobic zone;
所述膜池区内设有回流泵,所述回流泵的输出端设有硝化液回流管,且硝化液回流管分别与缺氧区、厌氧区、好氧区以及膜池区相连通,并与进泥管相连。A reflux pump is provided in the membrane pool area, and the output end of the reflux pump is provided with a nitrification liquid return pipe, and the nitrification liquid return pipe is respectively connected with the anoxic area, the anaerobic area, the aerobic area and the membrane pool area, And connected with the mud pipe.
优选的,所述格栅井的进水端设有污水管,所述污水管内设有挡网,所述挡网用于对污水进行初步过滤,所述调节池区内设有调节潜水搅拌器,所述调节潜水搅拌器用于对进入的污水均和调节处理,使其水量和水质都比较稳定。Preferably, a sewage pipe is provided at the water inlet end of the grid well, and a retaining net is provided in the sewage pipe, and the retaining net is used for preliminary filtering of the sewage, and a regulating submersible mixer is provided in the regulating pool area , the regulating submersible mixer is used for homogenizing and regulating treatment of the incoming sewage, so that the water quantity and water quality are relatively stable.
优选的,所述曝气管设有多个,多个曝气管呈并排状分布,且均与好氧池曝气管相连通。Preferably, there are multiple aeration tubes, and the multiple aeration tubes are arranged side by side, and are all connected to the aeration tubes of the aerobic tank.
优选的,所述膜清洗组件包括膜清洗泵,所述膜清洗泵的输入端与清水区相连通,所述膜清洗泵的输出端连接有膜清洗出水管,所述膜清洗出水管一端与膜产水管相连通,另一端连接有膜清洗泵回水管,且膜清洗泵回水管与清水区进水管相连通,所述膜清洗泵出水管上连接有膜清洗加药管。Preferably, the membrane cleaning assembly includes a membrane cleaning pump, the input end of the membrane cleaning pump is connected to the clean water area, the output end of the membrane cleaning pump is connected to a membrane cleaning outlet pipe, and one end of the membrane cleaning outlet pipe is connected to The membrane water production pipes are connected, and the other end is connected with the return pipe of the membrane cleaning pump, and the return pipe of the membrane cleaning pump is connected with the water inlet pipe of the clean water area, and the outlet pipe of the membrane cleaning pump is connected with a membrane cleaning dosing pipe.
优选的,所述设备排水管上连接有取样管。Preferably, a sampling pipe is connected to the drain pipe of the device.
优选的,所述设备区内设有事故泵,所述事故泵输出端设有事故泵排水管,所述事故泵的输入端连通有清水区出水管相连通。Preferably, an emergency pump is provided in the equipment area, and an emergency pump drain pipe is provided at the output end of the emergency pump, and the input end of the emergency pump is connected to the outlet pipe of the clean water area.
优选的,所述膜产水管以及清水区进水管共同连接有自吸泵。Preferably, the membrane water production pipe and the water inlet pipe of the clean water area are jointly connected with a self-priming pump.
优选的,各个所述管路外均安装有管路支架。Preferably, a pipe support is installed outside each of the pipes.
与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:
(1)本发明为集成式一体化MBR污水处理设备,设置的调节池以及格栅井,由格栅井对进入的污水进行初步过滤,去除生活污水中的软性缠绕物、较大固颗粒杂物及飘浮物,调节潜水搅拌器用于对不同时间或不同来源的污水进行混合,使流出的水质比较均匀,以避免后续处理设施承受过大的冲击负荷,并对污水进行均和调节处理,使其水量和水质都比较稳定,以便于进行后续工序的处理。(1) The present invention is an integrated integrated MBR sewage treatment equipment, the adjustment pool and the grid well are set, and the sewage entering is initially filtered by the grid well to remove soft entanglements and larger solid particles in domestic sewage For sundries and floating objects, adjust the submersible mixer to mix sewage at different times or from different sources, so that the quality of the outflowing water is relatively uniform, so as to avoid excessive impact loads on subsequent treatment facilities, and to carry out equalization and adjustment treatment of sewage. Make its water quantity and water quality relatively stable, so as to facilitate the treatment of subsequent processes.
(2)本发明为集成式一体化MBR污水处理设备,设置的缺氧区、厌氧区以及好氧区,进入缺氧段,同步进入的还有从沉淀池排出的回流污泥,兼性厌氧发酵细菌将污水中的可生物降解的有机物转化为挥发性脂肪酸类物质VFA这类低分子发酵中间产物,而聚磷细菌可将其体内存储的聚磷酸盐分解,所释放的能量可供好氧的聚磷菌在厌氧环境下维持从生存,随后污水进入厌氧段,反硝化菌就利用好氧段进行反硝化,达到同时降低BOD5和脱氮的目的,污水进入曝气的好氧段,聚磷菌过量地摄取周围环境中的溶解磷,并以聚磷的形式在体内储存起来,使出水中溶解磷的浓度达到最低,实现脱氮脱磷。(2) The present invention is an integrated integrated MBR sewage treatment equipment. The anoxic zone, anaerobic zone and aerobic zone are set, enter the anoxic zone, and return sludge discharged from the sedimentation tank is also entered synchronously. Facultative Anaerobic fermentation bacteria convert biodegradable organic matter in sewage into low-molecular fermentation intermediates such as volatile fatty acid substances VFA, while phosphorus-accumulating bacteria can decompose polyphosphate stored in their bodies, and the energy released can be used for The aerobic phosphorus accumulating bacteria can survive in the anaerobic environment, and then the sewage enters the anaerobic section, and the denitrifying bacteria use the aerobic section to denitrify, so as to achieve the purpose of reducing BOD5 and denitrification at the same time, and the sewage enters the aeration section. In the oxygen section, phosphorus accumulating bacteria excessively ingest dissolved phosphorus in the surrounding environment, and store it in the body in the form of phosphorus accumulation, so that the concentration of dissolved phosphorus in the effluent reaches the lowest level, and denitrification and dephosphorization are realized.
(3)本发明为集成式一体化MBR污水处理设备,设置的MBR膜组件,大大提高了系统固液分离的能力,活性污泥浓度可以大大提高,水力停留时间和污泥停留时间可以分别控制,而难降解的物质在反器中不断反和降解,膜的机械截流作用避免了微生物的流失,生物反器内可保持高的污泥浓度,从而能降低污泥负荷,且MBR工艺略去了二沉池,大大减少占地面积,MBR曝气池的活性污泥不因产水而流失,系统出水稳定、耐冲击负荷,较大的水力循环导致了污水的均匀混合,因而使活性污泥有很好的分散性,大大提高活性污泥的比表面积,从而提升对污水处理效果。(3) The present invention is an integrated integrated MBR sewage treatment equipment. The MBR membrane module provided greatly improves the solid-liquid separation ability of the system, the concentration of activated sludge can be greatly improved, and the hydraulic retention time and sludge retention time can be controlled separately. , and the refractory substances are continuously reversed and degraded in the reactor, the mechanical interception effect of the membrane avoids the loss of microorganisms, and a high sludge concentration can be maintained in the bioreactor, thereby reducing the sludge load, and the MBR process omits The secondary sedimentation tank is installed, which greatly reduces the floor area. The activated sludge in the MBR aeration tank is not lost due to water production. The system effluent is stable and resistant to impact loads. The mud has good dispersibility, which greatly increases the specific surface area of activated sludge, thereby improving the effect of sewage treatment.
(4)本发明为集成式一体化MBR污水处理设备,设置的膜清洗组件,膜清洗组件根据MBR膜的使用周期对MBR膜组件进行清洗,保证设备的使用寿命,以及设备对污水的处理效果。(4) The present invention is an integrated integrated MBR sewage treatment equipment, and the membrane cleaning component is set. The membrane cleaning component cleans the MBR membrane component according to the service cycle of the MBR membrane, so as to ensure the service life of the equipment and the treatment effect of the equipment on sewage .
附图说明Description of drawings
图1为本发明的整体结构示意图;Fig. 1 is the overall structure schematic diagram of the present invention;
图2为本发明中设备间内部结构示意图;Fig. 2 is a schematic diagram of the internal structure of the equipment room in the present invention;
图3为本发明中膜池区剖面结构示意图。Fig. 3 is a schematic diagram of the cross-sectional structure of the membrane pool area in the present invention.
附图标记中:1、格栅井;11、污水管;2、调节池区;21、调节潜水搅拌器;22、潜水泵;23、回流管;24、调节池出水管;3、污泥池区;31、进泥管;32、穿孔曝气管;4、清水池区;41、设备排水管;42、溢流管;5、缺氧区;51、碳源加药管;52、混合搅拌器;53、污泥回流管;6、厌氧区;7、好氧区;71、曝气管;72、加药管;8、膜池区;81、MBR膜组件;82、膜产水管;83、回流泵;84、硝化液回流管;85、膜清洗泵;851、膜清洗泵出水管;852、膜清洗泵回水管;853、膜清洗加药管;86、清水区;861、清水区进水管;862、清水区出水管;87、取样管;9、设备区;91、事故泵;911、事故泵排水管;92、曝气风机;93、好氧池曝气管;94、膜池曝气管;95、自吸泵;10、管路支架。Among the reference signs: 1, grid well; 11, sewage pipe; 2, regulating pool area; 21, regulating submersible mixer; 22, submersible pump; 23, return pipe; 24, regulating pond outlet pipe; 3, sludge Pool area; 31, mud inlet pipe; 32, perforated aeration pipe; 4, clear water pool area; 41, equipment drain pipe; 42, overflow pipe; 5, anoxic area; 51, carbon source dosing pipe; 52, Mixer; 53. Sludge return pipe; 6. Anaerobic zone; 7. Aerobic zone; 71. Aeration tube; 72. Dosing tube; 8. Membrane tank zone; 81. MBR membrane module; 82. Membrane Water production pipe; 83, return pump; 84, nitrifying liquid return pipe; 85, membrane cleaning pump; 851, membrane cleaning pump outlet pipe; 852, membrane cleaning pump return pipe; 853, membrane cleaning dosing pipe; 86, clear water area; 861. Inlet pipe of clear water area; 862. Outlet pipe of clear water area; 87. Sampling pipe; 9. Equipment area; 91. Emergency pump; 911. Drainage pipe of emergency pump; 92. Aeration fan; 93. Aerobic tank aeration pipe ; 94, membrane tank aeration pipe; 95, self-priming pump; 10, pipeline support.
具体实施方式detailed description
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其它实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
实施例Example
请参阅图1-3所示,本发明提供集成式一体化MBR污水处理设备技术方案:包括集成式箱体,集成式箱体内设有格栅井1、调节池区2、污泥池区3、清水池区4、缺氧区5、厌氧区6、好氧区7、膜池区8以及设备区9,格栅井1与调节池区2相连通,调节池区2内设有潜水泵22,潜水泵22的输出端连接有调节池出水管24,调节池出水管24上连接有回流管23,回流管23与调节池区2相连通,调节池出水管24与缺氧区5相连通,缺氧区5与厌氧区6相连通,厌氧区6与好氧区7相连通,好氧区7与膜池区8相连通,缺氧区5、厌氧区6、好氧区7以及膜池区8均与污泥池区3相连通,膜池区8与清水池区4相连通;Please refer to Figures 1-3, the present invention provides an integrated integrated MBR sewage treatment equipment technical solution: including an integrated box body, the integrated box body is equipped with a grid well 1, a regulating
缺氧区5上连接有碳源加药管51,缺氧区5以及厌氧区6内均设有混合搅拌器52,缺氧区5底部设有污泥回流管53,且污泥回流管53依次与厌氧区6、好氧区7以及膜池区8相连通,污泥池区3连接有进泥管31,进泥管31与污泥回流管53相连通;The
设备区9内设有两个曝气风机92,两个曝气风机92分别连接有好氧池曝气管93以及膜池曝气管94,膜池曝气管94与膜池区8相连通,且膜池区8内设有MBR膜组件81,MBR膜组件81与膜池曝气管94相连,MBR膜组件81上连接有膜产水管82,膜池区8内设有清水区86,膜产水管82与清水区86相连通,清水区86外分别设有清水区出水管862以及清水区进水管861,清水区进水管861与清水池区4相连通,清水池区4上连接有设备排水管41,设备排水管41与清水区进水管861相连,清水池区4上连接有溢流管42,清水区出水管862与膜池清洗组件相连,好氧池曝气管93与好氧区7相连通,且好氧区7内设有曝气管71,曝气管71与好氧池曝气管93相连,污泥池区3底部还设有穿孔曝气管32,穿孔曝气管32与膜池曝气管94相连通,好氧区7的上方连接有加药管72;There are two aeration fans 92 in the equipment area 9, and the two aeration fans 92 are respectively connected to the aeration pipe 93 of the aerobic tank and the aeration pipe 94 of the membrane pool, and the aeration tube 94 of the membrane pool is connected with the area 8 of the membrane pool , and the MBR membrane module 81 is provided in the membrane pool area 8, the MBR membrane module 81 is connected to the membrane pool aeration pipe 94, the membrane water production pipe 82 is connected to the MBR membrane module 81, and the clear water area 86 is provided in the membrane pool area 8, The membrane production water pipe 82 is connected with the clear water area 86, and the clear water area 86 is respectively provided with a clear water area outlet pipe 862 and a clear water area inlet pipe 861, and the clear water area inlet pipe 861 is connected with the clear water pool area 4, and the clear water pool area 4 is connected with The equipment drain pipe 41, the equipment drain pipe 41 is connected to the water inlet pipe 861 of the clean water area, the overflow pipe 42 is connected to the clean water pool area 4, the water outlet pipe 862 of the clean water area is connected to the membrane pool cleaning component, and the aerobic pool aeration pipe 93 is connected to the well The oxygen area 7 is connected, and the aeration pipe 71 is arranged in the aerobic area 7, and the aeration pipe 71 is connected with the aeration pipe 93 of the aerobic tank. The
膜池区8内设有回流泵83,回流泵83的输出端设有硝化液回流管84,且硝化液回流管84分别与缺氧区5、厌氧区6、好氧区7以及膜池区8相连通,并与进泥管31相连。A
在本实施方式中,污水由污水管11进入,穿过格栅井1进入到调节池区2内,开启潜水泵22,潜水泵22将污水通过调节池出水管24注入到缺氧区5内,由缺氧区5上的碳源加药管51投放试剂,完成脱碳,并依次进入厌氧区6以及好氧区7,使其完成脱氮以及除磷作业,产生的污泥由污泥回流管53进行收集,并通过进泥管31进入污泥池区3,完成储存,曝气风机92运作,由好氧池曝气管93以及膜池曝气管94分别注入膜池区8以及好氧区7内,使其污水充分与氧气接触,进一步提高对污水的处理,去除污水中的各种有机物质,使污水中的有机物含量大幅度降低,污泥由进泥管31注入,处理后的水由清水区进水管861排入至清水池区4收集。In this embodiment, the sewage enters through the
进一步的,格栅井1的进水端设有污水管11,污水管11内设有挡网,挡网用于对污水进行初步过滤,调节池区2内设有调节潜水搅拌器21,调节潜水搅拌器21用于对进入的污水均和调节处理,使其水量和水质都比较稳定。Further, the water inlet end of the grid well 1 is provided with a
在本实施方式中,调节池区2内的调节潜水搅拌器21对不同污水进行混合搅拌,使流出的水质比较均匀,以避免后续处理设施承受过大的冲击负荷,。In this embodiment, the regulating
进一步的,曝气管71设有多个,多个曝气管71呈并排状分布,且均与好氧池曝气管93相连通。Further, there are a plurality of
在本实施方式中,多个曝气管71可使好氧区7内的污水充分的与氧气接触反应,去除污水中的各种有机物质,使污水中的有机物含量大幅度降低。In this embodiment, a plurality of
进一步的,膜清洗组件包括膜清洗泵85,膜清洗泵85的输入端与清水区86相连通,膜清洗泵85的输出端连接有膜清洗出水管851,膜清洗出水管851一端与膜产水管82相连通,另一端连接有膜清洗泵回水管852,且膜清洗泵回水管852与清水区进水管861相连通,膜清洗泵出水管851上连接有膜清洗加药管853。Further, the membrane cleaning component includes a
在本实施方式中,由膜清洗加药管853添加清洗药剂,并开启膜清洗泵85,膜清洗泵85通过膜清洗出水管851对水注入至清水区内,并逆向注入MBR膜组件81内,实行清洗。In this embodiment, the cleaning agent is added from the membrane
进一步的,设备排水管41上连接有取样管87。Further, a
在本实施方式中,取样管87能够对处理后的水进行取样检测。In this embodiment, the
进一步的,设备区9内设有事故泵91,事故泵91输出端设有事故泵排水管911,事故泵91的输入端连通有清水区出水管862相连通。Further, an
进一步的,膜产水管82以及清水区进水管861共同连接有自吸泵95。Further, a self-priming
在本实施方式中,自吸泵95能够保证处理后的水排出。In this embodiment, the self-priming
进一步的,各个管路外均安装有管路支架10。Further, a
在本实施方式中,管路支架10能够对管路进行稳定的支撑。In this embodiment, the
具体的,本发明的工作原理及使用流程:本发明安装好过后,污水由污水管11进入,穿过格栅井1进入到调节池区2内,开启潜水泵22,潜水泵22将污水通过调节池出水管24注入到缺氧区5内,由缺氧区5上的碳源加药管51投放试剂,完成脱碳,并依次进入厌氧区6以及好氧区7,使其完成脱氮以及除磷作业,产生的污泥由污泥回流管53进行收集,并通过进泥管31进入污泥池区3,完成储存,曝气风机92运作,由好氧池曝气管93以及膜池曝气管94分别注入膜池区8以及好氧区7内,使其污水充分与氧气接触,进一步提高对污水的处理,去除污水中的各种有机物质,使污水中的有机物含量大幅度降低,污泥由进泥管31注入,处理后的水由清水区进水管861排入至清水池区4收集,直至完成全部工作顺序。Specifically, the working principle and application process of the present invention: after the present invention is installed, the sewage enters from the
在本发明的描述中,需要理解的是,术语“同轴”、“底部”、“一端”、“顶部”、“中部”、“另一端”、“上”、“一侧”、“顶部”、“内”、“前部”、“中央”、“两端”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。In describing the present invention, it is to be understood that the terms "coaxial", "bottom", "one end", "top", "middle", "other end", "upper", "side", "top ", "inner", "front", "central", "both ends" and other indicated orientations or positional relationships are based on the orientations or positional relationships shown in the drawings, and are only for the convenience of describing the present invention and simplifying the description, and It is not to indicate or imply that the device or element referred to must have a particular orientation, be constructed in a particular orientation, or operate in a particular orientation, and thus should not be construed as limiting the invention.
在本发明中,除非另有明确的规定和限定,术语“安装”、“设置”、“连接”、“固定”、“旋接”等术语应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或成一体;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通或两个元件的相互作用关系,除非另有明确的限定,对于本领域的普通技术人员而言,可以根据具体情况理解上述术语在本发明中的具体含义。In the present invention, terms such as "installation", "installation", "connection", "fixation" and "rotation connection" should be interpreted in a broad sense unless otherwise clearly specified and limited, for example, it may be a fixed connection, or It can be a detachable connection or integrated; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediary; it can be the internal communication of two components or the interaction relationship between two components Unless otherwise clearly defined, those skilled in the art can understand the specific meanings of the above terms in the present invention according to specific situations.
尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although the embodiments of the present invention have been shown and described, those skilled in the art can understand that various changes, modifications and substitutions can be made to these embodiments without departing from the principle and spirit of the present invention. and modifications, the scope of the invention is defined by the appended claims and their equivalents.
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| CN103435232A (en) * | 2013-09-05 | 2013-12-11 | 中国水电顾问集团中南勘测设计研究院 | AABR (Anaerobic Baffled Reactor)-compound type MBR (Membrane Biological Reactor) integrated device and method for treating organic wastewater |
| CN103936231A (en) * | 2014-04-29 | 2014-07-23 | 广州市市政工程设计研究院 | Energy-saving type inverted AAO-MBR (anaerobic/anoxic/oxic-membrane bioreactor) sewage treatment method |
| CN205258126U (en) * | 2015-09-09 | 2016-05-25 | 广州能淼环保科技有限公司 | AAO - MBR integration nitrogen and phosphorus removal sewage treatment device |
| CN205821109U (en) * | 2016-06-20 | 2016-12-21 | 浙江精功环境技术有限公司 | Integrated domestic sewage treatment system |
| CN109502882A (en) * | 2018-11-15 | 2019-03-22 | 陈志坚 | A kind of sewage disposal device and its processing method |
| CN109502919A (en) * | 2018-12-25 | 2019-03-22 | 武汉市木兰碧波环保科技有限公司 | A kind of processing method of domestic sewage in rural areas |
| CN210103689U (en) * | 2019-05-20 | 2020-02-21 | 青岛鑫源环保集团有限公司 | Integrated membrane method treatment equipment for domestic sewage |
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| CN116789329A (en) * | 2023-08-04 | 2023-09-22 | 青岛鑫源环保集团有限公司 | Water purification sewage treatment plant that possesses denitrification function |
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