CN202063793U - Biological response system used for multi-stage sewage treatment - Google Patents
Biological response system used for multi-stage sewage treatment Download PDFInfo
- Publication number
- CN202063793U CN202063793U CN2011200255318U CN201120025531U CN202063793U CN 202063793 U CN202063793 U CN 202063793U CN 2011200255318 U CN2011200255318 U CN 2011200255318U CN 201120025531 U CN201120025531 U CN 201120025531U CN 202063793 U CN202063793 U CN 202063793U
- Authority
- CN
- China
- Prior art keywords
- water
- pond
- wetland
- processing unit
- pool
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 205
- 230000008512 biological response Effects 0.000 title description 2
- 230000007062 hydrolysis Effects 0.000 claims abstract description 246
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 246
- 238000005273 aeration Methods 0.000 claims abstract description 114
- 238000006243 chemical reaction Methods 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 634
- 238000000354 decomposition reaction Methods 0.000 claims description 157
- 230000003647 oxidation Effects 0.000 claims description 145
- 238000007254 oxidation reaction Methods 0.000 claims description 145
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 109
- 239000001301 oxygen Substances 0.000 claims description 109
- 229910052760 oxygen Inorganic materials 0.000 claims description 109
- 239000007788 liquid Substances 0.000 claims description 85
- 238000000855 fermentation Methods 0.000 claims description 75
- 230000004151 fermentation Effects 0.000 claims description 67
- 238000012545 processing Methods 0.000 claims description 55
- 238000012423 maintenance Methods 0.000 claims description 44
- 239000011159 matrix material Substances 0.000 claims description 31
- 239000000945 filler Substances 0.000 claims description 26
- 244000005700 microbiome Species 0.000 claims description 25
- 238000001556 precipitation Methods 0.000 claims description 22
- 238000005276 aerator Methods 0.000 claims description 17
- 238000007789 sealing Methods 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 16
- 239000002893 slag Substances 0.000 claims description 16
- 238000001514 detection method Methods 0.000 claims description 14
- 239000002245 particle Substances 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims description 10
- 230000000813 microbial effect Effects 0.000 claims description 10
- 239000002351 wastewater Substances 0.000 claims description 7
- 239000004698 Polyethylene Substances 0.000 claims description 3
- -1 polyethylene Polymers 0.000 claims description 3
- 229920000573 polyethylene Polymers 0.000 claims description 3
- 238000011010 flushing procedure Methods 0.000 claims 18
- 239000000706 filtrate Substances 0.000 claims 9
- 210000002615 epidermis Anatomy 0.000 claims 2
- 238000009395 breeding Methods 0.000 claims 1
- 230000001488 breeding effect Effects 0.000 claims 1
- 229920001971 elastomer Polymers 0.000 claims 1
- 239000000806 elastomer Substances 0.000 claims 1
- 238000003306 harvesting Methods 0.000 claims 1
- 230000004941 influx Effects 0.000 claims 1
- 238000005070 sampling Methods 0.000 claims 1
- 238000004062 sedimentation Methods 0.000 abstract description 144
- 230000020477 pH reduction Effects 0.000 abstract description 75
- 238000006213 oxygenation reaction Methods 0.000 abstract description 58
- 238000013461 design Methods 0.000 abstract description 29
- 230000000694 effects Effects 0.000 abstract description 13
- 238000005516 engineering process Methods 0.000 abstract description 9
- 238000000746 purification Methods 0.000 abstract description 8
- 239000010410 layer Substances 0.000 description 201
- 238000005325 percolation Methods 0.000 description 121
- 238000003860 storage Methods 0.000 description 49
- 238000005192 partition Methods 0.000 description 48
- 238000001764 infiltration Methods 0.000 description 42
- 230000008595 infiltration Effects 0.000 description 42
- 230000003301 hydrolyzing effect Effects 0.000 description 40
- 241000196324 Embryophyta Species 0.000 description 39
- 238000009826 distribution Methods 0.000 description 32
- 238000000034 method Methods 0.000 description 27
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 24
- 239000005416 organic matter Substances 0.000 description 24
- 238000007689 inspection Methods 0.000 description 23
- 230000008569 process Effects 0.000 description 22
- 239000013049 sediment Substances 0.000 description 21
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 19
- 238000007667 floating Methods 0.000 description 19
- 239000011574 phosphorus Substances 0.000 description 19
- 229910052698 phosphorus Inorganic materials 0.000 description 19
- 235000013601 eggs Nutrition 0.000 description 18
- 238000013022 venting Methods 0.000 description 18
- 210000003608 fece Anatomy 0.000 description 17
- 230000005484 gravity Effects 0.000 description 17
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 16
- 238000009825 accumulation Methods 0.000 description 16
- 239000002344 surface layer Substances 0.000 description 15
- 238000011001 backwashing Methods 0.000 description 14
- 244000045947 parasite Species 0.000 description 13
- 238000001914 filtration Methods 0.000 description 12
- 229910052757 nitrogen Inorganic materials 0.000 description 12
- 231100000719 pollutant Toxicity 0.000 description 12
- 239000003344 environmental pollutant Substances 0.000 description 11
- 239000000126 substance Substances 0.000 description 11
- 241000255925 Diptera Species 0.000 description 8
- 230000009471 action Effects 0.000 description 8
- 229910021529 ammonia Inorganic materials 0.000 description 8
- 244000052616 bacterial pathogen Species 0.000 description 8
- 239000007787 solid Substances 0.000 description 8
- 238000004891 communication Methods 0.000 description 7
- 230000015556 catabolic process Effects 0.000 description 6
- 238000010276 construction Methods 0.000 description 6
- 238000006731 degradation reaction Methods 0.000 description 6
- 125000001477 organic nitrogen group Chemical group 0.000 description 6
- 230000032258 transport Effects 0.000 description 6
- 238000009360 aquaculture Methods 0.000 description 5
- 244000144974 aquaculture Species 0.000 description 5
- 239000002957 persistent organic pollutant Substances 0.000 description 5
- 239000006228 supernatant Substances 0.000 description 5
- 241000894006 Bacteria Species 0.000 description 4
- 230000006870 function Effects 0.000 description 4
- 102000004169 proteins and genes Human genes 0.000 description 4
- 108090000623 proteins and genes Proteins 0.000 description 4
- 230000008439 repair process Effects 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 4
- 241000894007 species Species 0.000 description 4
- 230000003068 static effect Effects 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 241000238631 Hexapoda Species 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 244000000010 microbial pathogen Species 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 239000004202 carbamide Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 210000003437 trachea Anatomy 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 241001633663 Iris pseudacorus Species 0.000 description 1
- 235000014676 Phragmites communis Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 240000001398 Typha domingensis Species 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 238000009412 basement excavation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 230000002925 chemical effect Effects 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000012938 design process Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 159000000014 iron salts Chemical class 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000003071 parasitic effect Effects 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
Classifications
-
- 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
- Biological Treatment Of Waste Water (AREA)
Abstract
本实用新型是多级污水处理用生物反应系统。多级沉淀预处理单元、多级水解酸化处理单元、曝气增氧处理单元和多级潜流湿地处理单元通过管路相连接构成,多级潜流湿地处理单元的进水湿地池、2组分解渗滤湿地池和出水湿地池依次排列,多级潜流湿地处理单元的一侧并列依次设置多级沉淀预处理单元、多级水解酸化处理单元和曝气增氧处理单元,并通过管路相连接。本实用新型设计科学,结构合理,主要采用自流方式,机电设备较少,运行成本低,污水处理费低,占地面积小,污水处理效果明显,可直接排入水库、河道和湖泊,运转维护管理方便,工程基建与运转费用低,一年四季都能进行净化处理,生物生态技术具有较强的自我调节能力和修复能力,污水处理符合国家排放标准。
The utility model is a biological reaction system for multi-stage sewage treatment. The multi-stage sedimentation pretreatment unit, the multi-stage hydrolysis acidification treatment unit, the aeration and oxygenation treatment unit and the multi-stage subsurface flow wetland treatment unit are connected by pipelines. The filter wetland pool and the effluent wetland pool are arranged in sequence, and one side of the multi-stage subsurface flow wetland treatment unit is arranged side by side with a multi-stage sedimentation pretreatment unit, a multi-stage hydrolysis acidification treatment unit and an aeration and oxygenation treatment unit, which are connected by pipelines. The utility model is scientific in design, reasonable in structure, mainly adopts self-flow mode, less electromechanical equipment, low operating cost, low sewage treatment fee, small floor area, obvious sewage treatment effect, can be directly discharged into reservoirs, rivers and lakes, and is easy to operate and maintain. The management is convenient, the project infrastructure and operation costs are low, and purification can be carried out all year round. The bio-ecological technology has strong self-regulation and restoration capabilities, and the sewage treatment meets the national discharge standards.
Description
技术领域 technical field
本实用新型涉及一种废水、污水的处理设施,尤其涉及一种多级污水处理用生物反应系统。 The utility model relates to a treatment facility for waste water and sewage, in particular to a biological reaction system for multi-stage sewage treatment. the
背景技术 Background technique
水污染会造成了生态系统的退化以及河道、湖泊水体的生物多样性的减少,目前我国许多地区的地表水质量差,且呈日益恶化趋势,流经大城市的河流污染尤其严重,在生态恶化的同时,严重影响城市的景观。通常城市污水处理厂是以工业和城市生活污水为处理对象,出水水质为二级标准,上述流经城市的河水、湖水的水质普遍为五类或劣五类,不适宜建立污水处理厂进行污水处理。20世纪70年代以来,人工湿地水处理技术开始受到人们的关注,具有低投资、低能耗等优点,成为水环境技术的研究热点。 Water pollution will cause the degradation of the ecosystem and the reduction of biodiversity in rivers and lakes. At present, the quality of surface water in many areas of our country is poor, and it is showing a deteriorating trend. The pollution of rivers flowing through large cities is particularly serious. Ecological deterioration At the same time, it seriously affects the landscape of the city. Usually, urban sewage treatment plants treat industrial and urban domestic sewage as the treatment object, and the effluent water quality is the second-level standard. deal with. Since the 1970s, water treatment technology of constructed wetlands has attracted people's attention. It has the advantages of low investment and low energy consumption, and has become a research hotspot in water environment technology. the
目前国际上采用的技术主要有三类:①化学方法:如加入化学药剂杀藻、加入铁盐促进磷的沉淀、加入石灰脱氮等,但是易造成二次污染;②物理方法:疏挖底泥、引水冲淤等,但往往治标不治本;③生态-生物方法:是国外近年来发展很快的一种新技术,水体生态-生物修复技术是按照自然界自身规律去恢复自然界的本来面貌,强化自然界自身的自净能力去治理被污染水体。 At present, there are three main types of technologies used in the world: ①Chemical methods: such as adding chemical agents to kill algae, adding iron salts to promote the precipitation of phosphorus, adding lime to denitrify, etc., but it is easy to cause secondary pollution; ②Physical methods: dredging sediment , Diversion of water to wash away silt, etc., but often treat the symptoms but not the root cause; ③Ecological-biological method: It is a new technology that has developed rapidly abroad in recent years. Nature's own self-purification ability to treat polluted water bodies. the
现有的人工湿地包括三个关键组成部分:植物、微生物、基质,人工建造不同粒径的填料为基质形成基床的床体,床体表面种植高效去污的耐水植物,扎根于基质床体内,基质支持着这些植物的根系,而基质和植物根系又为各种微生物提供附着的载体,在基质和植物根系表面形成微生物膜,水体以潜流形式渗过长有植物的潜层多孔滤床,基质床体内浸满了水体,通过潜流湿地中的物理、化学和生物作用,优化组合来完成对水体的净化。但仍存在很多缺陷和不足,人工湿地内部在溶解氧含量较低的情况下,造成表层好氧区的好氧微生物作用减弱,出水的水质较差,出水溶解氧浓度较低,不利于受纳水体的自净。基质填料大多采用砾石填料床为主,基质填料的品种和组成结构比较单一,基质填料的组份单一形成渗透系统较均一,水体的运行过程为简单水平运动,上、下水体交换较差,造成上层好氧和下层厌气区水流交换较弱,导致净化处理效果下降。部分水平流湿地为增加上下层水体的交换和延长水流路径,在湿地处理池底部人为的设置阻水堰,虽然增加上下层水体的交换强度以及延长水流路径,但容易形成死水区,造成整体净化处理的效率下降。 The existing constructed wetland consists of three key components: plants, microorganisms, and matrix. Fillers with different particle sizes are artificially constructed as the matrix to form the bed body. Water-resistant plants with high-efficiency decontamination are planted on the surface of the bed body, and they are rooted in the matrix bed. , the matrix supports the roots of these plants, and the matrix and plant roots provide a carrier for various microorganisms to attach to, forming a microbial film on the surface of the matrix and plant roots, and the water seeps through the subsurface porous filter bed with plants in the form of subsurface flow. The matrix bed is filled with water, and the purification of the water is completed through the optimal combination of physical, chemical and biological effects in the subsurface wetland. However, there are still many defects and deficiencies. When the dissolved oxygen content in the constructed wetland is low, the aerobic microorganisms in the surface aerobic zone are weakened, the water quality of the effluent is poor, and the concentration of dissolved oxygen in the effluent is low, which is not conducive to receiving Self-purification of water bodies. Most of the matrix fillers are made of gravel packing beds. The variety and composition of matrix fillers are relatively simple. The single composition of matrix fillers forms a relatively uniform permeation system. The operation process of the water body is simple horizontal movement, and the exchange of upper and lower water bodies is poor, resulting in The water flow exchange between the upper aerobic zone and the lower anaerobic zone is weak, resulting in a decline in the purification treatment effect. In order to increase the exchange of upper and lower water bodies and prolong the water flow path in some horizontal flow wetlands, weirs are artificially set up at the bottom of the wetland treatment pool. Although the exchange intensity of the upper and lower water bodies is increased and the water flow path is extended, it is easy to form dead water areas and cause overall purification. Processing efficiency drops. the
实用新型内容 Utility model content
本实用新型的主要目的在于解决上述污水处理中存在的问题,提供一种优先生态型、绿色环保型、节能型工艺、机电设备少、具有生物生态自我调节能力和修复能力的多级污水处理用生物反应系统。 The main purpose of this utility model is to solve the problems existing in the above-mentioned sewage treatment, and provide a multi-stage sewage treatment with priority ecological type, green environmental protection type, energy-saving technology, less electromechanical equipment, and biological ecological self-regulation ability and repair ability. biological response system. the
水处理工艺方法由于处理工艺不同,占地面积、处理特性、所需设备数量、处理成本、产泥量等也各不相同,应根据不同的地区特点,因地制宜,选定适合的污水处理方法。 Due to the different treatment processes, the water treatment process has different floor area, treatment characteristics, number of required equipment, treatment cost, mud production, etc., and the appropriate sewage treatment method should be selected according to the characteristics of different regions and local conditions. the
本实用新型在设计污水处理上考虑的因素有:处理水量规模,进水和出水水质,水质、水量的变化情况,占地面积大小,维护管理的难易程度,经济性包括建设费和运行费,对周边环境的影响,工程实际应用情况,处理性能情况,包括处理效果、处理的稳定性、抗冲击负荷性能、产泥量及污泥的稳定化程度等。 The factors considered in the design of sewage treatment in this utility model are: the scale of water treatment, the quality of influent and effluent water, the change of water quality and water quantity, the size of the occupied area, the difficulty of maintenance and management, and the economy including construction costs and operating costs , the impact on the surrounding environment, the actual application of the project, and the treatment performance, including the treatment effect, treatment stability, impact load resistance, sludge production and sludge stabilization degree, etc. the
本实用新型解决其技术问题所采用的技术方案是: The technical scheme that the utility model solves its technical problem adopts is:
由多级沉淀预处理单元、多级水解酸化处理单元、曝气增氧处理单元和多级潜流湿地处理单元通过管路相连接构成,多级潜流湿地处理单元的进水湿地池、2组分解渗滤湿地池和出水湿地池依次排列,多级潜流湿地处理单元的一侧并列依次设置多级沉淀预处理单元、多级水解酸化处理单元和曝气增氧处理单元,并通过管路相连接,或者多级沉淀预处理单元、多级水解酸化处理单元、曝气增氧处理单元和多级潜流湿地处理单元依次排列设置并通过管路相连接。 It is composed of multi-stage sedimentation pretreatment unit, multi-stage hydrolysis acidification treatment unit, aeration and oxygenation treatment unit and multi-stage subsurface flow wetland treatment unit connected by pipelines. The percolation wetland pool and the effluent wetland pool are arranged in sequence, and one side of the multi-stage subsurface flow wetland treatment unit is arranged side by side with a multi-stage sedimentation pretreatment unit, a multi-stage hydrolysis acidification treatment unit and an aeration and oxygenation treatment unit, which are connected by pipelines , or a multi-stage sedimentation pretreatment unit, a multi-stage hydrolytic acidification treatment unit, an aeration and aeration treatment unit and a multi-stage subsurface flow wetland treatment unit are arranged in sequence and connected by pipelines. the
工程设计中应在保证水质处理效果的前提下,充分利用现有地形和地貌的条件,因地制宜进行设计,尽量减少工程占地,减少土方开挖的工程量。设计过程中应按照循环经济的理念,优先选用生态型、绿色环保型、节能型工艺,最大限度地减少不可再生能源的消耗。按照不同的环境、区域以及时段,应用各项技术,统筹安排,科学设计,得到最佳的水环境治理效果,保证输水水质的安全。工程的设计与周边环境景观及生态建设相结合,在满足水环境改善的前提下,美化周围环境。 In engineering design, under the premise of ensuring the effect of water quality treatment, make full use of the existing terrain and landform conditions, design according to local conditions, minimize the land occupation of the project, and reduce the amount of earthwork excavation. During the design process, the concept of circular economy should be followed, and ecological, green, and energy-saving processes should be preferred to minimize the consumption of non-renewable energy. According to different environments, regions and time periods, apply various technologies, make overall arrangements, and scientifically design to obtain the best water environment treatment effect and ensure the safety of water quality. The design of the project is combined with the surrounding environmental landscape and ecological construction to beautify the surrounding environment on the premise of satisfying the improvement of the water environment. the
全部工程根据实际情况设计布局,由多级沉淀预处理单元、多级水解酸化处理单元、曝气增氧处理单元和多级潜流湿地处理单元组成,总体呈长方形布置,其中多级沉淀预处理单元、多级水解酸化处理单元、曝气增氧处理单元并排布置在一侧,多级潜流湿地处理单元布置在另一侧。也可以把多级沉淀预处理单元、多级水解酸化处理单元、曝气增氧处理单元和多级潜流湿地处理单元一字排开,按照污水处理工序排列。 The layout of the entire project is designed according to the actual situation. It consists of a multi-stage sedimentation pretreatment unit, a multi-stage hydrolysis acidification treatment unit, an aeration and oxygenation treatment unit and a multi-stage subsurface flow wetland treatment unit. The overall layout is rectangular, and the multi-stage sedimentation pretreatment unit The multi-stage hydrolytic acidification treatment unit and the aeration and oxygenation treatment unit are arranged side by side on one side, and the multi-stage subsurface flow wetland treatment unit is arranged on the other side. It is also possible to line up the multi-stage sedimentation pretreatment unit, the multi-stage hydrolytic acidification treatment unit, the aeration and oxygenation treatment unit and the multi-stage subsurface flow wetland treatment unit, and arrange them according to the sewage treatment process. the
污水源包括生活污水和养殖废水,污水源经管道收集后自流进入多级沉淀预处理单元内,多级沉淀预处理单元出水再自流进入多级水解酸化处理单元内,多级水解酸化处理单元出水进入集水池后,经水泵提升进入曝气增氧处理单元内,经曝气后出水自流进入多级潜流湿地处理单元,经好氧、厌氧、硝化和反硝化的反应过程后排放到河道或湖泊,全部设计采用开放式布局,便于景观建设。 Sewage sources include domestic sewage and aquaculture wastewater. The sewage sources are collected by pipelines and then flow into the multi-stage sedimentation pretreatment unit. After entering the sump, it is lifted by the water pump into the aeration and oxygenation treatment unit. After aeration, the effluent flows into the multi-stage subsurface flow wetland treatment unit by itself, and is discharged into the river or All lakes are designed with an open layout, which is convenient for landscape construction. the
多级沉淀预处理单元呈封闭箱体,箱体内由隔板分隔成至少3个空间,其空间依次分别为沉淀分解池、发酵沉淀池和蓄积池,每个空间顶部设置密闭的清渣口,清渣口上安设密封盖,构成密闭的运行空间。 The multi-stage sedimentation pretreatment unit is a closed box. The box is divided into at least 3 spaces by partitions. The spaces are respectively sedimentation and decomposition tanks, fermentation sedimentation tanks and storage tanks. A closed slag removal port is set on the top of each space. A sealing cover is installed on the slag cleaning port to form a closed operating space. the
污水源中夹带有一定量的悬浮物、漂浮物和泥沙之类,直接进入多级水 解酸化处理单元和多级潜流湿地处理单元会造成后续工艺的堵塞,影响整个系统的正常运行。故此,在进入多级水解酸化处理单元和多级潜流湿地处理单元之前,应拦截污水源中夹带的悬浮物、漂浮物和泥沙之类,是将悬浮物、漂浮物和泥沙实施收集、无害化处理、水量调节和沉淀功能,在同一流程中进行的一种预处理装置。沉淀分解池、发酵沉淀池和蓄积池的顶部设置清渣口,清渣口上盖上密封盖,保持沉淀分解池、发酵沉淀池和蓄积池处于密闭的环境。依据污水源的水质情况,多级沉淀预处理单元根据设计要求可以分隔设置成多个密闭的空间,实施污水预处理。 There is a certain amount of suspended solids, floating solids and sediment in the sewage source, which will directly enter the multi-stage hydrolysis acidification treatment unit and the multi-stage subsurface flow wetland treatment unit, which will cause blockage of subsequent processes and affect the normal operation of the entire system. Therefore, before entering the multi-stage hydrolysis acidification treatment unit and the multi-stage subsurface flow wetland treatment unit, the suspended matter, floating matter and sediment entrained in the sewage source should be intercepted, and the suspended matter, floating matter and sediment should be collected, Harmless treatment, water adjustment and sedimentation functions, a pretreatment device that is carried out in the same process. The tops of the sedimentation and decomposition tanks, fermentation sedimentation tanks and storage tanks are provided with slag removal ports, and the slag removal ports are covered with a sealing cover to keep the sedimentation decomposition tanks, fermentation sedimentation tanks and storage tanks in a closed environment. According to the water quality of the sewage source, the multi-stage sedimentation pretreatment unit can be divided into multiple closed spaces according to the design requirements to implement sewage pretreatment. the
多级沉淀预处理单元一侧的沉淀分解池的池壁上部设置进污口,进污口通过管路引入污水源,进污口的管路上设置闸阀,控制污水源的流入量,污水源为生活污水和养殖废水。沉淀分解池和发酵沉淀池之间的隔板中部设置倾斜的过流管至少1个,沉淀分解池的过流管的入口低于发酵沉淀池的过流管的出口,沉淀分解池内的污水源经沉淀、分解后的污水水体受水体重力作用从过流管流入发酵沉淀池内发酵、沉淀。 The upper part of the pool wall of the sedimentation and decomposition tank on the side of the multi-stage sedimentation pretreatment unit is provided with a sewage inlet. Domestic sewage and aquaculture wastewater. At least one inclined overflow pipe is set in the middle of the partition between the sedimentation and decomposition tank and the fermentation sedimentation tank. The sedimented and decomposed sewage water is subjected to the gravity of the water and flows from the overflow pipe into the fermentation sedimentation tank for fermentation and sedimentation. the
沉淀分解池主要截留含虫卵较多的粪便,松散的粪块因发酵、膨胀而向上浮升,比重大的下沉,形成上浮的粪皮、中层的粪液和下沉的粪渣,寄生虫属于比重大自然沉降于池底。沉淀分解池是密闭的厌氧环境的密闭池,蛋白性有机物经过厌氧发酵则被而分解,并产生氨等物质,具有杀灭寄生虫卵及病菌的作用。 The sedimentation and decomposition tank mainly retains feces containing more eggs. The loose feces float upward due to fermentation and expansion, and the larger ones sink to form floating feces, middle layer of feces and sinking feces. Parasitic The worms belong to a large proportion and naturally settle to the bottom of the pool. The sedimentation decomposition tank is a closed tank in a closed anaerobic environment. Protein organic matter is decomposed through anaerobic fermentation, and ammonia and other substances are produced, which can kill parasite eggs and pathogenic bacteria. the
污水源在沉淀分解池内经沉淀、分解后,污水源实现分离,处于中层的污水水体在水体重力的作用下,通过倾斜安设在隔板中部的过流管进入发酵沉淀池。多级沉淀预处理单元利用水体的自重力的作用以及污水源分离后的状态,在隔板上倾斜安设的过流管,水体从过流管中流过,悬浮物、漂浮物和沉渣阻隔在沉淀分解池内。 After the sewage source is precipitated and decomposed in the sedimentation and decomposition tank, the sewage source is separated, and the sewage water body in the middle layer enters the fermentation sedimentation tank through the overflow pipe installed obliquely in the middle of the partition under the action of water gravity. The multi-stage sedimentation pretreatment unit utilizes the self-gravity of the water body and the state after the separation of the sewage source. The overflow pipe installed obliquely on the partition, the water body flows through the overflow pipe, and the suspended matter, floating matter and sediment are blocked. Sediment decomposition tank. the
发酵沉淀池和蓄积池之间的隔板中部设置倾斜的过流管,发酵沉淀池的过流管的入口低于蓄积池的过流管的出口,发酵沉淀池内的污水水体又经发酵、沉淀后的污水液受水体重力作用从过流管流入蓄积池内分离、沉淀。 An inclined overflow pipe is set in the middle of the partition between the fermentation sedimentation tank and the storage tank. The inlet of the overflow pipe of the fermentation sedimentation tank is lower than the outlet of the overflow pipe of the storage tank. The sewage water in the fermentation sedimentation tank is fermented and settled. Under the action of water gravity, the sewage liquid flows from the overflow pipe into the storage tank for separation and sedimentation. the
发酵沉淀池进一步实施发酵、沉淀,与沉淀分解池相比,发酵沉淀池的粪皮和粪渣以及悬浮物和漂浮物的数量相应的减少,发酵、分解的程度较低,由于没有新污水源进入,污水液体处于比较静止状态,有利于漂浮在发酵沉淀池中的虫卵继续下沉,进一步分离污水液中的水体、悬浮物、漂浮物,把进一步分离出来的清液污水水体输送到蓄积池内。 The fermentation and sedimentation tank further implements fermentation and sedimentation. Compared with the sedimentation and decomposition tank, the number of dung skin and dung, suspended matter and floating matter in the fermentation and sedimentation tank is correspondingly reduced, and the degree of fermentation and decomposition is low. Since there is no new sewage source Entering, the sewage liquid is in a relatively static state, which is conducive to the continued sinking of the eggs floating in the fermentation sedimentation tank, further separating the water body, suspended matter, and floating matter in the sewage liquid, and transporting the further separated clear liquid sewage water body to the accumulation pool. the
多级沉淀预处理单元另一侧的蓄积池的池壁上部设置出水口,通过管路与多级水解酸化处理单元的池壁下部的进水口相连接,管路上设置闸阀,控制输出流量,进入蓄积池内的污水液水体再经发酵、沉淀后的清液水体从池壁上部的出水口通过管路自流输入多级水解酸化处理单元的进水口,管路上设置控制闸阀控制输入多级水解酸化处理单元的流量,进入多级沉淀预处理单元的污水源的流向自多级沉淀预处理单元一端的进污口利用水体的自重通过过流管向多级沉淀预处理单元另一端的出水口顺流流动,在流动的过程中 实施沉淀、发酵、分解、灭菌制成清液污水水体。 The upper part of the tank wall on the other side of the multi-stage sedimentation pretreatment unit is provided with a water outlet, which is connected to the water inlet at the lower part of the multi-stage hydrolysis acidification treatment unit through a pipeline. A gate valve is set on the pipeline to control the output flow and enter The sewage liquid water in the storage tank is fermented and precipitated, and the clear liquid water is fed into the water inlet of the multi-stage hydrolysis and acidification treatment unit through the pipeline from the outlet on the upper part of the tank wall, and the control gate valve is set on the pipeline to control the input into the multi-stage hydrolysis and acidification treatment The flow of the unit, the flow of the sewage source entering the multi-stage sedimentation pretreatment unit flows downstream from the sewage inlet at one end of the multi-stage sedimentation pretreatment unit through the overflow pipe to the outlet at the other end of the multi-stage sedimentation pretreatment unit by using the self-weight of the water body Flow, in the process of flow, carry out sedimentation, fermentation, decomposition, and sterilization to make clear liquid sewage water. the
多级沉淀预处理单元的蓄积池主要起储存污水液体的作用,经过沉淀分解池、发酵沉淀池的处理,蓄积池内已经基本上不含寄生虫卵和病原微生物,达到了污水源无害化要求,制成清液污水水体。污水源经过沉淀分解池、发酵沉淀池和蓄积池的发酵、沉淀和分解,能较好地起到杀灭虫卵及细菌的作用,蓄积池内的清液污水水体从安设在池壁上部的出水口通过管路进入多级水解酸化处理单元。 The storage tank of the multi-stage sedimentation pretreatment unit mainly plays the role of storing sewage liquid. After the treatment of the sedimentation decomposition tank and the fermentation sedimentation tank, the storage tank basically does not contain parasite eggs and pathogenic microorganisms, which meets the requirements of harmless sewage sources. , to make clear liquid sewage water body. The sewage source passes through the fermentation, sedimentation and decomposition of the sedimentation and decomposition tank, the fermentation sedimentation tank and the storage tank, which can better kill insect eggs and bacteria. The water outlet enters the multi-stage hydrolysis acidification treatment unit through the pipeline. the
多级沉淀预处理单元的出水口与多级水解酸化处理单元的进水口通过管路相连接,多级沉淀预处理单元的出水口与多级水解酸化处理单元的进水口实现一个落差,形成多级沉淀预处理单元的出水口向多级水解酸化处理单元的进水口自流。 The water outlet of the multi-stage sedimentation pretreatment unit is connected with the water inlet of the multi-stage hydrolysis acidification treatment unit through pipelines, and the water outlet of the multi-stage sedimentation pretreatment unit and the water inlet of the multi-stage hydrolysis acidification treatment unit realize a drop, forming multiple The water outlet of the one-stage sedimentation pretreatment unit flows to the water inlet of the multi-stage hydrolysis acidification treatment unit by itself. the
多级水解酸化处理单元呈封闭箱体,多级水解酸化处理单元一端的池壁下部设置进水口,多级水解酸化处理单元另一端的池壁上部设置出水口,出水口的管路上设置闸阀,控制输出流量。多级水解酸化处理单元的箱体内由隔板分隔成至少3个空间,其空间依次为进水水解氧化池、水解氧化池和出水水解氧化池,进水水解氧化池、水解氧化池和出水水解氧化池的顶部分别设置密闭的检修口,检修口上安设密封盖,在进水水解氧化池、水解氧化池和出水水解氧化池的隔板上设置L形过流管,L形过流管的进水口高于水解过滤层的顶端部,收集经过水解过滤层实施水解过滤的污水水体,L形过流管的出水口处于另一空间的水解过滤层内的下部,把水解过滤的污水水体输送到下一个水解过滤层,连通进水水解氧化池、水解氧化池和出水水解氧化池。 The multi-stage hydrolytic acidification treatment unit is in the form of a closed box. The lower part of the pool wall at one end of the multi-stage hydrolysis acidification treatment unit is provided with a water inlet, and the upper part of the pool wall at the other end of the multi-stage hydrolysis acidification treatment unit is provided with a water outlet. A gate valve is provided on the pipeline of the water outlet. Control output flow. The box of the multi-stage hydrolysis acidification treatment unit is divided into at least 3 spaces by partitions, and the spaces are successively the influent hydrolysis oxidation pool, the hydrolysis oxidation pool and the effluent hydrolysis oxidation pool, the inflow hydrolysis oxidation pool, the hydrolysis oxidation pool and the effluent hydrolysis tank. The top of the oxidation tank is provided with a closed inspection port, and a sealing cover is installed on the inspection port, and an L-shaped overcurrent tube is arranged on the separator of the influent hydrolysis oxidation tank, the hydrolysis oxidation tank and the outlet water hydrolysis oxidation tank, and the L-shaped over-current tube The water inlet is higher than the top of the hydrolysis filter layer, and collects the sewage water body that is hydrolyzed and filtered through the hydrolysis filter layer. The outlet of the L-shaped overflow pipe is located in the lower part of the hydrolysis filter layer in another space, and transports the hydrolysis filtered sewage water body To the next hydrolysis filter layer, it is connected to the influent hydrolysis oxidation pool, the hydrolysis oxidation pool and the outlet water hydrolysis oxidation pool. the
在进水水解氧化池、水解氧化池和出水水解氧化池内设置水解过滤层,水解过滤层的顶端部低于L形过流管的进水口和池壁上的出水口,水解过滤层中填充水解酸化虑料,水解酸化虑料采用粒径1-2cm的陶粒或聚乙烯弹性填粒。 A hydrolysis filter layer is installed in the influent hydrolysis oxidation tank, the hydrolysis oxidation tank and the outlet water hydrolysis oxidation tank. The top of the hydrolysis filter layer is lower than the water inlet of the L-shaped overflow pipe and the water outlet on the pool wall. Acidification material, hydrolysis acidification material adopts ceramsite or polyethylene elastic filler with a particle size of 1-2cm. the
多级水解酸化处理单元是装有水解过滤层的厌氧生物反应器,在滤料表面存有生物膜形态生长的微生物群体,滤料之间的空隙中存留了大量悬浮生长的微生物,清液污水水体通过水解过滤层时,有机物被截留、吸附及代谢分解,最后达到稳定化。同时,进水水解氧化池、水解氧化池和出水水解氧化池配置成密闭的厌氧环境,在厌氧环境中蛋白性有机物通过厌氧发酵而分解,并产生氨等物质,具有杀灭寄生虫卵及病菌的作用。 The multi-stage hydrolytic acidification treatment unit is an anaerobic bioreactor equipped with a hydrolysis filter layer. There are microbial groups growing in the form of biofilm on the surface of the filter material, and a large number of suspended microorganisms are stored in the gaps between the filter materials. When the sewage water passes through the hydrolysis filter layer, the organic matter is intercepted, adsorbed, metabolized and decomposed, and finally stabilized. At the same time, the influent hydrolysis oxidation tank, the hydrolysis oxidation tank and the effluent hydrolysis oxidation tank are configured in a closed anaerobic environment. In the anaerobic environment, proteinaceous organic matter is decomposed through anaerobic fermentation and produces ammonia and other substances, which can kill parasites. The role of eggs and bacteria. the
多级水解酸化处理单元在池壁下部安设进水口,把清液污水水体直接送入进水水解氧化池的水解过滤层实施水解过滤,多级水解酸化处理单元在池壁上部安设出水口,把水解过滤后的污水水体收集并输送到集水池内。进水水解氧化池、水解氧化池和出水水解氧化池的顶部设置检修口,检修口上盖上密封盖,保持进水水解氧化池、水解氧化池和出水水解氧化池处于密闭的环境。 The multi-stage hydrolysis and acidification treatment unit is equipped with a water inlet at the lower part of the pool wall, and the clear liquid sewage water body is directly sent to the hydrolysis filter layer of the influent hydrolysis oxidation tank for hydrolysis and filtration, and the multi-stage hydrolysis and acidification treatment unit is installed with a water outlet at the upper part of the pool wall , to collect and transport the hydrolyzed and filtered sewage water to the sump. An inspection port is provided on the top of the influent hydrolysis oxidation pool, the hydrolysis oxidation pool and the outlet water hydrolysis oxidation pool, and the inspection port is covered with a sealing cover to keep the inflow hydrolysis oxidation pool, the hydrolysis oxidation pool and the outlet water hydrolysis oxidation pool in a closed environment. the
进水水解氧化池、水解氧化池和出水水解氧化池之间的隔板上部安设L形过流管,L形过流管收集经过水解过滤层水解过滤的污水水体,并通过自流 输送到另一个池中的水解过滤层的底部再次实施水解过滤。 An L-shaped overflow pipe is installed on the upper part of the partition between the inlet water hydrolysis oxidation tank, the hydrolysis oxidation tank and the outlet water hydrolysis oxidation tank. The L-shaped overflow pipe collects the sewage water body that has been hydrolyzed and filtered by the hydrolysis filter layer, and transports it to another by gravity. The bottom of the hydrolytic filter layer in the pool is subjected to hydrolytic filtration again. the
进入多级水解酸化处理单元的清液水体的流向自多级水解酸化处理单元一端的进水口利用水体的自重通过L形过流管向多级水解酸化处理单元另一端的出水口顺流流动,在流动的过程中实施水解、氧化、发酵制成无害水体。 The clear liquid water entering the multi-stage hydrolysis acidification treatment unit flows from the water inlet at one end of the multi-stage hydrolysis acidification treatment unit to the water outlet at the other end of the multi-stage hydrolysis acidification treatment unit through the L-shaped flow pipe through the self-weight of the water body. In the process of flowing, hydrolysis, oxidation and fermentation are carried out to make harmless water. the
在污水源中的生活污水含高分子有机物的浓度较多,氮、磷等污染物多以有机氮和有机磷形式存在于水体中,如蛋白质类、尿素、生物细胞体等,不利于后续多级潜流湿地处理单元的快速降解,需要通过厌氧环境把高分子有机物降解为低分子有机物、有机氮降解为无机氮、有机磷降解为无机磷等,提高后续多级潜流湿地处理单元去除污染物的效率。经过水解过滤层的水解过滤后的无害水体漫过水解过滤层,聚集在出水水解氧化池的上部,从出水口自流入集水池。 The domestic sewage in the sewage source contains a high concentration of high-molecular organic matter, and pollutants such as nitrogen and phosphorus mostly exist in the water body in the form of organic nitrogen and organic phosphorus, such as proteins, urea, biological cells, etc., which are not conducive to subsequent multi-purpose The rapid degradation of the subsurface flow wetland treatment unit needs to degrade high molecular weight organic matter into low molecular weight organic matter, organic nitrogen into inorganic nitrogen, and organic phosphorus into inorganic phosphorus through an anaerobic environment, so as to improve the removal of pollutants in subsequent multilevel subsurface flow wetland treatment units. s efficiency. The harmless water after the hydrolysis and filtration of the hydrolysis filter layer overflows the hydrolysis filter layer, gathers in the upper part of the effluent hydrolysis oxidation tank, and flows into the water collection tank from the water outlet. the
曝气增氧处理单元整体呈箱形,曝气增氧处理单元一端的池壁上设置进水口,进水口上的管路设置闸阀,控制进水口的流量,集水出水池中的水解氧化的清液水体通过管路从进水口进入曝气增氧处理单元内。 The aeration and oxygenation treatment unit is in the shape of a box as a whole. The water inlet is set on the wall of the pool at one end of the aeration and oxygenation treatment unit. The pipeline on the water inlet is equipped with a gate valve to control the flow of the water inlet. The clear water enters the aeration and oxygenation treatment unit from the water inlet through the pipeline. the
曝气增氧处理单元另一端的池壁上部设置曝气机,曝气增氧处理单元的池底部沿池底部至少设置1根曝气管,曝气管与主干管相连接,曝气机与主干管端部相连接,主干管上设置控制闸阀,控制曝气管的进气量,曝气机通过主干管和曝气管向曝气增氧处理单元的池内曝气,增加无害水体中溶解氧的含量制成溶氧水体。 An aerator is installed on the upper part of the pool wall at the other end of the aeration and oxygenation treatment unit, and at least one aeration tube is installed along the bottom of the pool of the aeration and aeration treatment unit. The aeration tube is connected to the main pipe, and the aerator and The ends of the main pipe are connected, and a control gate valve is set on the main pipe to control the air intake of the aeration pipe. The content of dissolved oxygen is made into dissolved oxygen water. the
曝气增氧处理单元的一侧的上部设置出水口,出水口上的管路设置闸阀,控制出水口的流量,通过管路与波浪式多级潜流湿地装置的布水管相连接,经过增氧后的溶氧清液水体自流输送到波浪式多级潜流湿地装置内。 The upper part of one side of the aeration and oxygenation processing unit is provided with a water outlet, and the pipeline on the water outlet is provided with a gate valve to control the flow of the water outlet. The final dissolved oxygen clear liquid water body is transported to the wave-type multi-stage subsurface flow wetland device by gravity. the
经过水解过滤后的无害水体的溶解氧含量极低,曝气增氧处理单元就是要增加无害水体中的溶解氧的含量。曝气机通过主干管和曝气管相池中的无害水体实施曝气,增加无害水体的溶解氧的含量制成溶氧水体,为后续多级潜流湿地单元的好氧微生物提供氧源,溶氧水体从曝气增氧处理单元的出水口自流到多级潜流湿地单元。 The dissolved oxygen content of the harmless water body after hydrolysis and filtration is extremely low, and the aeration and oxygenation treatment unit is to increase the dissolved oxygen content in the harmless water body. The aerator performs aeration through the main pipe and the harmless water body in the phase tank of the aeration pipe, increasing the dissolved oxygen content of the harmless water body to make dissolved oxygen water body, providing oxygen source for the aerobic microorganisms in the subsequent multi-stage subsurface flow wetland unit , the dissolved oxygen water flows from the outlet of the aeration and oxygenation treatment unit to the multi-stage subsurface flow wetland unit. the
多级潜流湿地处理单元整体呈箱形,通过隔板分隔成至少4组潜流湿地池,依次排列为进水湿地池、2组分解渗滤湿地池和出水湿地池,进水湿地池与其中一组分解渗滤湿地池之间设置隔板,隔板的顶端部高于分解渗滤层的上表层,隔板的下部设置水平过流管至少1个,隔板的上部设置反冲洗连通口至少1个,反冲洗连通口高于分解渗滤层的表层。出水湿地池与另一组分解渗滤湿地池之间设置隔板,隔板的顶端部高于分解渗滤层的上表层,隔板的下部设置水平过流管至少1个,隔板的上部设置反冲洗连通口至少1个,反冲洗连通口高于分解渗滤层的表层。2组分解渗滤湿地池之间设置隔板,隔板安设在分解渗滤层内,隔板的顶端部低于分解渗滤层,2组分解渗滤湿地池上部的分解渗滤层相连通。多级潜流湿地处理单元一端的池壁上部设置反冲洗排空口,反冲洗排空口将反冲洗分解渗滤层的反冲洗水源和阻塞物一起排出多级潜流湿地处理单元外。 The multi-stage subsurface flow wetland treatment unit is box-shaped as a whole, and is divided into at least 4 groups of subsurface flow wetland pools by partitions, which are arranged in turn as an inlet wetland pool, two groups of decomposing and percolating wetland pools, and an outlet wetland pool. A partition is set between the component decomposition and percolation wetland pools. The top of the partition is higher than the upper surface of the decomposition and percolation layer. The lower part of the partition is provided with at least one horizontal flow pipe, and the upper part of the partition is provided with at least one backwash communication port. One, the backwash connection port is higher than the surface layer of the decomposed percolation layer. A partition is set between the effluent wetland pool and another group of decomposition and infiltration wetland pools. The top of the partition is higher than the upper surface layer of the decomposition and infiltration layer. At least one horizontal flow pipe is installed on the lower part of the partition. There is at least one backwash communication port, and the backwash communication port is higher than the surface layer of the decomposed percolation layer. A partition is set between the two-component decomposing and percolating wetland pools, and the partition is installed in the decomposing and percolating layer. The top of the partition is lower than the decomposing and percolating layer, and the decomposing and percolating layer on the upper part of the two-component decomposing and percolating wetland pools is connected. . The upper part of the pool wall at one end of the multi-stage subsurface flow wetland treatment unit is provided with a backwash emptying port, and the backwash emptying port discharges the backwash water source and obstructions from the backwash decomposed percolation layer to the outside of the multi-stage subsurface flow wetland treatment unit. the
多级潜流湿地单元是由填料基质、水生植物和附着在填料基质及植物根系区的微生物组成,构成独特的“基质-植物-微生物”生态系统。多级潜流湿地处理单元内分为进水湿地池、2组分解渗滤湿地池和出水湿地池,通过隔板和水平过流管设置,营造出溶氧水体在多级潜流湿地处理单元内的分解渗滤层内由表层到底层,再由底层到表层反复流动形成波浪式的流动,实施好氧、厌氧、硝化和反硝化的反应过程。隔板的上部设置反冲洗连通口,多级潜流湿地处理单元一端的池壁上部设置反冲洗排空口,在反冲洗分解渗滤层后,把进水湿地池、2组分解渗滤湿地池和出水湿地池顶部的反冲洗水源和阻塞物排出多级潜流湿地单元。 The multi-level subsurface flow wetland unit is composed of filler matrix, aquatic plants and microorganisms attached to the filler matrix and plant root zone, forming a unique "substrate-plant-microbe" ecosystem. The multi-stage subsurface flow wetland treatment unit is divided into an inflow wetland pool, a 2-component decomposition and percolation wetland pool, and an outlet wetland pool. Through the installation of partitions and horizontal flow pipes, the dissolved oxygen water body in the multi-stage subsurface flow wetland treatment unit is created. The decomposed infiltration layer flows repeatedly from the surface to the bottom layer, and then from the bottom layer to the surface layer to form a wave-like flow, and implements the reaction process of aerobic, anaerobic, nitrification and denitrification. The upper part of the partition is provided with a backwash connection port, and the upper part of the pool wall at one end of the multi-stage subsurface flow wetland treatment unit is provided with a backwash emptying port. and effluent wetland tank top backwash water source and blockage discharge multi-stage subsurface flow wetland unit. the
多级潜流湿地处理单元的池底部设置反冲洗管路至少1个,反冲洗管路埋设在分解渗滤层的底层,反冲洗管路贯穿进水湿地池、2组分解渗滤湿地池和出水湿地池的池底部,反冲洗管路与反冲洗主干管相连接,反冲洗主干管引出池外,反冲洗主干管从池外向反冲洗管路输入反冲洗水源。 At least one backwashing pipeline is installed at the bottom of the pool of the multi-stage subsurface flow wetland treatment unit, and the backwashing pipeline is buried at the bottom of the decomposed percolation layer. At the bottom of the wetland pool, the backwash pipeline is connected to the backwash main pipe, the backwash main pipe leads out of the pool, and the backwash main pipe enters the backwash water source from the outside of the pool to the backwash pipeline. the
当多级潜流湿地处理单元运行一段时间后,分解渗滤层出现阻塞,分解渗滤层中的阻塞物影响分解渗滤层的分解反应,需要对分解渗滤层实施反冲洗。从反冲洗主干管向反冲洗管路注入反冲洗水源,冲洗分解渗滤层,把分解渗滤层中的阻塞物反冲洗到进水湿地池、2组分解渗滤湿地池和出水湿地池的顶部,反冲洗水源和阻塞物通过多级潜流湿地单元上部的反冲洗连通口和反冲洗排空口排出多级潜流湿地单元。 After the multi-stage subsurface flow wetland treatment unit has been in operation for a period of time, the decomposed percolation layer is blocked, and the obstructions in the decomposed percolation layer affect the decomposition reaction of the decomposed percolation layer, so it is necessary to backwash the decomposed percolation layer. Inject the backwashing water source from the main backwashing pipe to the backwashing pipeline, flush the decomposed percolation layer, and backwash the obstructions in the decomposed percolation layer to the inlet wetland pool, the 2-component decomposed percolation wetland pool and the outlet wetland pool At the top, the backwash water source and obstructions are discharged from the multistage subsurface flow wetland unit through the backwash communication port and the backwash emptying port on the upper part of the multistage subsurface flow wetland unit. the
分别在进水湿地池、出水湿地池和2组分解渗滤湿地池内至少设置1个检测观察竖井,检测观察竖井贯穿分解渗滤层,直至池底部,通过检测观察竖井观测池中的水位以及从检测观察井中取水样。 Set up at least one detection and observation shaft in the influent wetland pool, effluent wetland pool and the two-component decomposition and percolation wetland pool respectively. The detection and observation shaft runs through the decomposition and percolation layer to the bottom of the pool. Water samples were taken from the observation well. the
当溶氧水体在多级潜流湿地处理单元中运行过程中,通过检测观察竖井观测进水湿地池、2组分解渗滤湿地池和出水湿地池的运行情况,以及从检测观察竖井中去除水样进行检测水质情况。 When the dissolved oxygen water body is operating in the multi-stage subsurface flow wetland treatment unit, observe the operation of the influent wetland pool, the 2-component decomposition infiltration wetland pool and the effluent wetland pool through the detection and observation shaft, and remove water samples from the detection and observation shaft Check water quality. the
潜流湿地池内设置分解渗滤层,进水湿地池和出水湿地池的分解渗滤层采用粒径2-4cm的砾石,2组分解渗滤湿地池分别采用页岩和陶粒,其中一组分解渗滤湿地池的分解渗滤层采用粒径4-8cm的页岩,另一组分解渗滤湿地池的分解渗滤层采用粒径2-4cm的陶粒。 The decomposing infiltration layer is set in the subsurface flow wetland pool. The decomposing and infiltrating layer of the influent wetland pool and the outflowing wetland pool adopts gravel with a particle size of 2-4cm. The decomposed infiltration layer of the percolation wetland pool uses shale with a particle size of 4-8 cm, and the decomposed percolation layer of the other group of decomposed percolation wetland pools uses ceramsite with a particle size of 2-4 cm. the
分解渗滤层的上表面种植水陆两栖的种植物,种植物的根系扎根在分解渗滤层内,种植物为芦苇、黄花鸢尾、香蒲、再力花、黑三菱,至少种植1种,分解渗滤层的填料基质为微生物提供附着载体,微生物在种植物的根系和填料基质表面形成微生物膜,通过种植物吸收去除水体中的污染物,并随着种植物的收割将污染物移出多级潜流湿地处理单元,溶氧水体在流动的过程中流经进水湿地池、2组分解渗滤湿地池和出水湿地池分解渗滤层的表层和底层制成排放水体。 Plant amphibious species on the upper surface of the decomposed percolation layer. The roots of the plants are rooted in the decomposed percolation layer. The species of plants are reed, yellow iris, cattail, Zaili flower, and black Mitsubishi. At least one species is planted. The filler matrix of the filter layer provides an attachment carrier for microorganisms. The microorganisms form a microbial film on the root system of the plant and the surface of the filler matrix, absorb and remove pollutants in the water body through the plant, and move the pollutant out of the multi-level subsurface flow as the plant is harvested. In the wetland treatment unit, the dissolved oxygen water flows through the inflow wetland pool, the 2-component decomposition and infiltration wetland pool, and the outlet wetland pool to decompose the surface and bottom layers of the percolation layer to make discharge water. the
多级潜流湿地处理单元的分解渗滤层设置在进水湿地池、2组分解渗滤湿地池和出水湿地池中,进水湿地池、2组分解渗滤湿地池和出水湿地池的分解渗滤层分别采用不同的填料基质,在分解渗滤层的表层上种植种植物,种植 物的根系扎根在分解渗滤层的表层内,构成植物根区。植物的根系和填料基质为微生物提供附着的载体,植物根系又为微生物提供氧源,在靠近植物根区的分解渗滤层的区域形成好氧区,在远离植物根区的分解渗滤层的区域形成厌氧区或兼氧区。本实用新型的多级潜流湿地处理单元与自然湿地相比,水流在填料基质的表层下流动,不易滋生蚊蝇,填料基质的表面种植物,水质净化能力强,景观效果好。 The decomposition and infiltration layer of the multi-stage subsurface flow wetland treatment unit is set in the inflow wetland pool, the 2-component decomposition and infiltration wetland pool and the effluent wetland pool. The filter layer adopts different filler substrates, plants are planted on the surface of the decomposed percolation layer, and the roots of the plants take root in the surface layer of the decomposed percolation layer to form the plant root zone. The root system of the plant and the filler matrix provide the carrier for the microorganisms to attach to, and the plant root system provides the oxygen source for the microorganisms, forming an aerobic zone in the area of the decomposed infiltration layer near the plant root zone, and forming an aerobic zone in the area of the decomposed infiltration layer far away from the plant root zone. Zones form anaerobic or facultative zones. Compared with the natural wetland, the multi-stage subsurface flow wetland treatment unit of the utility model has water flowing under the surface of the filler matrix, which is not easy to breed mosquitoes and flies. Plants are planted on the surface of the filler matrix, and the water purification ability is strong and the landscape effect is good. the
多级潜流湿地处理单元一端的池壁上部沿池壁安设收水管,收水管安设在分解渗滤层内,收水管的一端与蓄积排放池的进水口相连接,收水管的出水端部设置闸阀,控制排出的水量,收水管把收集的水体输入到蓄积排放池内。 On the upper part of the pool wall at one end of the multi-stage subsurface flow wetland treatment unit, a water collection pipe is installed along the pool wall, and the water collection pipe is installed in the decomposing seepage layer. A gate valve is set to control the amount of discharged water, and the water collection pipe inputs the collected water body into the storage and discharge tank. the
多级潜流湿地处理单元另一端的池壁上部沿池壁设置布水管,布水管安设在分解渗滤层内,布水管的一端与曝气增氧处理单元的出水口相连接,布水管的进水端部设置闸阀,控制进水量,把经过曝气增氧处理单元溶氧后的水体均匀的流出撒布在进水湿地池的分解渗滤层内。 The upper part of the pool wall at the other end of the multi-stage subsurface flow wetland treatment unit is provided with water distribution pipes along the pool wall. The water distribution pipes are installed in the decomposition and infiltration layer. A gate valve is set at the water inlet to control the water inlet, and evenly distribute the water after the oxygen dissolved in the aeration and oxygenation treatment unit into the decomposition and percolation layer of the inlet wetland pool. the
本实用新型的多级潜流湿地处理单元中进水湿地池、2组分解渗滤湿地池和出水湿地池的结构实现水体波浪式流动,从布水管撒布在进水湿地池一端的分解渗滤层的上部,水体流经进水湿地池、2组分解渗滤湿地池和出水湿地池形成表层到底层,底层又到表层的流动,最后安设在多级潜流湿地处理单元另一端的收水管在分解渗滤层的上部收集处理过的水体。与自然湿地相比,本实用新型在相同面积条件下处理能力大幅度提高,能够克服天然湿地比较脆弱的缺点,具有负荷率高、占地面积小、效果可靠、耐冲击负荷等优点,而且水流在填料表层以下流动,不易滋生蚊蝇。湿地表面种植水质净化能力强、景观效果好的水生植物,在净化水质的同时,起到良好的景观效果。 In the multi-stage subsurface flow wetland treatment unit of the utility model, the structure of the inlet wetland pool, the two-component decomposition and percolation wetland pool and the outlet wetland pool realizes the wave-like flow of the water body, and spreads the decomposition and percolation layer at one end of the water inlet wetland pool from the water distribution pipe In the upper part, the water flows through the influent wetland pool, the 2-component decomposition and infiltration wetland pool and the effluent wetland pool to form a flow from the surface layer to the bottom layer, and from the bottom layer to the surface layer. Finally, the water collection pipe installed at the other end of the multi-stage subsurface flow wetland treatment unit is The upper part of the disintegrated percolation layer collects the treated water body. Compared with natural wetlands, the utility model has greatly improved processing capacity under the same area conditions, can overcome the relatively fragile shortcomings of natural wetlands, and has the advantages of high load rate, small footprint, reliable effect, impact load resistance, etc., and the water flow It flows below the surface of the filler, so it is not easy to breed mosquitoes and flies. Aquatic plants with strong water purification ability and good landscape effect are planted on the surface of the wetland, which can purify the water quality and have a good landscape effect at the same time. the
检修放空管与进水湿地池、2组分解渗滤湿地池和出水湿地池相贯通,溶氧清液水体进入多级潜流湿地处理单元的流向是从布水管进入进水湿地池,利用水体的自重流经2组分解渗滤湿地池进入出水湿地池,由收水管收起输入到排放蓄积池内,溶氧水体在流动的过程中实现反复经过好氧、厌氧、硝化和反硝化的反应过程制成排放水体。 The maintenance vent pipe is connected with the inlet wetland pool, the 2-component decomposition and percolation wetland pool, and the outlet wetland pool. The flow direction of the dissolved oxygen clear water into the multi-stage subsurface flow wetland treatment unit is from the water distribution pipe into the water inlet wetland pool. The self-weight flows through the 2-component decomposition and infiltration wetland pool into the effluent wetland pool, and is collected by the water collection pipe and input into the discharge storage tank. The dissolved oxygen water body undergoes repeated aerobic, anaerobic, nitrification and denitrification reactions during the flow process The process makes the discharge water body. the
溶氧清液水体进入多级潜流湿地处理单元的流向是从布水管进入进水湿地池,利用水体的自重流经2组分解渗滤湿地池进入出水湿地池,由收水管收起输入到排放蓄积池内,溶氧水体在流动的过程中实现反复经过好氧、厌氧、硝化和反硝化的反应过程制成排放水体。 The flow direction of the dissolved oxygen clear liquid water entering the multi-stage submerged flow wetland treatment unit is from the water distribution pipe into the water inlet wetland pool, and uses the self-weight of the water body to flow through the 2-component decomposition and percolation wetland pool into the outlet wetland pool, and is collected by the water collection pipe and input to the discharge In the storage tank, the oxygen-dissolved water body undergoes repeated aerobic, anaerobic, nitrification and denitrification reaction processes in the process of flowing to produce a discharge water body. the
本实用新型实现水体波浪式流动的结构导致水体从表层到底层,又从底层到表层的流动,水体反复经过好氧、厌氧、硝化和反硝化的过程,实现高效去除水体中的有机污染物和氮磷。 The structure of the utility model to realize the wave-like flow of the water body leads to the flow of the water body from the surface layer to the bottom layer, and from the bottom layer to the surface layer, and the water body repeatedly undergoes the process of aerobic, anaerobic, nitrification and denitrification, so as to realize efficient removal of organic pollutants in the water body and nitrogen and phosphorus. the
多级水解酸化处理单元另一端部的池壁外设置集水出水池,集水出水池整体呈箱形,集水出水池与多级水解酸化处理单元另一端部的池壁相连接,多级水解酸化处理单元的出水口与集水出水池贯通,集水出水池的另一侧的池壁上部设置出水口,集水出水池内底部安设潜水泵,潜水泵通过管路穿过 出水口把水解氧化的清液水体提升,输送到曝气增氧处理单元内。 A water collection and outlet pool is arranged outside the pool wall at the other end of the multi-stage hydrolysis acidification treatment unit. The water collection and outlet pool is in the shape of a box as a whole. The water outlet of the hydrolysis and acidification treatment unit is connected with the water collection and outlet pool. The water outlet is set on the upper part of the pool wall on the other side of the water collection and outlet pool. A submersible pump is installed at the bottom of the water collection and outlet pool. The hydrolyzed and oxidized clear liquid water body is lifted and transported to the aeration and oxygenation treatment unit. the
在多级水解酸化处理单元内经过水解过滤层实施水解过滤后的无害水体从出水口流入集水池内蓄积起来,安设在集水池内的潜水泵通过管路把无害水体提升到曝气增氧处理单元内实施曝气增氧处理,把无害水体的水位提高,实现曝气增氧处理单元与多级潜流湿地单元产生落差,曝气增氧处理单元的水体自流到多级潜流湿地单元内。 In the multi-stage hydrolytic acidification treatment unit, the harmless water after hydrolysis and filtration through the hydrolysis filter layer flows into the sump from the water outlet and accumulates. The submersible pump installed in the sump lifts the harmless water to aeration through the pipeline. Aeration and oxygenation treatment is implemented in the aeration treatment unit to increase the water level of the harmless water body, to realize the drop between the aeration and aeration treatment unit and the multi-level subsurface flow wetland unit, and the water body of the aeration and aeration treatment unit flows to the multi-level subsurface flow wetland by itself within the unit. the
多级潜流湿地处理单元的一端的一侧设置蓄积排放池,蓄积排放池整体呈箱形,蓄积排放池的池壁与多级潜流湿地处理单元的出水湿地池的池壁相连接,与出水湿地池相邻的蓄积排放池的池壁上设置进水口,蓄积排放池的进水口与出水湿地池的收水管相连通,蓄积排放池一端的池壁上设置排放管,把经过处理后的排放水体通过排放管排放到河道或湖泊。 One side of one end of the multi-stage subsurface flow wetland treatment unit is provided with an accumulation and discharge pond, the accumulation and discharge pond is box-shaped as a whole, and the pool wall of the accumulation and discharge pond is connected with the pool wall of the outlet wetland pool of the multi-stage subsurface flow wetland treatment unit, and is connected with the outlet wetland A water inlet is set on the wall of the accumulation and discharge pond adjacent to the pool, and the water inlet of the accumulation and discharge pond is connected with the water collection pipe of the outlet wetland pool. Discharge to rivers or lakes through discharge pipes. the
在多级潜流湿地处理单元的一端的一侧配置蓄积排放池,把多级潜流湿地处理单元处理完的排放水体蓄积到蓄积排放池内,蓄积到适当的蓄积量等待排放时机,排放到河道或湖泊。 A storage and discharge pond is arranged on one side of one end of the multi-level subsurface flow wetland treatment unit, and the discharged water treated by the multi-level subsurface flow wetland treatment unit is stored in the storage and discharge pond, and accumulated to an appropriate storage volume to wait for the discharge opportunity, and then discharged to rivers or lakes . the
多级潜流湿地处理单元一侧的中部设置检修放空控制井,检修放空控制井整体呈箱形,检修放空控制井内设置放空管,放空管贯穿检修放空控制井的一侧井壁,在多级潜流湿地处理单元的进水湿地池、2组分解渗滤湿地池和出水湿地池一侧底部设置检修放空管,检修放空管与进水湿地池、2组分解渗滤湿地池和出水湿地池相贯通,检修放空管与检修放空控制井内的放空管相连接并贯通,检修放空管上设置控制闸阀构成检修放空管路,通过检修放空管路放空进水湿地池、2组分解渗滤湿地池和出水湿地池检修多级潜流湿地处理单元。 In the middle of one side of the multi-stage subsurface flow wetland treatment unit, an inspection and maintenance venting control well is set. The bottom of one side of the inlet wetland pool, the 2-component decomposition and infiltration wetland pool and the outlet wetland pool of the subsurface flow wetland treatment unit is provided with a maintenance vent pipe, and the maintenance vent pipe is connected with the water inlet wetland pool, the 2-component decomposition and infiltration wetland pool and the outlet water The wetland pools are interconnected, and the maintenance venting pipe is connected and connected with the venting pipe in the maintenance venting control well. A control gate valve is set on the maintenance venting pipe to form a maintenance venting pipeline, and the inlet wetland pool, 2-component decomposition infiltration wetland pool and effluent wetland pool maintenance multi-stage subsurface flow wetland treatment unit. the
当多级潜流湿地处理单元运行一段时间后,对多级潜流湿地处理单元实施检修,首先要排空多级潜流湿地处理单元内的水体,然后实施检修,在多级潜流湿地处理单元的侧面安设检修放空控制井,多级潜流湿地处理单元的进水湿地池、2组分解渗滤湿地池和出水湿地池一侧底部配置检修放空管,检修放空管连接到检修放空控制井内的放空管,从放空管排放进水湿地池、2组分解渗滤湿地池和出水湿地池内的水体,对多级潜流湿地处理单元实施检修。 After the multi-level subsurface flow wetland treatment unit has been in operation for a period of time, the multi-level subsurface flow wetland treatment unit needs to be overhauled. An inspection and venting control well is set up, and the bottom of one side of the inlet wetland pool, the 2-component decomposition infiltration wetland pool and the outlet wetland pool of the multi-stage subsurface flow wetland treatment unit is equipped with an inspection and venting pipe, and the inspection and venting pipe is connected to the vent in the inspection and venting control well. The empty pipe discharges the water in the inlet wetland pool, the 2-component decomposition infiltration wetland pool and the outlet wetland pool from the empty pipe, and performs maintenance on the multi-stage subsurface flow wetland treatment unit. the
污水源通过管路从多级沉淀预处理单元的沉淀分解池的进污口进入沉淀分解池内,污水源中夹带着一定量的悬浮物、漂浮物和泥沙,污水源所含杂质的比重不同,污水源进入沉淀分解池后形成上浮的浮渣、中层的污水水体和下沉的沉渣,沉淀分解池的密闭构成厌氧环境,污水源含有的蛋白性有机物通过厌氧发酵而分解,并产生氨等物质,杀灭寄生虫卵及病菌,实现沉淀、分解、发酵、灭菌污水处理,由于水体重力的作用沉淀分解池内的中层污水水体从设置在隔墙中部的过流管的入口进入过流管,从高于过流管的出口自流进入发酵沉淀池内。 The sewage source enters the sedimentation and decomposition tank from the sewage inlet of the sedimentation and decomposition tank of the multi-stage sedimentation pretreatment unit through the pipeline. The sewage source contains a certain amount of suspended matter, floating matter and sediment, and the proportion of impurities contained in the sewage source is different. After the sewage source enters the sedimentation and decomposition tank, it forms floating scum, middle sewage water and sinking sediment. The sealing of the sedimentation and decomposition tank forms an anaerobic environment. The proteinaceous organic matter contained in the sewage source is decomposed by anaerobic fermentation and produces Ammonia and other substances can kill parasite eggs and germs, realize sedimentation, decomposition, fermentation, and sterilized sewage treatment. Due to the action of water gravity, the middle-level sewage water in the sedimentation decomposition tank enters from the entrance of the overflow pipe set in the middle of the partition wall. The overflow pipe flows into the fermentation sedimentation tank from the outlet higher than the overflow pipe. the
污水源中含有悬浮物、漂浮物和泥沙类,污水源包括生活污水和养殖废水。生活污水和养殖废水中夹带着粪便,直接进入后续污水处理单元,会后续污水处理单元,影响后续污水处理单元的正常运行,本实用新型的 多级污水与处理单元拦截无水源中夹带的有悬浮物、漂浮物和泥沙类,把粪便的收集、无害化处理、水量调节和沉淀在多级沉淀预处理单元顺流实施预处理。 The sewage source contains suspended matter, floating matter and sediment, and the sewage source includes domestic sewage and aquaculture wastewater. Feces are entrained in domestic sewage and aquaculture wastewater, and directly enter the subsequent sewage treatment unit, which will affect the subsequent sewage treatment unit and affect the normal operation of the subsequent sewage treatment unit. The collection of feces, harmless treatment, water volume regulation and sedimentation are carried out downstream in the multi-stage sedimentation pretreatment unit. the
沉淀分解池主要截留含虫卵较多的粪便,松散的粪块因发酵膨胀产生上浮,比重较大的则下沉,形成上层为上浮的粪皮,中层为粪液,下层为下沉的粪渣,其中寄生虫的比重较大亦沉入池底。沉淀分解池营造出密闭厌氧环境,通过厌氧发酵和分解蛋白性有机物,并产生氨等物质,具有杀灭寄生虫卵和病菌的作用。 The sedimentation and decomposition tank mainly intercepts feces containing more insect eggs. The loose feces float up due to fermentation and expansion, and the larger specific gravity sinks to form the upper layer of floating feces skin, the middle layer of feces liquid, and the lower layer of sinking feces. The slag, in which the proportion of parasites is relatively large, also sinks to the bottom of the pool. The sedimentation and decomposition tank creates a closed anaerobic environment, through anaerobic fermentation and decomposition of proteinaceous organic matter, and produces ammonia and other substances, which can kill parasite eggs and germs. the
进入发酵沉淀池内的污水水体进一步的发酵、沉淀,发酵沉淀池与沉淀分解池相比浮渣和悬浮物的数量相对减少,污水水体处于比较静止状态,发酵和分解的程度较低,有利于污水水体中的浮渣和悬浮物继续实现发酵、分解和沉淀,污水水体又经发酵、沉淀后由于水体重力的作用发酵沉淀池内中层的污水液从设置在隔墙中部的过流管的入口进入过流管,从高于过流管的出口自流进入蓄积池内。 The sewage water entering the fermentation and sedimentation tank is further fermented and precipitated. Compared with the sedimentation and decomposition tank, the amount of scum and suspended matter in the fermentation and sedimentation tank is relatively reduced. The sewage water is in a relatively static state, and the degree of fermentation and decomposition is low, which is conducive to sewage The scum and suspended solids in the water body continue to ferment, decompose and settle, and the sewage water body is fermented and settled. Due to the action of water gravity, the sewage liquid in the middle layer of the fermentation sedimentation tank enters from the entrance of the overflow pipe set in the middle of the partition wall. The overflow pipe flows into the accumulator from the outlet higher than the overflow pipe. the
发酵沉淀池的作用是进一步发酵、沉淀,与沉淀分解池相比,进入发酵沉淀池的粪皮和粪渣的数量相对减少,发酵分解的程度较低,没有新粪便的进入,故此发酵沉淀池处于比较静止状态,有利于漂浮在粪池中的虫卵继续向池底沉淀。 The function of the fermentation and sedimentation tank is to further ferment and settle. Compared with the sedimentation and decomposition tank, the amount of feces and dung entering the fermentation and sedimentation tank is relatively reduced, the degree of fermentation and decomposition is low, and no new feces enter. Therefore, the fermentation and sedimentation tank It is in a relatively static state, which is conducive to the worm eggs floating in the septic tank to continue to settle to the bottom of the tank. the
进入蓄积池内的污水液再进一步的分离和沉淀,存储在蓄积池内污水液中层以上清液,残余的浮渣和悬浮物沉入池底,随着污水液不断的进入蓄积池,蓄积池的污水液的水位也不断升高,污水液的上层清液从安设在池壁上部的出水口通过管道自流到多级水解氧化单元,从多级水解氧化单元的池壁下部的进水口进入多级水解氧化单元内,污水源经过多级沉淀预处理单元的多级处理去除浮渣、悬浮物和沉渣,通过发酵、分解、沉淀和储存杀灭寄生虫卵、病原微生物和细菌,达到了无害化的设计要求,污水源经过多级沉淀预处理单元预处理制成污水清液,污水清液进入多级水解酸化处理单元。 The sewage liquid entering the storage tank is further separated and precipitated, and the supernatant liquid is stored in the middle layer of the sewage liquid in the storage tank, and the remaining scum and suspended matter sink to the bottom of the tank. As the sewage liquid continuously enters the storage tank, the sewage in the storage tank The water level of the sewage liquid is also rising continuously, and the supernatant liquid of the sewage liquid flows from the outlet installed on the upper part of the pool wall to the multi-stage hydrolysis oxidation unit through the pipeline, and enters the multi-stage hydrolysis oxidation unit from the water inlet at the lower part of the pool wall of the multi-stage hydrolysis oxidation unit. In the hydrolysis oxidation unit, the sewage source undergoes multi-stage treatment of the multi-stage sedimentation pretreatment unit to remove scum, suspended matter and sediment, and kills parasite eggs, pathogenic microorganisms and bacteria through fermentation, decomposition, precipitation and storage, achieving harmless According to the design requirements of the system, the sewage source is pretreated by a multi-stage sedimentation pretreatment unit to make a sewage clear liquid, and the sewage clear liquid enters a multi-stage hydrolysis acidification treatment unit. the
蓄积池的作用主要是储存污水清液,经过沉淀分解池和发酵沉淀池处理后的污水源进入蓄积池,基本上清除悬浮物、漂浮物和泥沙类物质,以及杀灭寄生虫卵和病原微生物,制成污水清液,达到无害化要求。污水源经过沉淀分解池、发酵沉淀池处理和蓄积池的发酵、分解、沉淀和储存,清除悬浮物、漂浮物和泥沙类,杀灭虫卵及细菌的作用,蓄积池内中、上层的污水清液进入多级水解氧化单元。 The function of the storage tank is mainly to store the sewage clear liquid, and the sewage source after the treatment of the sedimentation and decomposition tank and the fermentation sedimentation tank enters the storage tank, basically removes suspended solids, floating solids and sediment substances, and kills parasite eggs and pathogens Microorganisms are made into sewage clear liquid to meet the requirements of harmlessness. The sewage source is treated by the sedimentation and decomposition tank, the fermentation sedimentation tank and the fermentation, decomposition, sedimentation and storage of the storage tank to remove suspended solids, floating objects and sediments, and to kill insect eggs and bacteria. The middle and upper layers of sewage in the storage tank The supernatant enters the multi-stage hydrolysis oxidation unit. the
多级水解酸化处理单元由隔板分隔成至少3个空间,分为进水水解氧化池、水解氧化池和出水水解氧化池,隔板的上部安设L形过水管,进水水解氧化池、水解氧化池和出水水解氧化池中安设水解过滤层,水解过滤层的水解滤料的表面附着生物膜形态生长的微生物群体。 The multi-stage hydrolytic acidification treatment unit is divided into at least 3 spaces by partitions, which are divided into water inlet hydrolysis oxidation pool, hydrolysis oxidation pool and outlet water hydrolysis oxidation pool. A hydrolysis filter layer is installed in the hydrolysis oxidation pool and the effluent hydrolysis oxidation pool, and the surface of the hydrolysis filter material of the hydrolysis filter layer is attached with microbial groups growing in the form of a biofilm. the
无水源中的生活污水的高分子有机物浓度较多,且氮、磷等污染物多以有机氮和有机磷形式存在于水体中,如蛋白质类、尿素、生物细胞体等,在后续多级潜流湿地单元处理时不利于快速降解,需要通过在厌氧环境中将高 分子有机物降解为低分子有机物、有机氮降解为无机氮、有机磷降解为无机磷等,提高多级潜流湿地单元去除污染物的效率。 The concentration of polymeric organic matter in the domestic sewage in the non-water source is relatively high, and pollutants such as nitrogen and phosphorus mostly exist in the water body in the form of organic nitrogen and organic phosphorus, such as proteins, urea, biological cells, etc., in the subsequent multi-level subsurface flow The treatment of wetland units is not conducive to rapid degradation. It is necessary to degrade high-molecular organic matter into low-molecular organic matter, organic nitrogen into inorganic nitrogen, and organic phosphorus into inorganic phosphorus in an anaerobic environment to improve the removal of pollutants in multi-stage subsurface flow wetland units. s efficiency. the
污水清液从多级水解酸化处理单元底部的进水口进入进水水解氧化池的水解过滤层底部,随着污水清液的不断流入进水水解氧化池的水解过滤层内,水解过滤层内污水清液的水位不断提升,污水清液的水位漫过进水水解氧化池的水解过滤层,上升到进水水解氧化池的上部,达到安设在隔板上部的L形过流管的出水口,污水清液经过进水水解氧化池的水解过滤层的水解氧化后,通过L形过流管从进水水解氧化池进入水解氧化池的水解过滤层的底部。 The sewage clear liquid enters the bottom of the hydrolysis filter layer of the influent hydrolysis oxidation tank from the water inlet at the bottom of the multi-stage hydrolysis acidification treatment unit. The water level of the clear liquid continues to rise, and the water level of the sewage clear liquid overflows the hydrolysis filter layer of the influent hydrolysis oxidation tank, rises to the upper part of the influent hydrolysis oxidation tank, and reaches the outlet of the L-shaped overflow pipe installed on the upper part of the partition After the sewage clear liquid is hydrolyzed and oxidized by the hydrolytic filter layer of the influent hydrolytic oxidation tank, it enters the bottom of the hydrolytic filter layer of the hydrolytic oxidation tank from the influent hydrolytic oxidation tank through the L-shaped overflow pipe. the
随着污水清液的不断流入水解氧化池的水解过滤层内,水解过滤层内污水清液的水位不断提升,污水清液的水位漫过水解氧化池的水解过滤层,上升到水解氧化池的上部,达到安设在隔板上部的L形过流管的出水口,污水清液再次经过水解氧化池的水解过滤层的水解氧化后,通过L形过流管从水解氧化池进入出水水解氧化池的水解过滤层的底部。 As the sewage clear liquid continues to flow into the hydrolysis filter layer of the hydrolysis oxidation tank, the water level of the sewage clear liquid in the hydrolysis filter layer continues to rise, and the water level of the sewage clear liquid overflows the hydrolysis filter layer of the hydrolysis oxidation tank and rises to the water level of the hydrolysis oxidation tank The upper part reaches the outlet of the L-shaped overcurrent pipe installed on the upper part of the partition. After the sewage clear liquid is hydrolyzed and oxidized by the hydrolysis filter layer of the hydrolysis oxidation tank again, it enters the effluent hydrolysis oxidation from the hydrolysis oxidation tank through the L-shaped overcurrent pipe. The bottom of the pool's hydrolyzed filter layer. the
随着污水清液的不断流入出水水解氧化池的水解过滤层内,水解过滤层内污水清液的水位不断提升,污水清液的水位漫过出水水解氧化池的水解过滤层,上升到出水水解氧化池的上部,达到安设在多级水解酸化处理单元的池壁上部的出水口,污水清液再一次经过出水水解氧化池的水解过滤层的水解氧化后,通过池壁上部的出水口进入集水出水池,污水清液通过多级水解酸化处理单元的水解过滤层,在流经水解过滤层的过程中水解滤料的表面附着的微生物群体截留、吸附及代谢分解污水清液中的有机物,同时,多级水解酸化处理单元形成的密闭厌氧环境,对蛋白性有机物实施厌氧发酵,分解蛋白性有机物并产生氨等物质,起到杀灭寄生虫卵及病菌的作用,将高分子有机物降解为低分子有机物,有机氮降解为无机氮、有机磷降解为无机磷,有利于后续多级潜流湿地处理单元的快速降解,提高湿地处理对污染物的去除效率。 As the sewage clear liquid continues to flow into the hydrolysis filter layer of the effluent hydrolysis oxidation tank, the water level of the sewage clear liquid in the hydrolysis filter layer continues to rise, and the water level of the sewage clear liquid overflows the hydrolysis filter layer of the effluent hydrolysis oxidation tank and rises to the effluent hydrolysis The upper part of the oxidation tank reaches the water outlet installed on the upper part of the pool wall of the multi-stage hydrolysis acidification treatment unit. When the water is collected and discharged from the pool, the sewage clear liquid passes through the hydrolysis filter layer of the multi-stage hydrolysis acidification treatment unit. During the process of flowing through the hydrolysis filter layer, the microbial groups attached to the surface of the hydrolysis filter material intercept, absorb and metabolize the organic matter in the sewage clear liquid At the same time, the closed anaerobic environment formed by the multi-stage hydrolysis and acidification treatment unit implements anaerobic fermentation on the proteinaceous organic matter, decomposes the proteinaceous organic matter and produces ammonia and other substances, which plays the role of killing parasite eggs and germs. The degradation of organic matter into low-molecular organic matter, organic nitrogen into inorganic nitrogen, and organic phosphorus into inorganic phosphorus is conducive to the rapid degradation of subsequent multi-stage subsurface flow wetland treatment units and improves the removal efficiency of wetland treatment for pollutants. the
多级水解氧化单元是配置水解过滤层的厌氧生物反应器,在水解过滤层的基质滤料的表面附着生物膜形态生长的微生物群体,基质滤料间的空隙中截留了大量悬浮生长的微生物,污水水体通过水解过滤层时,有机物被截留,吸附和代谢分解,最终达到稳定化。多级水解氧化单元是营造密闭厌氧环境,蛋白性有机物通过厌氧发酵得到分解,并产生氨等物质,具有杀灭寄生虫卵及病菌的作用。 The multi-stage hydrolysis oxidation unit is an anaerobic bioreactor equipped with a hydrolysis filter layer. On the surface of the matrix filter material of the hydrolysis filter layer, a microbial population growing in the form of a biofilm is attached, and a large number of suspended microorganisms are trapped in the gaps between the matrix filter materials. , When the sewage water passes through the hydrolysis filter layer, the organic matter is intercepted, adsorbed and metabolized, and finally stabilized. The multi-stage hydrolysis and oxidation unit is to create a closed anaerobic environment. Protein organic matter is decomposed through anaerobic fermentation, and ammonia and other substances are produced, which can kill parasite eggs and bacteria. the
污水清液经过多级水解酸化处理单元的水解氧化处理制成无害水体,无害水体蓄积在集水出水池内,随着无害水体的不断蓄积,安设在集水出水池内的潜水泵通过管路把无害水体提升输送到曝气增氧处理单元内。 The sewage clear liquid is hydrolyzed and oxidized by the multi-stage hydrolysis and acidification treatment unit to make harmless water. The harmless water is accumulated in the water collection outlet pool. The pipeline lifts the harmless water body to the aeration and oxygenation treatment unit. the
无害水体从曝气增氧处理单元的进水口进入到曝气增氧处理单元内,曝气增氧处理单元的曝气机通过主干管和曝气管对无害水体实施曝气增氧处理制成溶氧水体,对无害水体实施曝气增氧处理是无害水体中的溶解氧含量,为多级潜流湿地处理单元内的好氧微生物提供氧源。 The harmless water enters the aeration and oxygenation treatment unit from the water inlet of the aeration and oxygenation treatment unit, and the aerator of the aeration and oxygenation treatment unit performs aeration and oxygenation treatment on the harmless water body through the main pipe and the aeration pipe Make dissolved oxygen water body, implement aeration and oxygenation treatment on harmless water body to reduce the dissolved oxygen content in harmless water body, and provide oxygen source for aerobic microorganisms in the multi-stage subsurface flow wetland treatment unit. the
经多级水解氧化单元水解氧化后,水体中溶解氧的含量极低,曝气增氧 处理单元的主要作用是快速提高污水水体中的溶解氧的含量,为后续多级潜流湿地单元内的好氧微生物提供氧源。 After hydrolysis and oxidation by the multi-stage hydrolysis oxidation unit, the content of dissolved oxygen in the water body is extremely low. The main function of the aeration and oxygenation treatment unit is to quickly increase the content of dissolved oxygen in the sewage water body, which is good for the subsequent multi-stage subsurface flow wetland unit. Aerobic microorganisms provide a source of oxygen. the
随着曝气增氧处理单元内溶氧水体的不断增加,溶氧水体从出水口通过管路自流进入多级潜流湿地处理单元的布水管,布水管均匀的把溶氧水体撒布在多级潜流湿地处理单元的进水湿地池的分解渗滤层内,随着溶氧水体的水体重力作用充满进水湿地池的分解渗滤层,进水湿地池内的水位不断升高,溶氧水体从隔板下部的水平过流管进入其中一组分解渗滤湿地池内的底部,溶氧水体不断的涌入其中一组分解渗滤湿地池并充满另一组分解渗滤湿地池。 With the continuous increase of dissolved oxygen water in the aeration and oxygenation treatment unit, the dissolved oxygen water flows from the outlet through the pipeline into the water distribution pipe of the multi-level subsurface flow wetland treatment unit, and the water distribution pipe evenly spreads the dissolved oxygen water in the multi-level subsurface flow In the decomposed percolation layer of the influent wetland pool of the wetland treatment unit, as the water gravity of the dissolved oxygen water body fills the decomposed percolation layer of the influent wetland pool, the water level in the influent wetland pool continues to rise, and the dissolved oxygen water body from The horizontal flow pipe at the lower part of the partition enters the bottom of one set of decomposition and infiltration wetland pools, and dissolved oxygen water continuously flows into one set of decomposition and infiltration wetland pools and fills the other set of decomposition and infiltration wetland pools. the
多级潜流湿地单元是由基质滤料、水生植物以及分解渗滤层中附着在植物根区的微生物组成,营造出一种独特的“基质滤料-种植物-微生物”生态系统。多级潜流湿地单元的结构是波浪式流动的潜流湿地,种植物的根系扎根在分解渗滤层的表层,种植物根系和基质滤料为微生物提供附着的载体,种植物的根系又为微生物提供氧源。在靠近根区的分解渗滤层形成好氧区,在远离根区的分解渗滤层形成厌氧或兼氧区,溶氧水体从分解渗滤层的上表层流到分解渗滤层的底层,再从分解渗滤层的底层流到分解渗滤层的上表层,不断往复,溶氧水体在多级潜流湿地单元内波浪式流动,反复经过好氧、厌氧、硝化和反硝化的反应过程,实现高效去除有机污染物和氮磷。 The multi-level subsurface wetland unit is composed of matrix filter material, aquatic plants, and microorganisms attached to the plant root zone in the decomposed infiltration layer, creating a unique "matrix filter material-plant-microbe" ecosystem. The structure of the multi-level subsurface wetland unit is a subsurface wetland with wave-like flow. The root system of the plant takes root in the surface layer of the decomposed infiltration layer. oxygen source. The aerobic zone is formed in the decomposed percolation layer near the root zone, and the anaerobic or facultative zone is formed in the decomposed percolation layer far from the root zone, and the dissolved oxygen water flows from the upper surface layer of the decomposed percolation layer to the bottom layer of the decomposed percolation layer , and then flow from the bottom of the decomposed percolation layer to the upper surface of the decomposed percolation layer, continuously reciprocating, the dissolved oxygen water flows in waves in the multi-level subsurface flow wetland unit, and repeatedly undergoes aerobic, anaerobic, nitrification and denitrification reactions process to achieve efficient removal of organic pollutants and nitrogen and phosphorus. the
溶氧水体充满其中一组分解渗滤湿地池的分解渗滤层,其中一组分解渗滤湿地池内的水位不断升高,随着溶氧水体的水位升高并漫过隔板的顶端,溶氧水体从隔板顶端进入另一组分解渗滤湿地池,溶氧水体的不断流入充满另一组分解渗滤湿地池的分解渗滤层,另一组分解渗滤湿地池内的水位不断升高,随着溶氧水体的水体重力作用从隔板下部的水平过流管进入出水湿地池的分解渗滤层内,溶氧水体不断的涌入出水湿地池的分解渗滤层并充满出水湿地池,出水湿地池内的水位不断升高,随着溶氧水体的水位升高达到收水管的位置。 The dissolved oxygen water body is filled with the decomposed percolation layer of one group of decomposed percolation wetland pools, and the water level in one of the decomposed percolation wetland pools is continuously rising. From the top of the clapboard into another group of decomposition and infiltration wetland pools, the dissolved oxygen water continuously flows into the decomposition and infiltration layer of another group of decomposition and infiltration wetland pools, and the water level in the other group of decomposition and infiltration wetland pools continues to rise. Due to the water gravity of the dissolved oxygen water body, the horizontal flow pipe at the lower part of the partition enters the decomposition and percolation layer of the outlet wetland pool, and the dissolved oxygen water continuously flows into the decomposition and percolation layer of the outlet wetland pool and fills the outlet wetland pool. The water level in the effluent wetland pool continues to rise, and reaches the position of the water collection pipe as the water level of the dissolved oxygen water body rises. the
溶氧水体进入多级潜流湿地处理单元,流经进水湿地池、2组分解渗滤湿地池和出水湿地池的分解渗滤层形成波浪式的流动,进水湿地池、2组分解渗滤湿地池和出水湿地池的分解渗滤层构成“基质--植物--微生物”生态系统,种植物的根系扎根于分解渗滤层的表层,分解渗滤层的填料基质为微生物提供附着的载体,种植物的根系为微生物提供氧源,在靠近根区的填料基质层形成好氧区,远离根区的填料基质层形成厌氧区或兼氧区,溶氧水体在流动的过程中流经分解渗滤层的表层和底层,反复经过好氧、厌氧、硝化和反硝化的反应过程,实施高效去除溶氧水体中的有机污染物和氮磷制成排放水体,排放水体收入收水管内,排放水体从收水管进入排放蓄积池内蓄积,再由排放管排放到河道或湖泊。 The dissolved oxygen water enters the multi-stage subsurface flow wetland treatment unit, and flows through the decomposed infiltration layer of the influent wetland pool, the 2-component decomposing and percolating wetland pool and the effluent wetland pool to form a wave-like flow. The decomposed infiltration layer of the wetland pool and the effluent wetland pool constitutes a "matrix-plant-microbe" ecosystem. The root system of the plant takes root in the surface layer of the decomposed infiltration layer, and the filler matrix of the decomposed infiltration layer provides a carrier for microorganisms to attach to. , the root system of plant species provides oxygen source for microorganisms, the aerobic zone is formed in the filler matrix layer close to the root zone, and the anaerobic zone or facultative zone is formed in the filler matrix layer far away from the root zone, and the dissolved oxygen water flows through the decomposition process The surface layer and the bottom layer of the percolation layer go through the reaction process of aerobic, anaerobic, nitrification and denitrification repeatedly, and implement the efficient removal of organic pollutants and nitrogen and phosphorus in the dissolved oxygen water body to make the discharge water body, and the discharge water body is collected into the water collection pipe. The discharge water enters the discharge storage tank from the water collection pipe to accumulate, and then is discharged to rivers or lakes through the discharge pipe. the
本实用新型与自然湿地相比,在相同面积条件下污水处理能力大幅度提高,克服天然湿地比较脆弱的缺点,具有负荷率高、占地面积小、效果可靠、耐冲击负荷等优点,水流在分解渗滤层的表层以下流动,不易滋生蚊蝇,种 植水质净化能力强,具有良好的景观效果。 Compared with the natural wetland, the utility model greatly improves the sewage treatment capacity under the same area conditions, overcomes the relatively fragile shortcomings of the natural wetland, and has the advantages of high load rate, small floor area, reliable effect, and impact load resistance. It flows below the surface of the decomposed percolation layer, which is not easy to breed mosquitoes and flies. It has a strong ability to purify the planting water and has a good landscape effect. the
当溶氧水体在多级潜流湿地处理单元中运行过程中,通过检测观察竖井观测进水湿地池、2组分解渗滤湿地池和出水湿地池的运行情况是否达到设计要求,从检测观察竖井中抽取水样进行检测水质是否达到设计要求,及时调节布水管上的闸阀,控制进水量,抑制分解渗滤层中的水流速度,调整分解渗滤层处于最佳分解状态。 When the dissolved oxygen water body is operating in the multi-stage subsurface flow wetland treatment unit, observe whether the operation conditions of the influent wetland pool, the two-component decomposition infiltration wetland pool and the outlet wetland pool meet the design requirements through the detection and observation shaft. Take water samples to test whether the water quality meets the design requirements, adjust the gate valve on the water distribution pipe in time, control the water intake, suppress the water flow velocity in the decomposed percolation layer, and adjust the decomposed percolation layer to be in the best decomposition state. the
当溶氧水体在多级潜流湿地处理单元中运行过程中,通过检测观察竖井观测进水湿地池、2组分解渗滤湿地池和出水湿地池的运行情况是否达到设计要求,从检测观察竖井中抽取水样进行检测水质是否达到设计要求,及时调节布水管上的闸阀,控制进水量,抑制分解渗滤层中的水流速度,调整分解渗滤层处于最佳分解状态。 When the dissolved oxygen water body is operating in the multi-stage subsurface flow wetland treatment unit, observe whether the operation conditions of the influent wetland pool, the two-component decomposition infiltration wetland pool and the outlet wetland pool meet the design requirements through the detection and observation shaft. Take water samples to test whether the water quality meets the design requirements, adjust the gate valve on the water distribution pipe in time, control the water intake, suppress the water flow velocity in the decomposed percolation layer, and adjust the decomposed percolation layer to be in the best decomposition state. the
当溶氧水体在多级潜流湿地处理单元中运行过程中,通过检测观察竖井观测进水湿地池、2组分解渗滤湿地池和出水湿地池的运行情况,以及从检测观察竖井中去除水样进行检测水质情况。 When the dissolved oxygen water body is operating in the multi-stage subsurface flow wetland treatment unit, observe the operation of the influent wetland pool, the 2-component decomposition infiltration wetland pool and the effluent wetland pool through the detection and observation shaft, and remove water samples from the detection and observation shaft Check water quality. the
当多级沉淀预处理单元运行一段时间后沉淀分解池、发酵沉淀池和蓄积池内的底部沉淀了沉渣,依照设计要求需要对沉淀分解池、发酵沉淀池和蓄积池实施清渣、清淤,关闭进污口的管路上的闸阀,停止污水源的流入,关闭出水口的管路上的闸阀,停止污水处理后的污水源的流出。打开沉淀分解池、发酵沉淀池和蓄积池顶部清渣口的密封盖,清除沉淀分解池、发酵沉淀池和蓄积池内的沉渣和淤泥,清除过流管、进污口和出水口内壁上的附着污垢,保持畅通。关闭沉淀分解池、发酵沉淀池和蓄积池顶部清渣口的密封盖,打开进污口的管路上的闸阀和出水口的管路上的闸阀,启动多级沉淀预处理单元恢复运行。 When the multi-stage sedimentation pretreatment unit has been running for a period of time, the bottom of the sedimentation and decomposition tank, fermentation sedimentation tank and storage tank has deposited sediment. According to the design requirements, it is necessary to clean the sedimentation and decomposition tank, fermentation sedimentation tank and storage tank. The gate valve on the pipeline of the sewage inlet stops the inflow of the sewage source, and closes the gate valve on the pipeline of the water outlet to stop the outflow of the sewage source after sewage treatment. Open the sealing cover of the slag removal port on the top of the sedimentation and decomposition tank, fermentation sedimentation tank and storage tank, remove the sediment and silt in the sedimentation and decomposition tank, fermentation sedimentation tank and storage tank, and remove the adhesion on the inner wall of the overflow pipe, sewage inlet and water outlet Dirt, keep it clear. Close the sealing cover of the slag removal port on the top of the sedimentation tank, fermentation sedimentation tank and storage tank, open the gate valve on the pipeline of the sewage inlet and the gate valve on the pipeline of the water outlet, and start the multi-stage sedimentation pretreatment unit to resume operation. the
污水源中夹带有一定量的悬浮物、漂浮物和泥沙之类,经沉淀、分解后,污水源实现分离,处于中层的污水水体在水体重力的作用下,通过倾斜安设在隔板中部的过流管分流到下一池中,几经分流直至从安设在多级沉淀预处理单元另一端的出水口自流到多级水解氧化单元内实施下一流程的污水处理,多级水解氧化单元内的悬浮物、漂浮物和泥沙之类不断沉淀在池底,经过一段时间的运行池底的沉渣蓄积在池底,影响多级沉淀预处理单元的污水处理的运行,则需要对多级沉淀预处理单元实施清渣工作。 There is a certain amount of suspended matter, floating matter and sediment in the sewage source. After sedimentation and decomposition, the sewage source is separated. The sewage water body in the middle layer is installed in the middle of the partition by tilting under the action of water gravity. The flow pipe of the overflow pipe is shunted to the next pool, and after several shunts, it flows automatically from the outlet installed at the other end of the multi-stage sedimentation pretreatment unit to the multi-stage hydrolysis and oxidation unit for the next process of sewage treatment. The multi-stage hydrolysis and oxidation unit Suspended matter, floating matter and sediment in the tank are continuously deposited at the bottom of the tank. After a period of operation, the sediment at the bottom of the tank accumulates at the bottom of the tank, which affects the operation of the sewage treatment of the multi-stage sedimentation pretreatment unit. The sedimentation pretreatment unit implements slag removal work. the
当多级水解酸化处理单元运行一段时间后依照设计要求对进水水解氧化池、水解氧化池、出水水解氧化池和集水出水池实施检修和维护,关闭进水口的管路上的闸阀,停止清液污水水体的流入,排空多级水解酸化处理单元内的无害水体,关闭出水口的管路上的闸阀,开启潜水泵排空集水出水池内的无害水体,关闭潜水泵。打开进水水解氧化池、水解氧化池和出水水解氧化池的顶部检修口上的密封盖,对进水水解氧化池、水解氧化池和出水水解氧化池实施检修和维护,清洗集水出水池的池壁上的附着污垢,清洗L形过流管、进水口和出水口内壁上的附着污垢,保持通畅,检修和维护潜水泵。检修和维护结束后,关闭进水水解氧化池、水解氧化池和出水水解氧化池的 顶部检修口上的密封盖,打开进水口的管路上的闸阀出水口的管路上的闸阀,启动多级水解酸化处理单元恢复运行。 After the multi-stage hydrolytic acidification treatment unit has been in operation for a period of time, according to the design requirements, the influent hydrolytic oxidation tank, the hydrolytic oxidation tank, the effluent hydrolytic oxidation tank and the water collection outlet tank shall be inspected and maintained, and the gate valve on the pipeline of the water inlet shall be closed to stop cleaning. The inflow of liquid sewage water body, empty the harmless water body in the multi-stage hydrolysis acidification treatment unit, close the gate valve on the pipeline of the water outlet, turn on the submersible pump to empty the harmless water body in the water collection outlet pool, and turn off the submersible pump. Open the sealing cover on the top inspection port of the inlet hydrolysis oxidation pool, hydrolysis oxidation pool and outlet water hydrolysis oxidation pool, carry out inspection and maintenance on the inlet water hydrolysis oxidation pool, hydrolysis oxidation pool and outlet water hydrolysis oxidation pool, and clean the pools of the water collection and outlet pools The attached dirt on the wall, clean the attached dirt on the inner wall of the L-shaped overflow pipe, the water inlet and the water outlet, keep it unobstructed, overhaul and maintain the submersible pump. After inspection and maintenance, close the sealing caps on the top inspection ports of the inlet hydrolysis oxidation tank, hydrolysis oxidation tank and outlet water hydrolysis oxidation tank, open the gate valve on the pipeline of the water inlet and the gate valve on the pipeline of the water outlet, and start the multi-stage hydrolysis and acidification The processing unit resumes operation. the
本实用新型的多级水解酸化处理单元是装有水解过滤层的厌氧生物反应器,根据设计要求经过一段时间的运行,多级水解酸化处理单元内的池壁、进水口、L形过流管、出水口、管道和潜水泵都会存在着附着污垢,附着污垢不断的蓄积、加厚,会影响多级水解酸化处理单元的污水处理的运行,需要对多级水解酸化处理单元实施检修和维护。 The multi-stage hydrolysis acidification treatment unit of the utility model is an anaerobic bioreactor equipped with a hydrolysis filter layer. Pipes, water outlets, pipelines and submersible pumps will all have attached dirt, which will continue to accumulate and thicken, which will affect the operation of the sewage treatment of the multi-stage hydrolytic acidification treatment unit, and the multi-stage hydrolysis acidification treatment unit needs to be overhauled and maintained . the
当曝气增氧处理单元运行一段时间后依照设计要求对曝气增氧处理单元实施检修和维护,关闭进水口的管路上的闸阀,停止清液污水水体的流入,排空曝气增氧处理单元内的溶氧水体,关闭出水口的管路上的闸阀,清除曝气增氧处理单元的池壁上的附着污垢,清洗主干管和曝气管,保持畅通,检修和维护曝气机。开启进水口的管路上的闸阀,注入清液污水水体,开启出水口的管路上的闸阀,贯通向多级潜流湿地处理单元的布水管输送溶氧水体,开启曝气机,通过主干管和曝气管向曝气增氧处理单元内的清液污水水体曝气增氧,曝气增氧处理单元恢复运行。 After the aeration and oxygenation treatment unit has been in operation for a period of time, the aeration and oxygenation treatment unit shall be overhauled and maintained according to the design requirements, the gate valve on the pipeline of the water inlet shall be closed, the inflow of clear liquid and sewage water shall be stopped, and the aeration and aeration treatment shall be emptied For the dissolved oxygen water in the unit, close the gate valve on the pipeline of the water outlet, remove the attached dirt on the pool wall of the aeration and aeration treatment unit, clean the main pipe and aeration pipe, keep it unblocked, and repair and maintain the aerator. Open the gate valve on the pipeline of the water inlet, inject clear liquid and sewage water, open the gate valve on the pipeline of the water outlet, pass through the water distribution pipeline of the multi-stage subsurface flow wetland treatment unit to transport dissolved oxygen water, turn on the aerator, and pass through the main pipe and aeration The trachea aerates and increases oxygen to the clear liquid sewage water body in the aeration and oxygen enhancement treatment unit, and the aeration and oxygen enhancement treatment unit resumes operation. the
本实用新型的曝气增氧处理单元是要增加无害水体中的溶解氧的含量,为后续多级潜流湿地单元的好氧微生物提供氧源。根据设计要求经过一段时间的运行,曝气增氧处理单元的池壁、进水口、出水口、主干管、曝气管和曝气机均会存在着附着污垢,随着附着污垢的不断续集、加厚,会直接影响曝气增氧处理单元的运行,需要对曝气增氧处理单元实施检修和维护。 The aeration and oxygenation treatment unit of the utility model is to increase the dissolved oxygen content in the harmless water body, and provide an oxygen source for the aerobic microorganisms in the subsequent multi-stage subsurface flow wetland unit. After a period of operation according to the design requirements, there will be attached dirt on the pool wall, water inlet, water outlet, main pipe, aeration pipe and aerator of the aeration and oxygenation treatment unit. With the continuous continuation of the attached dirt, Thickening will directly affect the operation of the aeration and oxygenation treatment unit, and the aeration and oxygenation treatment unit needs to be overhauled and maintained. the
当多级潜流湿地处理单元运行一段时间后分解渗滤层出现阻塞,分解渗滤层中的阻塞物影响分解渗滤层的分解反应,需要对分解渗滤层实施反冲洗,关闭布水管上的闸阀,停止输入溶氧水体,排空收水管内的排放水体,关闭收水管上的闸阀。从反冲洗主干管向反冲洗管路注入反冲洗水源,冲洗分解渗滤层,把分解渗滤层中的阻塞物反冲洗到进水湿地池、2组分解渗滤湿地池和出水湿地池的顶部,出水湿地池的顶部的反冲洗水源和阻塞物通过多级潜流湿地单元上部的反冲洗排空口排出多级潜流湿地单元。停止向反冲洗管路注入反冲洗水源,关闭反冲洗排空口,打开进水湿地池、2组分解渗滤湿地池和出水湿地池的检修放空管上的闸阀,从放空管放空进水湿地池、2组分解渗滤湿地池和出水湿地池反冲洗水体,关闭进水湿地池、2组分解渗滤湿地池和出水湿地池的检修放空管上的闸阀,开启布水管上的闸阀,开始输入溶氧水体,开启收水管上的闸阀,多级潜流湿地处理单元恢复运行。 When the multi-stage subsurface flow wetland treatment unit runs for a period of time, the decomposed percolation layer is blocked, and the blockage in the decomposed percolation layer affects the decomposition reaction of the decomposed percolation layer. It is necessary to backwash the decomposed percolation layer and close the water distribution pipe. Gate valve, stop the input of dissolved oxygen water, empty the discharge water in the water collection pipe, and close the gate valve on the water collection pipe. Inject the backwashing water source from the main backwashing pipe to the backwashing pipeline, flush the decomposed percolation layer, and backwash the obstructions in the decomposed percolation layer to the inlet wetland pool, the 2-component decomposed percolation wetland pool and the outlet wetland pool At the top, the backwash water source and obstructions at the top of the effluent wetland pool are discharged from the multi-stage subsurface flow wetland unit through the backwash emptying port on the upper part of the multi-stage subsurface flow wetland unit. Stop injecting the backwash water source into the backwash pipeline, close the backwash vent, open the gate valves on the maintenance vent pipes of the inlet wetland pool, the 2-component decomposition percolation wetland pool and the outlet wetland pool, and vent the air from the vent pipe. Backwash the water body in the water wetland pool, the 2-component decomposing and infiltrating wetland pool and the effluent wetland pool, close the gate valve on the inspection and venting pipe of the influent wetland pool, the 2-component decomposing and infiltrating wetland pool and the effluent wetland pool, and open the gate valve on the water distribution pipe Gate valve, start to input dissolved oxygen water, open the gate valve on the water collection pipe, and the multi-stage subsurface flow wetland treatment unit resumes operation. the
从曝气增氧处理单元增加溶解氧含量的溶氧水体进入多级潜流湿地处理单元实施好氧、厌氧、硝化和反硝化的处理,根据设计要求经过一段时间的运行,分解渗滤层内产生阻塞物,影响分解渗滤层的分解反应,需要对多级潜流湿地处理单元实施反冲洗,清洗分解渗滤层。 The dissolved oxygen water body with increased dissolved oxygen content from the aeration and oxygenation treatment unit enters the multi-stage subsurface flow wetland treatment unit for aerobic, anaerobic, nitrification and denitrification treatment. After a period of operation according to the design requirements, the infiltration layer is decomposed. The blockage will affect the decomposition reaction of the decomposed percolation layer. It is necessary to backwash the multi-stage subsurface flow wetland treatment unit to clean the decomposed percolation layer. the
当多级潜流湿地处理单元长时间运行后,按设计要求需要对多级潜流湿地处理单元进行检修和维护,关闭布水管上的闸阀,停止进水,放空收水管中的排放水,关闭收水管的闸阀,停止出水,打开进水湿地池、2组分解渗滤 湿地池和出水湿地池的检修放空管上的闸阀,从放空管放空进水湿地池、2组分解渗滤湿地池和出水湿地池污水处理水体,对多级潜流湿地处理单元实施检修和维护。清洗布水管、收水管反冲洗连通口和反冲洗排空口的内壁上附着污垢,清整分解渗滤层上表层的种植物。检修结束,关闭进水湿地池、2组分解渗滤湿地池和出水湿地池的检修放空管上的闸阀,开启布水管上的闸阀,开始进水,开启收水管的闸阀,开始出水,多级潜流湿地处理单元恢复运行。 After the multi-stage subsurface flow wetland treatment unit has been in operation for a long time, it is necessary to overhaul and maintain the multi-stage subsurface flow wetland treatment unit according to the design requirements, close the gate valve on the water distribution pipe, stop the water intake, empty the discharge water in the water collection pipe, and close the water collection pipe Stop the water outlet, open the gate valves on the maintenance vent pipes of the inlet wetland pool, the 2-component decomposition and infiltration wetland pool and the outlet wetland pool, and empty the inlet wetland pool, the 2-component decomposition and percolation wetland pool and the discharge pipe from the vent pipe The sewage treatment water body of the effluent wetland pool shall be overhauled and maintained for the multi-stage subsurface flow wetland treatment unit. Clean the dirt attached to the inner wall of the backwash connection port of the water distribution pipe and the water collection pipe and the backwash emptying port, and clean and decompose the plants on the upper surface of the percolation layer. After the maintenance is over, close the gate valves on the inspection and venting pipes of the inlet wetland pool, the 2-component decomposing and percolating wetland pool and the outlet wetland pool, open the gate valve on the water distribution pipe, start water intake, open the gate valve of the water collection pipe, start water discharge, and more The first-level subsurface flow wetland treatment unit resumed operation. the
当多级潜流湿地处理单元运行一段时间后,根据设计要求需要对多级潜流湿地处理单元实施检修和维护。清洗布水管、收水管反冲洗连通口和反冲洗排空口的内壁上附着污垢,清整分解渗滤层上表层的种植物。 After the multi-stage subsurface flow wetland treatment unit has been in operation for a period of time, it is necessary to overhaul and maintain the multi-stage subsurface flow wetland treatment unit according to the design requirements. Clean the dirt attached to the inner wall of the backwash connection port of the water distribution pipe and the water collection pipe and the backwash emptying port, and clean and decompose the plants on the upper surface of the percolation layer. the
本实用新型对悬浮物的去除率可达到90.9%,对化学需氧量的去除率可达到85%,对生化需氧量的去除率可达到90%,对总氮的去除率可达到50%,对氨氮的去除率可达到68%,对总磷的去除率可达到87.5%,见去除污染物计算表。 The utility model has a removal rate of 90.9% for suspended solids, 85% for chemical oxygen demand, 90% for biochemical oxygen demand, and 50% for total nitrogen. , The removal rate of ammonia nitrogen can reach 68%, and the removal rate of total phosphorus can reach 87.5%, see the calculation table of pollutant removal. the
去除污染物的效果计算表 Calculation table of the effect of removing pollutants
本实用新型是多级污水处理用生物反应系统。设计科学,结构合理,投资省,工期短,见效快,负荷率高,主要采用自流方式,机电设备较少,运行成本低,污水处理费低,占地面积小,污水处理效果明显,可直接排入水库、河道和湖泊,能够克服天然湿地比较脆弱的缺点,氮磷去除能力强,耐冲击负荷,运转维护管理方便,工程基建与运转费用低,一年四季都能进行净化处理,水解渗滤层的渗透系数高,对水流阻力相对较小,多数污水处理单元采用密闭处理方式,水流在填料表层以下流动,卫生条件好,不易产生臭味和滋生蚊蝇等优点。采用开放式布局,便于景观建设,可以和城市景观建设紧密结合,作为公园绿地,同时可起到美化环境作用,改善相邻地区的景观。 The utility model is a biological reaction system for multi-stage sewage treatment. The design is scientific, the structure is reasonable, the investment is low, the construction period is short, the effect is quick, and the load rate is high. Discharging into reservoirs, rivers and lakes can overcome the weakness of natural wetlands. It has strong nitrogen and phosphorus removal capacity, impact load resistance, convenient operation, maintenance and management, low engineering infrastructure and operation costs, and can be purified all year round. The permeability coefficient of the filter layer is high, and the resistance to water flow is relatively small. Most sewage treatment units adopt a closed treatment method, and the water flow flows below the surface of the filler. The sanitary conditions are good, and it is not easy to produce odors and breed mosquitoes and flies. The open layout is convenient for landscape construction, and can be closely integrated with urban landscape construction. It can be used as a park green space, and at the same time, it can beautify the environment and improve the landscape of adjacent areas. the
本实用新型采用生物生态处理技术对生活污水进行处理,机电设备较少,生物生态技术具有较强的自我调节能力和修复能力,使用寿命至少在50年以上。本实用新型污水处理符合国家排放标准。 The utility model adopts biological ecological treatment technology to process domestic sewage, has less mechanical and electrical equipment, biological ecological technology has strong self-regulation ability and repair ability, and the service life is at least 50 years. The sewage treatment of the utility model conforms to the national discharge standard. the
附图说明 Description of drawings
以下结合附图和实施例对本实用新型详细说明。 The utility model is described in detail below in conjunction with accompanying drawing and embodiment. the
图1多级污水处理用生物反应系统的整体布局示意图 Figure 1 Schematic diagram of the overall layout of the biological reaction system for multi-stage sewage treatment
图2多级污水处理用生物反应系统的整体布局示意图 Figure 2 Schematic diagram of the overall layout of the biological reaction system for multi-stage sewage treatment
图3多级污水处理用生物反应系统的多级沉淀预处理单元的剖视示意图 Figure 3 Schematic cross-sectional view of the multi-stage sedimentation pretreatment unit of the biological reaction system for multi-stage sewage treatment
图4多级污水处理用生物反应系统的多级水解酸化处理单元的剖视示意图 Figure 4 Schematic cross-sectional view of the multi-stage hydrolysis acidification treatment unit of the biological reaction system for multi-stage sewage treatment
图5多级污水处理用生物反应系统的曝气增氧处理单元的剖视示意图 Figure 5 Schematic cross-sectional view of the aeration and oxygenation treatment unit of the biological reaction system for multi-stage sewage treatment
图6多级污水处理用生物反应系统的多级潜流湿地处理单元的剖视示意图 Fig. 6 Schematic cross-sectional view of the multi-stage subsurface flow wetland treatment unit of the biological reaction system for multi-stage sewage treatment
1多级沉淀预处理单元,2多级水解酸化处理单元,3曝气溶氧装置,4多级潜流湿地处理单元,5集水出水池,6沉淀分解池,7发酵沉淀池,8蓄积池,9过流管,10清渣口,11进污口,12出水口,13进水口,14管路,15检修口,16L形过流管,17水解酸化填滤料,18曝气机,19布水管,20水平过流管,21收水管,22放空管,23种植物,24检修放空管,25蓄积排放池,26排放管,27检测观察竖井,28检修放空控制井,29水解过滤层,30曝气管,31潜水泵,32反冲洗排空口,33隔板,34主干管,35进水湿地池,36分解渗滤湿地,37出水湿地池,38分解渗滤层,39放空管,39进水水解氧化池,40水解氧化池,41出水水解氧化池,42反冲洗管路,43反冲洗连通口。 1. Multi-stage sedimentation pretreatment unit, 2. Multi-stage hydrolysis acidification treatment unit, 3. Aeration and dissolved oxygen device, 4. Multi-stage subsurface flow wetland treatment unit, 5. Water collection and effluent tank, 6. Sedimentation and decomposition tank, 7. Fermentation sedimentation tank, 8. Storage tank , 9 overcurrent pipe, 10 slag removal port, 11 sewage inlet, 12 water outlet, 13 water inlet, 14 pipeline, 15 inspection port, 16L-shaped overcurrent pipe, 17 hydrolysis acidification filling filter material, 18 aerator, 19 Water distribution pipes, 20 Horizontal flow pipes, 21 Water collection pipes, 22 Vent pipes, 23 Plants, 24 Maintenance vent pipes, 25 Accumulation and discharge tanks, 26 Discharge pipes, 27 Inspection and observation shafts, 28 Maintenance and venting control wells, 29 Hydrolysis filter layer, 30 aeration pipe, 31 submersible pump, 32 backwash emptying port, 33 clapboard, 34 main pipe, 35 water inlet wetland pool, 36 decomposition percolation wetland, 37 water outlet wetland pool, 38 decomposition percolation layer , 39 vent pipe, 39 water inlet hydrolysis oxidation pool, 40 hydrolysis oxidation pool, 41 water outlet hydrolysis oxidation pool, 42 backwash pipeline, 43 backwash connection port. the
具体实施方式 Detailed ways
实施例1 Example 1
由多级沉淀预处理单元(1)、多级水解酸化处理单元(2)、曝气增氧处理单元(3)和多级潜流湿地处理单元(4)通过管路(14)相连接构成,多级潜流湿地处理单元(4)的进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)依次排列,多级潜流湿地处理单元(4)的一侧并列依次设置多级沉淀预处理单元(1)、多级水解酸化处理单元(2)和曝气增氧处理单元(3),并通过管路(14)相连接,如图1所示。 It is composed of a multi-stage sedimentation pretreatment unit (1), a multi-stage hydrolysis acidification treatment unit (2), an aeration and oxygenation treatment unit (3) and a multi-stage subsurface flow wetland treatment unit (4) connected by a pipeline (14), The inflow wetland pool (35), the 2-component decomposition and infiltration wetland pool (36) and the outlet wetland pool (37) of the multistage subsurface flow wetland treatment unit (4) are arranged in sequence, and one side of the multistage subsurface flow wetland treatment unit (4) The multi-stage sedimentation pretreatment unit (1), the multi-stage hydrolytic acidification treatment unit (2) and the aeration and oxygenation treatment unit (3) are arranged side by side in sequence, and are connected by pipelines (14), as shown in FIG. 1 . the
实施例2 Example 2
多级沉淀预处理单元(1)、多级水解酸化处理单元(2)、曝气增氧处理单元(3)和多级潜流湿地处理单元(4)依次排列设置并通过管路(14)相连接,如图2所示。 The multi-stage sedimentation pretreatment unit (1), the multi-stage hydrolytic acidification treatment unit (2), the aeration and aeration treatment unit (3) and the multi-stage subsurface flow wetland treatment unit (4) are arranged in sequence and connected to each other through the pipeline (14). connection, as shown in Figure 2. the
实施例3 Example 3
多级沉淀预处理单元(1)呈封闭箱体,箱体内由隔板(33)分隔成至少3个空间,其空间依次分别为沉淀分解池(6)、发酵沉淀池(7)和蓄积池(8),每个空间顶部设置密闭的清渣口(10),清渣口(10)上安设密封盖,构成密闭的运行空间。 The multi-stage sedimentation pretreatment unit (1) is a closed box, and the box is divided into at least 3 spaces by a partition (33), and the spaces are respectively the sedimentation and decomposition tank (6), the fermentation sedimentation tank (7) and the storage tank. (8), an airtight slag removal port (10) is arranged on the top of each space, and a sealing cover is installed on the slag removal port (10), forming a closed operating space. the
多级沉淀预处理单元(1)一侧的沉淀分解池(6)的池壁上部设置进污口(11),进污口(11)通过管路(14)引入污水源,进污口(11)的管路(14)上设置闸阀,控制污水源的流入量,污水源为生活污水和养殖废水。沉淀分解池(6)和发酵沉淀池(7)之间的隔板(33)中部设置倾斜的过流管(9) 至少1个,沉淀分解池(6)的过流管(9)的入口低于发酵沉淀池(7)的过流管(9)的出口,沉淀分解池(6)内的污水源经沉淀、分解后的污水水体受水体重力作用从过流管(9)流入发酵沉淀池(7)内发酵、沉淀。 The upper part of the pool wall of the sedimentation decomposition tank (6) on one side of the multi-stage sedimentation pretreatment unit (1) is provided with a sewage inlet (11), and the sewage inlet (11) is introduced into a sewage source through a pipeline (14), and the sewage inlet ( 11) A gate valve is set on the pipeline (14) to control the inflow of the sewage source, and the sewage source is domestic sewage and aquaculture wastewater. At least one inclined overflow pipe (9) is arranged in the middle of the partition (33) between the sedimentation and decomposition tank (6) and the fermentation sedimentation tank (7), and the inlet of the overflow pipe (9) of the sedimentation and decomposition tank (6) Lower than the outlet of the overflow pipe (9) of the fermentation sedimentation tank (7), the sewage source in the sedimentation and decomposition tank (6) has been precipitated and decomposed. The sewage water body is subjected to the gravity of the water and flows from the overflow pipe (9) into the fermentation tank. Fermentation and sedimentation in the sedimentation tank (7). the
发酵沉淀池(7)和蓄积池(8)之间的隔板(33)中部设置倾斜的过流管(9),发酵沉淀池(7)的过流管(9)的入口低于蓄积池(8)的过流管(9)的出口,发酵沉淀池(7)内的污水水体又经发酵、沉淀后的污水液受水体重力作用从过流管(9)流入蓄积池(8)内分离、沉淀。 An inclined overflow pipe (9) is arranged in the middle of the partition (33) between the fermentation sedimentation tank (7) and the accumulation tank (8), and the inlet of the overflow pipe (9) of the fermentation sedimentation tank (7) is lower than the accumulation tank The outlet of the overflow pipe (9) of (8), the sewage water body in the fermentation sedimentation tank (7) is fermented, and the sewage liquid after sedimentation flows into the storage tank (8) from the overflow pipe (9) under the action of water gravity. Internal separation and precipitation. the
多级沉淀预处理单元(1)另一侧的蓄积池(8)的池壁上部设置出水口(12),通过管路(14)与多级水解酸化处理单元(2)的池壁下部的进水口(13)相连接,管路(14)上设置闸阀,控制输出流量,进入蓄积池(8)内的污水液水体再经发酵、沉淀后的清液水体从池壁上部的出水口(12)通过管路(14)自流输入多级水解酸化处理单元(2)的进水口(13),管路(14)上设置控制闸阀控制输入多级水解酸化处理单元(2)的流量,进入多级沉淀预处理单元(1)的污水源的流向自多级沉淀预处理单元(1)一端的进污口(11)利用水体的自重通过过流管(9)向多级沉淀预处理单元(1)另一端的出水口(12)顺流流动,在流动的过程中实施沉淀、发酵、分解、灭菌制成清液污水水体,如图1、图2、图3所示。 A water outlet (12) is provided on the upper part of the tank wall of the reservoir (8) on the other side of the multi-stage sedimentation pretreatment unit (1), and the water outlet (12) is connected to the lower part of the tank wall of the multi-stage hydrolysis acidification treatment unit (2) through the pipeline (14). The water inlets (13) are connected, and gate valves are set on the pipelines (14) to control the output flow. The sewage liquid water entering the storage tank (8) is then fermented and precipitated from the water outlet ( 12) The water inlet (13) of the multi-stage hydrolysis and acidification treatment unit (2) is automatically input through the pipeline (14), and a control gate valve is set on the pipeline (14) to control the flow input into the multi-stage hydrolysis and acidification treatment unit (2). The sewage source of the multi-stage sedimentation pretreatment unit (1) flows from the sewage inlet (11) at one end of the multi-stage sedimentation pretreatment unit (1) to the multi-stage sedimentation pretreatment unit through the overflow pipe (9) by using the self-weight of the water body (1) The water outlet (12) at the other end flows downstream, and during the flow process, sedimentation, fermentation, decomposition, and sterilization are carried out to make clear liquid sewage water, as shown in Figures 1, 2 and 3. the
实施例4 Example 4
多级水解酸化处理单元(2)呈封闭箱体,多级水解酸化处理单元(2)一端的池壁下部设置进水口(13),多级水解酸化处理单元(2)另一端的池壁上部设置出水口(12),出水口(12)的管路(14)上设置闸阀,控制输出流量。多级水解酸化处理单元(2)的箱体内由隔板(33)分隔成至少3个空间,其空间依次为进水水解氧化池(39)、水解氧化池(40)和出水水解氧化池(41),进水水解氧化池(39)、水解氧化池(40)和出水水解氧化池(41)的顶部分别设置密闭的检修口(15),检修口(15)上安设密封盖,在进水水解氧化池(39)、水解氧化池(40)和出水水解氧化池(41)的隔板(33)上设置L形过流管(16),L形过流管(16)的进水口高于水解过滤层(29)的顶端部,收集经过水解过滤层(29)实施水解过滤的污水水体,L形过流管(16)的出水口处于另一空间的水解过滤层(29)内的下部,把水解过滤的污水水体输送到下一个水解过滤层,连通进水水解氧化池(39)、水解氧化池(40)和出水水解氧化池(41)。 The multi-stage hydrolytic acidification treatment unit (2) is in the form of a closed box, the lower part of the pool wall at one end of the multi-stage hydrolysis acidification treatment unit (2) is provided with a water inlet (13), and the upper part of the pool wall at the other end of the multi-stage hydrolysis acidification treatment unit (2) is The water outlet (12) is set, and a gate valve is set on the pipeline (14) of the water outlet (12) to control the output flow. The casing of the multi-stage hydrolytic acidification treatment unit (2) is divided into at least 3 spaces by a partition (33), and the spaces are sequentially the influent hydrolytic oxidation pool (39), the hydrolytic oxidation pool (40) and the effluent hydrolytic oxidation pool ( 41), the tops of the water inlet hydrolysis oxidation tank (39), the hydrolysis oxidation tank (40) and the water outlet hydrolysis oxidation tank (41) are respectively provided with airtight inspection ports (15), and a sealing cover is installed on the inspection port (15). An L-shaped overcurrent pipe (16) is arranged on the dividing plate (33) of the inlet water hydrolysis oxidation pond (39), the hydrolysis oxidation pond (40) and the outlet water hydrolysis oxidation pond (41), and the inlet of the L-shaped overflow pipe (16) The water outlet is higher than the top of the hydrolysis filter layer (29), collects the sewage water body that is hydrolyzed and filtered through the hydrolysis filter layer (29), and the water outlet of the L-shaped overcurrent pipe (16) is in another space of the hydrolysis filter layer (29) The lower part in the inner part transports the hydrolyzed and filtered sewage water body to the next hydrolyzed filter layer, and communicates with the influent hydrolyzed oxidation pond (39), the hydrolyzed oxidized pond (40) and the effluent hydrolyzed oxidized pond (41). the
在进水水解氧化池(39)、水解氧化池(40)和出水水解氧化池(41)内设置水解过滤层(29),水解过滤层(29)的顶端部低于L形过流管(16)的进水口和池壁上的出水口(12),水解过滤层(29)填充水解酸化虑料(17),水解酸化虑料(17)采用粒径1-2cm的陶粒或聚乙烯弹性填粒。 The hydrolysis filter layer (29) is set in the water inlet hydrolysis oxidation tank (39), the hydrolysis oxidation tank (40) and the outlet water hydrolysis oxidation tank (41), and the top of the hydrolysis filter layer (29) is lower than the L-shaped overflow pipe ( 16) of the water inlet and the water outlet (12) on the pool wall, the hydrolysis filter layer (29) is filled with hydrolysis acidification material (17), and the hydrolysis acidification material (17) adopts ceramsite or polyethylene with a particle size of 1-2cm Elastic filler. the
进入多级水解酸化处理单元(2)的清液水体的流向自多级水解酸化处理单元(2)一端的进水口(13)利用水体的自重通过L形过流管(16)向多级水解酸化处理单元(2)另一端的出水口(12)顺流流动,在流动的过程中实施水解、氧化、发酵制成无害水体。 The clear liquid water entering the multi-stage hydrolysis acidification treatment unit (2) flows from the water inlet (13) at one end of the multi-stage hydrolysis acidification treatment unit (2) to the multi-stage hydrolysis through the L-shaped overflow pipe (16) by the self-weight of the water body. The water outlet (12) at the other end of the acidification treatment unit (2) flows downstream, and is hydrolyzed, oxidized, and fermented during the flowing process to form a harmless water body. the
多级水解酸化处理单元(2)另一端部的池壁外设置集水出水池(5),集水出水池(5)整体呈箱形,集水出水池(5)与多级水解酸化处理单元(2)另一端部的池壁相连接,多级水解酸化处理单元(2)的出水口(13)与集水出水池(5)贯通,集水出水池(5)的另一侧的池壁上部设置出水口(12),集水出水池(5)内底部安设潜水泵(31),潜水泵(31)通过管路(14)穿过出水口(12)把水解氧化的清液水体提升,输送到曝气增氧处理单元(3)内,如图1、图2、4所示。 A water collection and outlet pool (5) is arranged outside the pool wall at the other end of the multi-stage hydrolysis acidification treatment unit (2). The pool wall at the other end of the unit (2) is connected, the water outlet (13) of the multi-stage hydrolysis acidification treatment unit (2) is connected with the water collection outlet pool (5), and the other side of the water collection outlet pool (5) A water outlet (12) is arranged on the upper part of the pool wall, and a submersible pump (31) is installed at the bottom of the water collection outlet pool (5). The liquid water body is lifted and transported to the aeration and oxygenation treatment unit (3), as shown in Fig. 1, Fig. 2 and Fig. 4 . the
实施例5 Example 5
曝气增氧处理单元(3)整体呈箱形,曝气增氧处理单元(3)一端的池壁上设置进水口(13),进水口(13)上的管路(14)设置闸阀,控制进水口(13)的流量,集水出水池(5)中的水解氧化的清液水体通过管路(14)从进水口(13)进入曝气增氧处理单元(3)内。 The aeration and oxygenation processing unit (3) is box-shaped as a whole, and a water inlet (13) is arranged on the pool wall at one end of the aeration and oxygenation processing unit (3), and a gate valve is arranged on the pipeline (14) on the water inlet (13). The flow rate of the water inlet (13) is controlled, and the hydrolyzed and oxidized clear liquid water in the water collection outlet (5) enters the aeration and oxygenation treatment unit (3) from the water inlet (13) through the pipeline (14). the
曝气增氧处理单元(3)另一端的池壁上部设置曝气机(18),曝气增氧处理单元(3)的池底部沿池底部至少设置1根曝气管(30),曝气管(30)与主干管(34)相连接,曝气机(18)与主干管(34)端部相连接,主干管(34)上设置控制闸阀,控制曝气管(30)的进气量,曝气机(18)通过主干管(34)和曝气管(30)向曝气增氧处理单元(3)的池内曝气,增加无害水体中溶解氧的含量制成溶氧水体。 An aerator (18) is arranged on the upper part of the pool wall at the other end of the aeration and oxygenation treatment unit (3), and at least one aeration pipe (30) is arranged at the bottom of the pool of the aeration and oxygenation treatment unit (3) along the bottom of the pool. The trachea (30) is connected with the main pipe (34), the aerator (18) is connected with the end of the main pipe (34), and the main pipe (34) is provided with a control gate valve to control the intake Gas volume, the aerator (18) aerates into the tank of the aeration and oxygenation treatment unit (3) through the main pipe (34) and the aeration pipe (30), increasing the content of dissolved oxygen in the harmless water body to make dissolved oxygen Water body. the
曝气增氧处理单元(3)的一侧的上部设置出水口(12),出水口(12)上的管路(14)设置闸阀,控制出水口(12)的流量,通过管路(14)与波浪式多级潜流湿地装置(4)的布水管(19)相连接,经过增氧后的溶氧清液水体自流输送到波浪式多级潜流湿地装置(4)内,如图1、图2、图5所示。 The top of one side of the aeration and oxygenation treatment unit (3) is provided with a water outlet (12), and the pipeline (14) on the water outlet (12) is provided with a gate valve to control the flow of the water outlet (12). ) is connected to the water distribution pipe (19) of the wave-type multi-stage submerged flow wetland device (4), and the dissolved oxygen clear liquid water body after oxygenation is transported to the wave-type multi-stage submerged flow wetland device (4) by gravity, as shown in Figure 1, Shown in Figure 2 and Figure 5. the
实施例6 Example 6
多级潜流湿地处理单元(4)整体呈箱形,通过隔板(33)分隔成至少4组潜流湿地池,依次排列为进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37),进水湿地池(35)与其中一组分解渗滤湿地池(36)之间设置隔板(33),隔板(33)的顶端部高于分解渗滤层(38)的上表层,隔板(33)的下部设置水平过流管(20)至少1个,隔板(33)的上部设置反冲洗连通口(43)至少1个。出水湿地池(37)与另一组分解渗滤湿地池(36)之间设置隔板(33),隔板(33)的顶端部高于分解渗滤层(38)的上表层,隔板(33)的下部设置水平过流管(20)至少1个,隔板(33)的上部设置反冲洗连通口(43)至少1个。2组分解渗滤湿地池(36)之间设置隔板(33),隔板(33)安设在分解渗滤层(38)内,隔板(33)的顶端部低于分解渗滤层(38),2组分解渗滤湿地池(36)上部的分解渗滤层(38)相连通。多级潜流湿地处理单元(4)一端的池壁上部设置反冲洗排空口(32),反冲洗排空口(32)将反冲洗分解渗滤层(38)的反冲洗水源和阻塞物一起排出多级潜流湿地处理单元(4)外。 The multi-stage subsurface flow wetland treatment unit (4) is box-shaped as a whole, and is divided into at least 4 groups of subsurface flow wetland pools by a partition (33), which are arranged in turn as an inflow wetland pool (35) and 2 groups of decomposition and percolation wetland pools (36). and the outlet wetland pool (37), the water inlet wetland pool (35) and one of the decomposition and percolation wetland pools (36) are provided with a partition (33), and the top part of the partition (33) is higher than the decomposition and percolation layer (38), the bottom of the dividing plate (33) is provided with at least one horizontal overflow pipe (20), and the top of the dividing plate (33) is provided with at least one backwash communication port (43). A partition (33) is arranged between the effluent wetland pool (37) and another set of decomposition and percolation wetland pools (36), the top of the partition (33) is higher than the upper surface of the decomposition and percolation layer (38), and the partition The lower part of (33) is provided with at least one horizontal flow pipe (20), and the upper part of the partition (33) is provided with at least one backwash communication port (43). A partition (33) is set between the two components of the decomposition and filtration wetland pool (36), the partition (33) is installed in the decomposition and filtration layer (38), and the top of the partition (33) is lower than the decomposition and filtration layer (38), the decomposition and filtration layer (38) on the upper part of the 2-component decomposition and filtration wetland pool (36) is connected. The upper part of the pool wall at one end of the multi-stage subsurface flow wetland treatment unit (4) is provided with a backwash emptying port (32), and the backwashing emptying port (32) is used to decompose the backwashing water source of the percolation layer (38) and the blockage together. Discharge out of the multistage subsurface flow wetland treatment unit (4). the
多级潜流湿地处理单元(4)的池底部设置反冲洗管路(42)至少1个,反冲洗管路(42)埋设在分解渗滤层(38)的底层,反冲洗管路(42)贯穿 进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)的池底部,反冲洗管路(42)与反冲洗主干管相连接,反冲洗主干管引出池外,反冲洗主干管从池外向反冲洗管路(42)输入反冲洗水源。 At least one backwash pipeline (42) is arranged at the bottom of the pool of the multi-stage subsurface flow wetland treatment unit (4), and the backwash pipeline (42) is buried in the bottom layer of the decomposed percolation layer (38), and the backwash pipeline (42) Run through the bottom of the inlet wetland pool (35), the 2-component decomposition and percolation wetland pool (36) and the outlet wetland pool (37), the backwash pipeline (42) is connected with the backwash main pipe, and the backwash main pipe leads to Outside the pool, the main backwashing pipe is input backwashing water source to the backwashing pipeline (42) from the outside of the pool. the
分别在进水湿地池(35)、出水湿地池(37)和2组分解渗滤湿地池(36)内至少设置1个检测观察竖井(27),检测观察竖井(27)贯穿分解渗滤层(38),直至池底部,通过检测观察竖井(27)观测池中的水位以及从检测观察井(27)中取水样。 At least one detection and observation shaft (27) is set in the water inlet wetland pool (35), the water outlet wetland pool (37) and the two-component decomposition and percolation wetland pool (36), and the detection and observation shaft (27) runs through the decomposition and percolation layer (38), until the bottom of the pond, the water level in the observation pond by detecting the observation shaft (27) and taking water samples from the detection observation well (27). the
潜流湿地池内设置分解渗滤层(38),进水湿地池(35)和出水湿地池(37)的分解渗滤层(38)采用粒径2-4cm的砾石,2组分解渗滤湿地池(36)分别采用页岩和陶粒,其中一组分解渗滤湿地池(36)的分解渗滤层(38)采用粒径4-8cm的页岩,另一组分解渗滤湿地池(36)的分解渗滤层(38)采用粒径2-4cm的陶粒。 The decomposing and percolating layer (38) is arranged in the subsurface wetland pool, and the decomposing and percolating layer (38) of the influent wetland pool (35) and the outflowing wetland pool (37) adopts gravel with a particle size of 2-4 cm, and two components decompose and infiltrate the wetland pool (36) adopt shale and ceramsite respectively, wherein the decomposed percolation layer (38) of one group of decomposition and percolation wetland pools (36) adopts the shale of particle size 4-8cm, another group of decomposition percolation wetland tanks (36 ) The decomposition percolation layer (38) adopts the ceramsite of particle diameter 2-4cm. the
分解渗滤层(38)的上表面种植水陆两栖的种植物(23),种植物(23)的根系扎根在分解渗滤层(38)内,种植物(23)为芦苇、黄花鸢尾、香蒲、再力花、黑三菱,至少种植1种,分解渗滤层(38)的填料基质为微生物提供附着载体,微生物在种植物的根系和填料基质表面形成微生物膜,通过种植物(23)吸收去除水体中的污染物,并随着种植物(23)的收割将污染物移出多级潜流湿地处理单元(4),溶氧水体在流动的过程中流经进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)分解渗滤层(38)的表层和底层制成排放水体。 Amphibious plants (23) are planted on the upper surface of the decomposed percolation layer (38), and the roots of the plants (23) are rooted in the decomposed percolation layer (38). , Zailihua, and Black Mitsubishi, plant at least one species, decompose the filler matrix of the percolation layer (38) to provide an attachment carrier for the microorganisms, and the microorganisms form a microbial film on the root system of the plant and the surface of the filler matrix, which is absorbed by the plant (23) Remove the pollutants in the water body, and move the pollutants out of the multi-stage subsurface flow wetland treatment unit (4) as the plants (23) are harvested, and the dissolved oxygen water flows through the inflow wetland pool (35), 2 groups The surface layer and the bottom layer of the decomposed percolation layer (38) are decomposed into the discharge water body by decomposing the percolation wetland pond (36) and the effluent wetland pond (37). the
多级潜流湿地处理单元(4)一端的池壁上部沿池壁安设收水管(21),收水管(21)安设在分解渗滤层(38)内,收水管(21)的一端与蓄积排放池(25)的进水口(13)相连接,收水管(21)的出水端部设置闸阀,控制排出的水量,收水管(21)把收集的水体输入到蓄积排放池(25)内。 The upper part of the pool wall at one end of the multi-stage subsurface flow wetland treatment unit (4) is provided with a water collection pipe (21) along the pool wall, and the water collection pipe (21) is installed in the decomposed percolation layer (38), and one end of the water collection pipe (21) is connected to the The water inlets (13) of the storage and discharge tanks (25) are connected, and gate valves are set at the outlet end of the water collection pipe (21) to control the amount of discharged water. The water collection pipe (21) inputs the collected water into the storage and discharge tank (25) . the
多级潜流湿地处理单元(4)另一端的池壁上部沿池壁设置布水管(19),布水管(19)安设在分解渗滤层(38)内,布水管(19)的一端与曝气增氧处理单元(3)的出水口(12)相连接,布水管(19)的进水端部设置闸阀,控制进水量,把经过曝气增氧处理单元(3)溶氧后的水体均匀的流出撒布在进水湿地池(35)的分解渗滤层(38)内。 The upper part of the pool wall at the other end of the multi-stage subsurface flow wetland treatment unit (4) is provided with a water distribution pipe (19) along the pool wall, and the water distribution pipe (19) is installed in the decomposed percolation layer (38), and one end of the water distribution pipe (19) is connected to the The water outlets (12) of the aeration and oxygenation treatment unit (3) are connected, and the water inlet end of the water distribution pipe (19) is provided with a gate valve to control the water intake, and the oxygen dissolved in the aeration and oxygenation treatment unit (3) The water body evenly flows out and spreads in the decomposed percolation layer (38) of the water inlet wetland pool (35). the
多级潜流湿地处理单元(4)的一端的一侧设置蓄积排放池(25),蓄积排放池(25)整体呈箱形,蓄积排放池(25)的池壁与多级潜流湿地处理单元(4)的出水湿地池(37)的池壁相连接,与出水湿地池(37)相邻的蓄积排放池(25)的池壁上设置进水口(13),蓄积排放池(25)的进水口(13)与出水湿地池(37)的收水管(21)相连通,蓄积排放池(25)一端的池壁上设置排放管(26),把经过处理后的排放水体通过排放管(26)排放到河道或湖泊。 One side of one end of the multi-stage subsurface flow wetland processing unit (4) is provided with an accumulation discharge pond (25), the accumulation discharge pond (25) is in a box shape as a whole, and the pool wall of the accumulation discharge pond (25) is in contact with the multistage subsurface flow wetland treatment unit ( 4) The pool wall of the water outlet wetland pool (37) is connected, and the water inlet (13) is set on the pool wall of the accumulation discharge pool (25) adjacent to the water outlet wetland pool (37), and the inlet of the accumulation discharge pool (25) The water outlet (13) is connected with the water collection pipe (21) of the outlet wetland pool (37), and the discharge pipe (26) is arranged on the pool wall at one end of the accumulation discharge pond (25), and the discharged water body after treatment is passed through the discharge pipe (26) ) into rivers or lakes. the
多级潜流湿地处理单元(4)一侧的中部设置检修放空控制井(28),检修放空控制井(28)整体呈箱形,检修放空控制井(28)内设置放空管(22),放空管(22)贯穿检修放空控制井(28)的一侧井壁,在多级潜流 湿地处理单元(4)的进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)一侧底部设置检修放空管(24),检修放空管(24)与进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)相贯通,检修放空管(24)与检修放空控制井(28)内的放空管(22)相连接并贯通,检修放空管(24)上设置控制闸阀构成检修放空管路,通过检修放空管路放空进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)检修多级潜流湿地处理单元(4)。 The middle part of one side of the multi-stage subsurface flow wetland treatment unit (4) is provided with an inspection and maintenance venting control well (28). The venting pipe (22) runs through one side well wall of the maintenance venting control well (28), in the influent wetland pool (35), the 2-component decomposition percolation wetland pool (36) and the multi-stage subsurface flow wetland treatment unit (4). The bottom of one side of the outlet wetland pool (37) is provided with a maintenance vent pipe (24), and the maintenance vent pipe (24) is connected to the water inlet wetland pool (35), the 2-component decomposition and percolation wetland pool (36) and the outlet wetland pool (37) ), the maintenance vent pipe (24) is connected and connected with the vent pipe (22) in the maintenance vent control well (28), and a control gate valve is set on the maintenance vent pipe (24) to form a maintenance vent pipeline. The multi-stage subsurface flow wetland treatment unit (4) is overhauled by venting the inlet wetland pool (35), the 2-component decomposition percolation wetland pool (36) and the outlet wetland pool (37) through the maintenance and venting pipeline. the
溶氧清液水体进入多级潜流湿地处理单元(4)的流向是从布水管(19)进入进水湿地池(35),利用水体的自重流经2组分解渗滤湿地池(36)进入出水湿地池(37),由收水管(21)收起输入到排放蓄积池(25)内,溶氧水体在流动的过程中实现反复经过好氧、厌氧、硝化和反硝化的反应过程制成排放水体,如图1、图2、图6所示。 The flow direction of the dissolved oxygen clear liquid water entering the multi-stage subsurface flow wetland treatment unit (4) is from the water distribution pipe (19) into the water inlet wetland pool (35), and the self-weight of the water body flows through the two-component decomposition and percolation wetland pool (36) into the The effluent wetland pool (37) is collected and input into the discharge storage tank (25) by the water collection pipe (21), and the dissolved oxygen water body realizes the reaction process of aerobic, anaerobic, nitrification and denitrification repeatedly in the process of flowing. into discharge water bodies, as shown in Figure 1, Figure 2, and Figure 6. the
实施例7 Example 7
污水源通过管路从多级沉淀预处理单元(1)的沉淀分解池(6)的进污口(11)进入沉淀分解池(6)内,污水源中夹带着一定量的悬浮物、漂浮物和泥沙,污水源所含杂质的比重不同,污水源进入沉淀分解池(6)后形成上浮的浮渣、中层的污水水体和下沉的沉渣,沉淀分解池(6)的密闭构成厌氧环境,污水源含有的蛋白性有机物通过厌氧发酵而分解,并产生氨等物质,杀灭寄生虫卵及病菌,实现沉淀、分解、发酵、灭菌污水处理,由于水体重力的作用沉淀分解池(6)内的中层污水水体从设置在隔墙(33)中部的过流管(9)的入口进入过流管(9),从高于过流管(9)的出口自流进入发酵沉淀池(7)内。 The sewage source enters the sedimentation decomposition tank (6) from the sewage inlet (11) of the sedimentation decomposition tank (6) of the multi-stage sedimentation pretreatment unit (1) through the pipeline, and a certain amount of suspended solids, floating Matter and sediment, the specific gravity of the impurities contained in the sewage source is different. After the sewage source enters the sedimentation and decomposition tank (6), it will form floating scum, middle sewage water and sinking sediment. The closed sedimentation and decomposition tank (6) will form an exhaust Oxygen environment, the proteinaceous organic matter contained in the sewage source is decomposed by anaerobic fermentation, and produces ammonia and other substances, killing parasite eggs and germs, realizing precipitation, decomposition, fermentation, and sterilized sewage treatment, due to the action of water gravity. The middle sewage water body in the decomposition tank (6) enters the overflow pipe (9) from the inlet of the overflow pipe (9) arranged in the middle of the partition wall (33), and flows into the fermentation pipe from the outlet higher than the overflow pipe (9) In the sedimentation tank (7). the
进入发酵沉淀池(7)内的污水水体进一步的发酵、沉淀,发酵沉淀池(7)与沉淀分解池(6)相比浮渣和悬浮物的数量相对减少,污水水体处于比较静止状态,发酵和分解的程度较低,有利于污水水体中的浮渣和悬浮物继续实现发酵、分解和沉淀,污水水体又经发酵、沉淀后由于水体重力的作用发酵沉淀池(7)内中层的污水液从设置在隔墙(33)中部的过流管(9)的入口进入过流管(9),从高于过流管(9)的出口自流进入蓄积池(8)内。 The sewage water body in the fermentation sedimentation tank (7) is further fermented and precipitated. Compared with the sedimentation decomposition tank (6), the amount of scum and suspended matter in the fermentation sedimentation tank (7) is relatively reduced, and the sewage water body is in a relatively static state. The degree of decomposition and decomposition is low, which is conducive to the continuous fermentation, decomposition and precipitation of scum and suspended matter in the sewage water body. After the sewage water body is fermented and precipitated, the sewage in the middle layer of the fermentation sedimentation tank (7) is fermented due to the gravity of the water. The liquid enters the overflow pipe (9) from the inlet of the overflow pipe (9) arranged in the middle of the partition wall (33), and flows into the accumulator (8) from the outlet higher than the overflow pipe (9). the
进入蓄积池(8)内的污水液再进一步的分离和沉淀,存储在蓄积池(8)内污水液中层以上清液,残余的浮渣和悬浮物沉入池底,随着污水液不断的进入蓄积池(8),蓄积池(8)的污水液的水位也不断升高,污水液的上层清液从安设在池壁上部的出水口(12)通过管道(14)自流到多级水解氧化单元(2),从多级水解氧化单元(2)的池壁下部的进水口(13)进入多级水解氧化单元(2)内,污水源经过多级沉淀预处理单元(1)的多级处理去除浮渣、悬浮物和沉渣,通过发酵、分解、沉淀和储存杀灭寄生虫卵、病原微生物和细菌,达到了无害化的设计要求,污水源经过多级沉淀预处理单元(1)预处理制成污水清液,污水清液进入多级水解酸化处理单元(2)。 The sewage liquid entering the storage tank (8) is further separated and precipitated, and is stored in the supernatant above the middle layer of the sewage liquid in the storage tank (8), and the remaining scum and suspended matter sink to the bottom of the tank. Entering the storage tank (8), the water level of the sewage liquid in the storage tank (8) also continues to rise, and the supernatant liquid of the sewage liquid flows from the water outlet (12) installed on the upper part of the tank wall through the pipeline (14) to the multi-stage The hydrolytic oxidation unit (2) enters the multi-stage hydrolytic oxidation unit (2) from the water inlet (13) at the lower part of the pool wall of the multi-stage hydrolytic oxidation unit (2), and the sewage source passes through the multi-stage sedimentation pretreatment unit (1) Multi-stage treatment removes scum, suspended matter and sediment, kills parasite eggs, pathogenic microorganisms and bacteria through fermentation, decomposition, precipitation and storage, and meets the design requirements of harmlessness. The sewage source passes through a multi-stage sedimentation pretreatment unit ( 1) The sewage clear liquid is prepared by pretreatment, and the sewage clear liquid enters the multi-stage hydrolysis acidification treatment unit (2). the
多级水解酸化处理单元(2)由隔板(33)分隔成至少3个空间,分为进水水解氧化池(39)、水解氧化池(40)和出水水解氧化池(41),隔板(33) 的上部安设L形过水管(16),进水水解氧化池(39)、水解氧化池(40)和出水水解氧化池(41)中安设水解过滤层(29),水解过滤层(29)的水解滤料的表面附着生物膜形态生长的微生物群体。 The multi-stage hydrolytic acidification treatment unit (2) is divided into at least 3 spaces by a partition (33), which is divided into an influent hydrolysis oxidation pool (39), a hydrolysis oxidation pool (40) and an outlet water hydrolysis oxidation pool (41). The upper part of (33) installs L-shaped water-passing pipe (16), installs hydrolysis filter layer (29) in the water inlet hydrolysis oxidation tank (39), hydrolysis oxidation tank (40) and outlet water hydrolysis oxidation tank (41), and hydrolysis filter layer (29) The surface of the hydrolyzed filter material adheres to the microbial population growing in the form of a biofilm. the
污水清液从多级水解酸化处理单元(2)底部的进水口(13)进入进水水解氧化池(39)的水解过滤层(29)底部,随着污水清液的不断流入进水水解氧化池(39)的水解过滤层(29)内,水解过滤层(29)内污水清液的水位不断提升,污水清液的水位漫过进水水解氧化池(39)的水解过滤层(29),上升到进水水解氧化池(39)的上部,达到安设在隔板(33)上部的L形过流管(16)的出水口,污水清液经过进水水解氧化池(39)的水解过滤层(29)的水解氧化后,通过L形过流管(16)从进水水解氧化池(39)进入水解氧化池(40)的水解过滤层(29)的底部。 The sewage clear liquid enters the bottom of the hydrolysis filter layer (29) of the influent hydrolysis oxidation tank (39) from the water inlet (13) at the bottom of the multi-stage hydrolysis acidification treatment unit (2), and as the sewage clear liquid continuously flows into the influent water, it is hydrolyzed and oxidized In the hydrolysis filter layer (29) of the pool (39), the water level of the sewage clear liquid in the hydrolysis filter layer (29) is continuously raised, and the water level of the sewage clear liquid overflows the hydrolysis filter layer (29) of the influent hydrolysis oxidation tank (39). , rise to the top of the influent hydrolysis oxidation tank (39), reach the water outlet of the L-shaped overflow pipe (16) that is installed on the dividing plate (33) top, and the sewage clear liquid passes through the water inflow hydrolysis oxidation tank (39) After the hydrolytic oxidation of the hydrolytic filter layer (29), enter the bottom of the hydrolytic filter layer (29) of the hydrolytic oxidation tank (40) from the influent hydrolytic oxidation tank (39) through the L-shaped overcurrent pipe (16). the
随着污水清液的不断流入水解氧化池(40)的水解过滤层(29)内,水解过滤层(29)内污水清液的水位不断提升,污水清液的水位漫过水解氧化池(40)的水解过滤层(29),上升到水解氧化池(40)的上部,达到安设在隔板(33)上部的L形过流管(16)的出水口,污水清液再次经过水解氧化池(40)的水解过滤层(29)的水解氧化后,通过L形过流管(16)从水解氧化池(40)进入出水水解氧化池(41)的水解过滤层(29)的底部。 Along with the continuous flow of sewage clear liquid into the hydrolysis filter layer (29) of the hydrolysis oxidation tank (40), the water level of the sewage clear liquid in the hydrolysis filter layer (29) is continuously promoted, and the water level of the sewage clear liquid overflows the hydrolysis oxidation tank (40 ) of the hydrolysis filter layer (29), rises to the top of the hydrolysis oxidation tank (40), and reaches the water outlet of the L-shaped overcurrent pipe (16) installed on the top of the partition (33), and the sewage clear liquid is once again hydrolyzed and oxidized After the hydrolytic oxidation of the hydrolytic filter layer (29) of the pool (40), enter the bottom of the hydrolytic filter layer (29) of the effluent hydrolytic oxidation tank (41) from the hydrolytic oxidation tank (40) by the L-shaped overflow pipe (16). the
随着污水清液的不断流入出水水解氧化池(41)的水解过滤层(29)内,水解过滤层(29)内污水清液的水位不断提升,污水清液的水位漫过出水水解氧化池(41)的水解过滤层(29),上升到出水水解氧化池(41)的上部,达到安设在多级水解酸化处理单元(2)的池壁上部的出水口(12),污水清液再一次经过出水水解氧化池(41)的水解过滤层(29)的水解氧化后,通过池壁上部的出水口(12)进入集水出水池(5),污水清液通过多级水解酸化处理单元(2)的水解过滤层(29),在流经水解过滤层(29)的过程中水解滤料的表面附着的微生物群体截留、吸附及代谢分解污水清液中的有机物,同时,多级水解酸化处理单元(2)形成的密闭厌氧环境,对蛋白性有机物实施厌氧发酵,分解蛋白性有机物并产生氨等物质,起到杀灭寄生虫卵及病菌的作用,将高分子有机物降解为低分子有机物,有机氮降解为无机氮、有机磷降解为无机磷,有利于后续多级潜流湿地处理单元(4)的快速降解,提高湿地处理对污染物的去除效率。 As the sewage clear liquid continuously flows into the hydrolysis filter layer (29) of the effluent hydrolysis oxidation tank (41), the water level of the sewage clear liquid in the hydrolysis filter layer (29) continues to rise, and the water level of the sewage clear liquid overflows the effluent hydrolysis oxidation tank The hydrolysis filter layer (29) of (41) rises to the top of the effluent hydrolysis oxidation tank (41), reaches the water outlet (12) that is installed on the top of the pool wall of the multistage hydrolysis acidification treatment unit (2), and the sewage clear liquid After passing through the hydrolysis and oxidation of the hydrolysis filter layer (29) of the effluent hydrolysis oxidation tank (41) again, it enters the water collection effluent tank (5) through the water outlet (12) on the upper part of the pool wall, and the sewage clear liquid is treated by multi-stage hydrolysis and acidification The hydrolysis filter layer (29) of the unit (2), in the process of flowing through the hydrolysis filter layer (29), the microbial population attached to the surface of the hydrolysis filter material intercepts, absorbs and metabolizes the organic matter in the sewage clear liquid, and at the same time, the multi-stage The airtight anaerobic environment formed by the hydrolysis and acidification treatment unit (2) implements anaerobic fermentation on proteinaceous organic matter, decomposes proteinaceous organic matter and produces ammonia and other substances, plays a role in killing parasite eggs and germs, and degrades high-molecular organic matter It is low-molecular organic matter, organic nitrogen is degraded to inorganic nitrogen, and organic phosphorus is degraded to inorganic phosphorus, which is beneficial to the rapid degradation of the subsequent multi-stage subsurface flow wetland treatment unit (4), and improves the removal efficiency of wetland treatment for pollutants. the
污水清液经过多级水解酸化处理单元(2)的水解氧化处理制成无害水体,无害水体蓄积在集水出水池(5)内,随着无害水体的不断蓄积,安设在集水出水池(5)内的潜水泵(31)通过管路(14)把无害水体提升输送到曝气增氧处理单元(3)内。 The sewage clear liquid is hydrolyzed and oxidized by the multi-stage hydrolysis and acidification treatment unit (2) to make harmless water, which is accumulated in the water collection outlet pool (5). The submersible pump (31) in the water outlet pool (5) lifts the harmless water body into the aeration and oxygenation treatment unit (3) through the pipeline (14). the
无害水体从曝气增氧处理单元(3)的进水口(13)进入到曝气增氧处理单元(3)内,曝气增氧处理单元(3)的曝气机(18)通过主干管(34)和曝气管(30)对无害水体实施曝气增氧处理制成溶氧水体,对无害水体实施曝气增氧处理是无害水体中的溶解氧含量,为多级潜流湿地处理单元(4)内的好氧微生物提供氧源。 Harmless water enters the aeration and oxygenation treatment unit (3) from the water inlet (13) of the aeration and oxygenation treatment unit (3), and the aerator (18) of the aeration and oxygenation treatment unit (3) passes through the trunk Pipe (34) and aeration pipe (30) carry out aeration and oxygenation treatment to harmless water body to make dissolved oxygen water body, carry out aeration and oxygenation treatment to harmless water body is the dissolved oxygen content in the harmless water body, is multi-level Aerobic microorganisms in the subsurface wetland treatment unit (4) provide an oxygen source. the
随着曝气增氧处理单元(3)内溶氧水体的不断增加,溶氧水体从出水口(12)通过管路(14)自流进入多级潜流湿地处理单元(4)的布水管(19),布水管(19)均匀的把溶氧水体撒布在多级潜流湿地处理单元(4)的进水湿地池(35)的分解渗滤层(38)内,随着溶氧水体的水体重力作用充满进水湿地池(35)的分解渗滤层(38),进水湿地池(35)内的水位不断升高,溶氧水体从隔板(33)下部的水平过流管(20)进入其中一组分解渗滤湿地池(36)内的底部,溶氧水体不断的涌入其中一组分解渗滤湿地池(36)并充满另一组分解渗滤湿地池(36)。 With the continuous increase of the dissolved oxygen water body in the aeration and oxygenation treatment unit (3), the dissolved oxygen water body flows from the water outlet (12) through the pipeline (14) into the water distribution pipe (19) of the multi-stage subsurface flow wetland treatment unit (4). ), the water distributing pipe (19) evenly spreads the dissolved oxygen water body in the decomposition and percolation layer (38) of the inflow wetland pool (35) of the multi-stage subsurface flow wetland treatment unit (4), with the water weight of the dissolved oxygen water body Force action fills the decomposed percolation layer (38) of the water inlet wetland pool (35), the water level in the water inlet wetland pool (35) continues to rise, and the dissolved oxygen water passes through the horizontal flow pipe (20 ) into the bottom of one set of decomposition and percolation wetland pools (36), dissolved oxygen water continuously pours into one set of decomposition and percolation wetland pools (36) and fills another set of decomposition and percolation wetland pools (36). the
溶氧水体充满其中一组分解渗滤湿地池(36)的分解渗滤层(38),其中一组分解渗滤湿地池(36)内的水位不断升高,随着溶氧水体的水位升高并漫过隔板(33)的顶端,溶氧水体从隔板(33)顶端进入另一组分解渗滤湿地池(36),溶氧水体的不断流入充满另一组分解渗滤湿地池(36)的分解渗滤层(38),另一组分解渗滤湿地池(36)内的水位不断升高,随着溶氧水体的水体重力作用从隔板(33)下部的水平过流管(20)进入出水湿地池(37)的分解渗滤层(38)内,溶氧水体不断的涌入出水湿地池(37)的分解渗滤层(38)并充满出水湿地池(37),出水湿地池(37)内的水位不断升高,随着溶氧水体的水位升高达到收水管(21)的位置。 The dissolved oxygen water body is filled with the decomposing and percolating layer (38) of one group of decomposing and percolating wetland ponds (36), and the water level in one group of decomposing and percolating wetland ponds (36) is constantly rising, and as the water level of the dissolved oxygen water body rises, High and over the top of the partition (33), the dissolved oxygen water enters another group of decomposition and infiltration wetland pools (36) from the top of the partition (33), and the continuous inflow of the dissolved oxygen water fills another group of decomposition and filtration wetland pools (36 ), the water level in the other group of decomposition and filtration wetland pools (36) is constantly rising, and the horizontal flow pipe at the bottom of the clapboard (33) will (20) enter the decomposed percolation layer (38) of the effluent wetland pool (37), and the dissolved oxygen water continuously pours into the decomposed percolation layer (38) of the effluent wetland pool (37) and fills the effluent wetland pool (37), The water level in the effluent wetland pool (37) rises continuously, and reaches the position of the water collection pipe (21) along with the rise of the water level of the dissolved oxygen water body. the
溶氧水体进入多级潜流湿地处理单元(4),流经进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)的分解渗滤层(38)形成波浪式的流动,进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)的分解渗滤层(38)构成“基质--植物--微生物”生态系统,种植物的根系扎根于分解渗滤层(38)的表层,分解渗滤层(38)的填料基质为微生物提供附着的载体,种植物的根系为微生物提供氧源,在靠近根区的填料基质层形成好氧区,远离根区的填料基质层形成厌氧区或兼氧区,溶氧水体在流动的过程中流经分解渗滤层(38)的表层和底层,反复经过好氧、厌氧、硝化和反硝化的反应过程,实施高效去除溶氧水体中的有机污染物和氮磷制成排放水体,排放水体收入收水管(21)内,排放水体从收水管(21)进入排放蓄积池(25)内蓄积,再由排放管(26)排放到河道或湖泊,如图1、图2、图3、图4、图5、图6所示。 The dissolved oxygen water enters the multi-stage subsurface flow wetland treatment unit (4), flows through the decomposition and percolation layer (38) of the influent wetland pool (35), the two-component decomposition and percolation wetland pool (36) and the outlet wetland pool (37) to form Wave-like flow, the decomposed percolation layer (38) of the influent wetland pool (35), the two-component decomposed percolation wetland pool (36) and the outlet wetland pool (37) constitutes a "matrix-plant-microbe" ecosystem , the root system of the plant is rooted in the surface layer of the decomposed percolation layer (38), the filler matrix of the decomposed percolation layer (38) provides a carrier for the microorganisms to attach to, the root system of the plant provides the oxygen source for the microorganisms, and the filler near the root zone The matrix layer forms an aerobic zone, and the filler matrix layer away from the root zone forms an anaerobic zone or a facultative zone. The oxygen-dissolved water flows through the surface and bottom layer of the decomposed percolation layer (38) during the flow, and repeatedly passes through the aerobic and anaerobic zones. Oxygen, nitrification and denitrification reaction process, implement efficient removal of organic pollutants and nitrogen and phosphorus in the dissolved oxygen water body to make discharge water body, the discharge water body is collected in the water collection pipe (21), and the discharge water body enters the discharge accumulation from the water collection pipe (21) Accumulate in the pond (25), discharge to river course or lake by discharge pipe (26) again, as shown in Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6. the
实施例8 Example 8
当溶氧水体在多级潜流湿地处理单元(4)中运行过程中,通过检测观察竖井(27)观测进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)的运行情况是否达到设计要求,从检测观察竖井(27)中抽取水样进行检测水质是否达到设计要求,及时调节布水管(19)上的闸阀,控制进水量,抑制分解渗滤层(38)中的水流速度,调整分解渗滤层(38)处于最佳分解状态,如图1、图2、图6所示。 When the dissolved oxygen water body is running in the multi-stage subsurface flow wetland treatment unit (4), the inflow wetland pool (35), the 2-component decomposition and infiltration wetland pool (36) and the outlet wetland pool ( 37) whether the operation status meets the design requirements, take water samples from the detection and observation shaft (27) to test whether the water quality meets the design requirements, adjust the gate valve on the water distribution pipe (19) in time, control the water intake, and inhibit the decomposition of the percolation layer ( 38) in the water velocity, adjust and decompose the percolation layer (38) to be in the optimum decomposition state, as shown in Fig. 1, Fig. 2 and Fig. 6. the
实施例9 Example 9
当溶氧水体在多级潜流湿地处理单元(4)中运行过程中,通过检测观察竖井(27)观测进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池 (37)的运行情况是否达到设计要求,从检测观察竖井(27)中抽取水样进行检测水质是否达到设计要求,及时调节布水管(19)上的闸阀,控制进水量,抑制分解渗滤层(38)中的水流速度,调整分解渗滤层(38)处于最佳分解状态,如图1、图2、图6所示。 When the dissolved oxygen water body is running in the multi-stage subsurface flow wetland treatment unit (4), the inflow wetland pool (35), the 2-component decomposition and infiltration wetland pool (36) and the outlet wetland pool ( 37) whether the operation status meets the design requirements, take water samples from the detection and observation shaft (27) to test whether the water quality meets the design requirements, adjust the gate valve on the water distribution pipe (19) in time, control the water intake, and inhibit the decomposition of the percolation layer ( 38) in the water velocity, adjust and decompose the percolation layer (38) to be in the optimum decomposition state, as shown in Fig. 1, Fig. 2 and Fig. 6. the
实施例10 Example 10
当多级沉淀预处理单元(1)运行一段时间后沉淀分解池(6)、发酵沉淀池(7)和蓄积池(8)内的底部沉淀了沉渣,依照设计要求需要对沉淀分解池(6)、发酵沉淀池(7)和蓄积池(8)实施清渣、清淤,关闭进污口(11)的管路(14)上的闸阀,停止污水源的流入,关闭出水口(12)的管路(14)上的闸阀,停止污水处理后的污水源的流出。打开沉淀分解池(6)、发酵沉淀池(7)和蓄积池(8)顶部清渣口(10)的密封盖,清除沉淀分解池(6)、发酵沉淀池(7)和蓄积池(8)内的沉渣和淤泥,清除过流管(9)、进污口(11)和出水口(12)内壁上的附着污垢,保持畅通。关闭沉淀分解池(6)、发酵沉淀池(7)和蓄积池(8)顶部清渣口(10)的密封盖,打开进污口(11)的管路(14)上的闸阀和出水口(12)的管路(14)上的闸阀,启动多级沉淀预处理单元(1)恢复运行,如图1、图2、图3所示。 When the multi-stage sedimentation pretreatment unit (1) runs for a period of time, the bottom of the sedimentation and decomposition tank (6), the fermentation sedimentation tank (7) and the storage tank (8) has deposited sediment, and the sedimentation and decomposition tank (6) needs to be adjusted according to the design requirements. ), the fermentation sedimentation tank (7) and the storage tank (8) implement slag removal and desilting, close the gate valve on the pipeline (14) of the sewage inlet (11), stop the inflow of the sewage source, and close the water outlet (12) The gate valve on the pipeline (14) stops the outflow of the sewage source after the sewage treatment. Open the sealing cover of the slag removal port (10) on the top of the precipitation decomposition tank (6), the fermentation sedimentation tank (7) and the storage tank (8), and remove the precipitation decomposition tank (6), the fermentation sedimentation tank (7) and the storage tank (8) ), remove the attached dirt on the inner wall of the overflow pipe (9), the sewage inlet (11) and the water outlet (12), and keep it unimpeded. Close the sealing cover of the sedimentation and decomposition tank (6), the fermentation sedimentation tank (7) and the slag removal port (10) at the top of the storage tank (8), open the gate valve and the water outlet on the pipeline (14) of the sewage inlet (11) The gate valve on the pipeline (14) of (12) starts the multi-stage precipitation pretreatment unit (1) to resume operation, as shown in Fig. 1 , Fig. 2 and Fig. 3 . the
实施例11 Example 11
当多级水解酸化处理单元(2)运行一段时间后依照设计要求对进水水解氧化池(39)、水解氧化池(40)、出水水解氧化池(41)和集水出水池(5)实施检修和维护,关闭进水口(13)的管路(14)上的闸阀,停止清液污水水体的流入,排空多级水解酸化处理单元(2)内的无害水体,关闭出水口(12)的管路(14)上的闸阀,开启潜水泵(31)排空集水出水池(5)内的无害水体,关闭潜水泵(31)。打开进水水解氧化池(39)、水解氧化池(40)和出水水解氧化池(41)的顶部检修口(15)上的密封盖,对进水水解氧化池(39)、水解氧化池(40)和出水水解氧化池(41)实施检修和维护,清洗集水出水池(5)的池壁上的附着污垢,清洗L形过流管(16)、进水口(13)和出水口(12)内壁上的附着污垢,保持通畅,检修和维护潜水泵(31)。检修和维护结束后,关闭进水水解氧化池(39)、水解氧化池(40)和出水水解氧化池(41)的顶部检修口(15)上的密封盖,打开进水口(13)的管路(14)上的闸阀出水口(12)的管路(14)上的闸阀,启动多级水解酸化处理单元(2)恢复运行,如图1、图2、图4所示。 After the multi-stage hydrolysis and acidification treatment unit (2) has been in operation for a period of time, the influent hydrolysis oxidation pond (39), the hydrolysis oxidation pond (40), the effluent hydrolysis oxidation pond (41) and the water collection and discharge pond (5) are implemented according to the design requirements. Overhaul and maintenance, close the gate valve on the pipeline (14) of the water inlet (13), stop the inflow of the clear liquid sewage water body, empty the harmless water body in the multi-stage hydrolysis acidification treatment unit (2), close the water outlet (12 ) on the pipeline (14), open the submersible pump (31) to empty the harmless water body in the water collection outlet pool (5), and close the submersible pump (31). Open the sealing cover on the top inspection port (15) of the water inlet hydrolysis oxidation pond (39), the hydrolysis oxidation pond (40) and the water outlet hydrolysis oxidation pond (41), to the water inlet hydrolysis oxidation pond (39), the hydrolysis oxidation pond ( 40) and the effluent hydrolysis oxidation tank (41) implement overhaul and maintenance, clean the attached dirt on the pool wall of the water collection effluent tank (5), clean the L-shaped overflow pipe (16), water inlet (13) and water outlet ( 12) Adhesive dirt on the inner wall, keep it unobstructed, overhaul and maintain the submersible pump (31). After the overhaul and maintenance are finished, close the sealing cover on the top inspection port (15) of the water inlet hydrolysis oxidation pond (39), the hydrolysis oxidation pond (40) and the outlet water hydrolysis oxidation pond (41), open the pipe of the water inlet (13) The gate valve on the pipeline (14) of the gate valve water outlet (12) on the road (14) starts the multi-stage hydrolysis acidification treatment unit (2) to resume operation, as shown in Figure 1, Figure 2, and Figure 4. the
实施例12 Example 12
当曝气增氧处理单元(3)运行一段时间后依照设计要求对曝气增氧处理单元(3)实施检修和维护,关闭进水口(13)的管路(14)上的闸阀,停止清液污水水体的流入,排空曝气增氧处理单元(3)内的溶氧水体,关闭出水口(12)的管路(14)上的闸阀,清除曝气增氧处理单元(3)的池壁上的附着污垢,清洗主干管(34)和曝气管(30),保持畅通,检修和维护曝气机(18)。开启进水口(13)的管路(14)上的闸阀,注入清液污水水体,开启出水口(12)的管路(14)上的闸阀,贯通向多级潜流湿地处理单元(4)的布水管 (19)输送溶氧水体,开启曝气机(18),通过主干管(34)和曝气管(30)向曝气增氧处理单元(3)内的清液污水水体曝气增氧,曝气增氧处理单元(3)恢复运行,如图1、图2、图5所示。 After the aeration and oxygenation processing unit (3) has been in operation for a period of time, the aeration and oxygenation processing unit (3) is overhauled and maintained according to the design requirements, the gate valve on the pipeline (14) of the water inlet (13) is closed, and the cleaning is stopped. The inflow of the liquid sewage water body, emptying the dissolved oxygen water body in the aeration and aeration treatment unit (3), closing the gate valve on the pipeline (14) of the water outlet (12), clearing the aeration and aeration treatment unit (3) Attach dirt on the pool wall, clean main pipe (34) and aeration pipe (30), keep unimpeded, overhaul and maintain aerator (18). Open the gate valve on the pipeline (14) of the water inlet (13), inject clear liquid and sewage water, open the gate valve on the pipeline (14) of the water outlet (12), and connect to the multi-stage subsurface flow wetland treatment unit (4) The water distribution pipe (19) transports the dissolved oxygen water body, turns on the aerator (18), and aerates the clear liquid sewage water body in the aeration and oxygenation treatment unit (3) through the main pipe (34) and the aeration pipe (30). Oxygen, the aeration and oxygenation treatment unit (3) resumes operation, as shown in Figure 1, Figure 2, and Figure 5. the
实施例13 Example 13
当多级潜流湿地处理单元(4)运行一段时间后分解渗滤层(38)出现阻塞,分解渗滤层(38)中的阻塞物影响分解渗滤层(38)的分解反应,需要对分解渗滤层(38)实施反冲洗,关闭布水管(19)上的闸阀,停止输入溶氧水体,排空收水管(21)内的排放水体,关闭收水管(21)上的闸阀。从反冲洗主干管向反冲洗管路(42)注入反冲洗水源,冲洗分解渗滤层(38),把分解渗滤层(38)中的阻塞物反冲洗到进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)的顶部,出水湿地池(37)的顶部的反冲洗水源和阻塞物通过多级潜流湿地单元(4)上部的反冲洗排空口(32)排出多级潜流湿地单元(4)。停止向反冲洗管路(42)注入反冲洗水源,关闭反冲洗排空口(32),打开进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)的检修放空管(24)上的闸阀,从放空管(22)放空进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)反冲洗水体,关闭进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)的检修放空管(24)上的闸阀,开启布水管(19)上的闸阀,开始输入溶氧水体,开启收水管(21)上的闸阀,多级潜流湿地处理单元(4)恢复运行,如图1、图2、图6所示。 When the multi-stage subsurface flow wetland treatment unit (4) runs for a period of time, the decomposed percolation layer (38) is blocked, and the obstructions in the decomposed percolation layer (38) affect the decomposition reaction of the decomposed percolation layer (38). The percolation layer (38) implements backwashing, closes the gate valve on the water distribution pipe (19), stops inputting the dissolved oxygen water body, empties the discharge water body in the water collection pipe (21), and closes the gate valve on the water collection pipe (21). Inject the backwash water source from the backwash main pipe to the backwash pipeline (42), flush the decomposed percolation layer (38), and backwash the obstruction in the decomposed percolation layer (38) to the influent wetland pool (35), The top of the 2-component decomposition and percolation wetland pool (36) and the outlet wetland pool (37), the backwash water source and obstructions on the top of the outlet wetland pool (37) are emptied through the backwash on the upper part of the multi-stage subsurface flow wetland unit (4) The port (32) discharges the multi-stage subsurface flow wetland unit (4). Stop injecting the backwash water source into the backwash pipeline (42), close the backwash emptying port (32), open the water inlet wetland pool (35), the 2-component decomposition percolation wetland pool (36) and the water outlet wetland pool (37) Check and repair the gate valve on the vent pipe (24), empty the inlet wetland pool (35), the 2-component decomposition percolation wetland pool (36) and the outlet wetland pool (37) to backwash the water body from the vent pipe (22), and close Open the gate valve on the water distribution pipe (19) and start inputting the solution Oxygen water body, open the gate valve on the water collection pipe (21), and the multi-stage subsurface flow wetland treatment unit (4) resumes operation, as shown in Fig. 1, Fig. 2 and Fig. 6 . the
实施例14 Example 14
当多级潜流湿地处理单元(4)长时间运行后,按设计要求需要对多级潜流湿地处理单元(4)进行检修和维护,关闭布水管(19)上的闸阀,停止进水,放空收水管(26)中的排放水,关闭收水管(26)的闸阀,停止出水,打开进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)的检修放空管(24)上的闸阀,从放空管(22)放空进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)污水处理水体,对多级潜流湿地处理单元(4)实施检修和维护。清洗布水管(19)、收水管(21)反冲洗连通口(43)和反冲洗排空口(32)的内壁上附着污垢,清整分解渗滤层(38)上表层的种植物。检修结束,关闭进水湿地池(35)、2组分解渗滤湿地池(36)和出水湿地池(37)的检修放空管(24)上的闸阀,开启布水管(19)上的闸阀,开始进水,开启收水管(26)的闸阀,开始出水,多级潜流湿地处理单元(4)恢复运行,如图1、图2、图6所示。 After the multi-stage subsurface flow wetland treatment unit (4) has been in operation for a long time, it is necessary to overhaul and maintain the multi-stage subsurface flow wetland treatment unit (4) according to the design requirements, close the gate valve on the water distribution pipe (19), stop water intake, and discharge Discharge water in the water pipe (26), close the gate valve of the water collection pipe (26), stop the water outlet, open the inspection and discharge of the water inlet wetland pool (35), the 2-component decomposition percolation wetland pool (36) and the water outlet wetland pool (37) The gate valve on the empty pipe (24) is used to empty the inlet wetland pool (35), the 2-component decomposition infiltration wetland pool (36) and the sewage treatment water body of the outlet wetland pool (37) from the emptying pipe (22), for multi-level subsurface flow The wetland treatment unit (4) implements overhaul and maintenance. Clean the dirt that is attached to the inwall of the water distribution pipe (19), the water collection pipe (21) backwash communication port (43) and the backwash emptying port (32), and clean and decompose the planting on the upper surface of the percolation layer (38). After the maintenance is over, close the gate valves on the maintenance vent pipes (24) of the inlet wetland pool (35), the 2-component decomposition and percolation wetland pool (36) and the outlet wetland pool (37), and open the gate valve on the water distribution pipe (19) , start water intake, open the gate valve of the water collection pipe (26), start water discharge, and the multi-stage subsurface flow wetland processing unit (4) resumes operation, as shown in Fig. 1, Fig. 2 and Fig. 6 . the
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200255318U CN202063793U (en) | 2011-01-26 | 2011-01-26 | Biological response system used for multi-stage sewage treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200255318U CN202063793U (en) | 2011-01-26 | 2011-01-26 | Biological response system used for multi-stage sewage treatment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202063793U true CN202063793U (en) | 2011-12-07 |
Family
ID=45057662
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200255318U Expired - Fee Related CN202063793U (en) | 2011-01-26 | 2011-01-26 | Biological response system used for multi-stage sewage treatment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202063793U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102120677A (en) * | 2011-01-26 | 2011-07-13 | 天津市水利科学研究院 | Biological response system for multistage sewage treatment as well as manufacturing method and sewage treatment method |
| CN102923861A (en) * | 2012-11-30 | 2013-02-13 | 南京大学 | Constructed wetland for treating sewage with low carbon nitrogen ratio by utilizing ores |
| CN104086038A (en) * | 2014-05-26 | 2014-10-08 | 华中农业大学 | Comprehensive processing method for squeezing sewage generated in process of extracting xanthophyll from tagetes erecta |
| CN108609741A (en) * | 2018-05-12 | 2018-10-02 | 农业部沼气科学研究所 | A kind of sewage treatment unit of shallow-layer flowing |
| CN118050300A (en) * | 2024-04-16 | 2024-05-17 | 河北天辰仪器设备有限公司 | Geotextile intelligent vertical permeability coefficient determination method and determination device |
-
2011
- 2011-01-26 CN CN2011200255318U patent/CN202063793U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102120677A (en) * | 2011-01-26 | 2011-07-13 | 天津市水利科学研究院 | Biological response system for multistage sewage treatment as well as manufacturing method and sewage treatment method |
| CN102120677B (en) * | 2011-01-26 | 2012-10-03 | 天津市水利科学研究院 | Biological response system for multistage sewage treatment as well as manufacturing method and sewage treatment method |
| CN102923861A (en) * | 2012-11-30 | 2013-02-13 | 南京大学 | Constructed wetland for treating sewage with low carbon nitrogen ratio by utilizing ores |
| CN102923861B (en) * | 2012-11-30 | 2014-01-22 | 南京大学 | Constructed wetland for treating sewage with low carbon nitrogen ratio by utilizing ores |
| CN104086038A (en) * | 2014-05-26 | 2014-10-08 | 华中农业大学 | Comprehensive processing method for squeezing sewage generated in process of extracting xanthophyll from tagetes erecta |
| CN108609741A (en) * | 2018-05-12 | 2018-10-02 | 农业部沼气科学研究所 | A kind of sewage treatment unit of shallow-layer flowing |
| CN108609741B (en) * | 2018-05-12 | 2023-11-10 | 农业部沼气科学研究所 | Domestic sewage treatment device with shallow flowing layer |
| CN118050300A (en) * | 2024-04-16 | 2024-05-17 | 河北天辰仪器设备有限公司 | Geotextile intelligent vertical permeability coefficient determination method and determination device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102120677B (en) | Biological response system for multistage sewage treatment as well as manufacturing method and sewage treatment method | |
| CN110550829B (en) | Tower ecological purification integrated device of little town domestic sewage | |
| CN101973637B (en) | River channel purification system for processing rural domestic sewage | |
| CN201372233Y (en) | Unpowered Integrated Constructed Wetland Sewage Treatment System | |
| CN104926038B (en) | A kind of biological and ecological composite handling arrangement for rural sewage treatment | |
| CN109020091A (en) | A kind of combined type artificial marsh sewage treatment system and its processing method | |
| CN100400438C (en) | Eutrophic river, lake water body and initial rainwater compound artificial wetland treatment system | |
| CN105254127B (en) | The micro- aeration composite artificial marsh sewage treatment system of self-cleaning type | |
| CN203768124U (en) | Ecological filter for micro-polluted water treatment | |
| CN207468411U (en) | A kind of rural domestic sewage treatment system | |
| CN109607975B (en) | Constructed wetland structure for repairing super-eutrophic water body and endogenous pollution | |
| CN116425346B (en) | Unpowered buried vertical flow wetland rural domestic sewage treatment device and method | |
| CN103951064A (en) | Ecological filter used for micro-polluted water treatment | |
| CN206289121U (en) | Multi-stage ecological tank and ecological pool combined system | |
| CN108128967A (en) | A kind of river water body dystopy comprehensive high-efficiency processing method and system | |
| CN110845084A (en) | Artificial wetland system applied to super-limit purification treatment of low-concentration polluted water body | |
| CN202063793U (en) | Biological response system used for multi-stage sewage treatment | |
| CN102838208A (en) | River channel purifier technology for polluted river water quality improvement | |
| CN105948423A (en) | Sewage treatment system | |
| CN105236687A (en) | Sewage treatment device and method for self-cleaning type micro-aeration vertical baffled wetland | |
| CN109592791B (en) | Composite artificial wetland system and operation method thereof | |
| CN205011588U (en) | Waters sewage treatment plant | |
| CN100464812C (en) | An artificially enhanced land infiltration sewage treatment device | |
| CN206828325U (en) | Septic tank+A20 processing units | |
| CN205740688U (en) | A kind of artificial wet land treating system of residents in rural community percolate |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111207 Termination date: 20130126 |