CN110590080A - A biofilm sewage treatment equipment - Google Patents
A biofilm sewage treatment equipment Download PDFInfo
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- CN110590080A CN110590080A CN201910985044.7A CN201910985044A CN110590080A CN 110590080 A CN110590080 A CN 110590080A CN 201910985044 A CN201910985044 A CN 201910985044A CN 110590080 A CN110590080 A CN 110590080A
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- 239000010865 sewage Substances 0.000 title claims abstract description 77
- 238000000746 purification Methods 0.000 claims abstract description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 238000005189 flocculation Methods 0.000 claims abstract description 20
- 230000016615 flocculation Effects 0.000 claims abstract description 20
- 238000001914 filtration Methods 0.000 claims abstract description 14
- 238000011001 backwashing Methods 0.000 claims abstract description 12
- 239000011941 photocatalyst Substances 0.000 claims abstract description 6
- 239000011148 porous material Substances 0.000 claims abstract description 3
- 238000005273 aeration Methods 0.000 claims description 14
- 241000894006 Bacteria Species 0.000 claims description 9
- 239000012982 microporous membrane Substances 0.000 claims description 6
- 239000007921 spray Substances 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 5
- 239000012528 membrane Substances 0.000 claims description 5
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 claims 1
- 239000000126 substance Substances 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 2
- 241001148470 aerobic bacillus Species 0.000 description 8
- 239000005416 organic matter Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 229920000620 organic polymer Polymers 0.000 description 6
- 239000002957 persistent organic pollutant Substances 0.000 description 6
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 238000012851 eutrophication Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 229910052698 phosphorus Inorganic materials 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 230000001699 photocatalysis Effects 0.000 description 2
- 238000000053 physical method Methods 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 208000035473 Communicable disease Diseases 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 231100001240 inorganic pollutant Toxicity 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physical Water Treatments (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本发明涉及污水处理技术领域,具体来说是一种生物膜污水处理设备,包括过滤池、厌氧池、好氧池及收集净化池;过滤池分隔为过滤区及垃圾存储区,过滤区内设置有细孔过滤网板,过滤池的顶部设置有污水入口;厌氧池内设置有若干组厌氧生物膜及絮凝管,好氧池内并排设置有若干好氧生物膜;收集净化池内顶部设置有紫外线灯,收集净化池内相对侧壁上设置有光触媒板,收集净化池的侧壁上还设置有排水管;收集净化池上还设置有反冲洗管,反冲洗管依次贯穿厌氧池、好氧池并向过滤池内部延伸,反冲洗管上设置有反冲洗泵;本发明不仅对污水进行物理过滤法、生物法和化学法进行净化,而且使水发生循环从而实现自净,提升了净水的效果。
The invention relates to the technical field of sewage treatment, in particular to a biofilm sewage treatment equipment, comprising a filter tank, an anaerobic tank, an aerobic tank and a collection and purification tank; the filter tank is divided into a filter area and a garbage storage area, and the filter area A fine-pore filter screen plate is arranged, and a sewage inlet is arranged on the top of the filter tank; several groups of anaerobic biofilms and flocculation pipes are arranged in the anaerobic tank, and several aerobic biofilms are arranged side by side in the aerobic tank; Ultraviolet lamp, photocatalyst plates are arranged on the opposite side walls of the collection and purification tank, and a drainage pipe is also arranged on the side wall of the collection and purification tank; the collection and purification tank is also provided with a backwash pipe, which runs through the anaerobic tank and the aerobic tank in turn. It extends to the inside of the filter tank, and the backwashing pipe is provided with a backwashing pump; the invention not only purifies the sewage by physical filtration, biological and chemical methods, but also circulates the water to realize self-purification and improve the effect of water purification. .
Description
技术领域technical field
本发明涉及污水处理技术领域,具体来说是一种生物膜污水处理设备。The invention relates to the technical field of sewage treatment, in particular to a biological membrane sewage treatment equipment.
背景技术Background technique
生活污水是居民日常生活中排出的废水,主要来源于居住建筑和公共建筑,生活污水所含的污染物主要是有机物,如蛋白质、碳水化合物、脂肪、氨氮等,污水中的细菌和病原体以生活污水中的有机物为营养而大量繁殖,可导致传染病蔓延流行,因此生活污水排放前必须进行处理。Domestic sewage is the wastewater discharged from the daily life of residents, mainly from residential buildings and public buildings. The pollutants contained in domestic sewage are mainly organic substances, such as proteins, carbohydrates, fats, ammonia nitrogen, etc. The organic matter in sewage is multiplied for nutrition, which can lead to the spread of infectious diseases, so domestic sewage must be treated before it is discharged.
污水处理的手段有很多,常见的包括用物理法、化学法和生物法,其中生物膜法是利用附着生长于某些固体物表面的微生物(即生物膜)进行有机污水处理的方法,生物膜是由高度密集的好氧菌、厌氧菌、兼性菌、真菌、原生动物以及藻类等组成的生态系统,生物膜首先吸附污水中的有机物,由好气层的好气菌将其分解,再进入厌气层由厌气菌进行分解。There are many means of sewage treatment, the common ones include physical method, chemical method and biological method. Among them, biofilm method is a method of organic sewage treatment using microorganisms (ie biofilm) attached to the surface of certain solid objects. It is an ecosystem composed of highly dense aerobic bacteria, anaerobic bacteria, facultative bacteria, fungi, protozoa and algae. The anaerobic layer is decomposed by anaerobic bacteria.
现有技术的生物膜污水处理设备往往仅注重了污水的处理,而忽略了在使用时过滤网堵塞及厌氧池和好氧池的清洁问题,此时往往需要人工来对过滤网进行清洗,以及对厌氧池和好氧池进行除杂,不仅增加了人工的消耗,而且容易导致物理过滤时过滤的不够彻底,以及厌氧池和好氧池内的生物膜使用寿命短暂,极大地降低了污水处理时的工作效率。The biofilm sewage treatment equipment in the prior art often only pays attention to the treatment of sewage, and ignores the clogging of the filter screen and the cleaning of the anaerobic tank and the aerobic tank during use. At this time, it is often necessary to manually clean the filter screen. And the removal of impurities in anaerobic and aerobic tanks not only increases labor consumption, but also easily leads to insufficient filtration during physical filtration, and the short service life of biofilms in anaerobic and aerobic tanks, which greatly reduces the Efficiency in sewage treatment.
发明内容SUMMARY OF THE INVENTION
针对上述存在的技术不足,本发明的目的是提供了一种生物膜污水处理设备,不仅对污水进行物理过滤法、生物法和化学法进行净化,而且使水发生循环从而实现自净,提升了净水的效率。In view of the above-mentioned technical deficiencies, the purpose of the present invention is to provide a biofilm sewage treatment equipment, which not only purifies the sewage by physical filtration, biological and chemical methods, but also circulates the water to realize self-purification and improve the cleanliness. water efficiency.
为解决上述技术问题,本发明采用如下技术方案:In order to solve the above-mentioned technical problems, the present invention adopts the following technical solutions:
一种生物膜污水处理设备,包括过滤池、厌氧池、好氧池及收集净化池,所述过滤池与所述厌氧池通过第一流通管贯通连接,所述厌氧池、所述好氧池和所述收集净化池依次通过第二流通管贯通连接;A biofilm sewage treatment equipment, comprising a filter tank, an anaerobic tank, an aerobic tank and a collection and purification tank, the filter tank and the anaerobic tank are connected through a first flow pipe, the anaerobic tank, the The aerobic pool and the collection and purification pool are in turn connected through the second flow pipe;
所述过滤池通过横板由上至下分隔为过滤区及垃圾存储区,所述过滤区内设置有漏斗状的细孔过滤网板,所述细孔过滤网板的底部贯穿所述横板并与所述垃圾存储区连通,所述过滤池的顶部设置有污水入口,所述过滤池下侧还设置有用于排垃圾的出排通道;The filter tank is divided into a filter area and a garbage storage area from top to bottom by a horizontal plate. The filter area is provided with a funnel-shaped fine-porous filter screen plate, and the bottom of the fine-porous filter screen plate penetrates the horizontal plate. and communicate with the garbage storage area, the top of the filter tank is provided with a sewage inlet, and the lower side of the filter tank is also provided with an outlet channel for discharging garbage;
所述厌氧池的内下方水平设置有第一多孔板,所述第一多孔板的顶部并排设置有若干组厌氧生物膜,所述第一多孔板的底部设置填充有天然有机高分子絮凝剂的絮凝管,所述絮凝管上设置有流通孔,所述第一流通管的一端与所述过滤区连通,另一端与所述絮凝管连通,所述好氧池内并排设置有若干好氧生物膜;The bottom of the anaerobic tank is horizontally provided with a first porous plate, the top of the first porous plate is arranged with several groups of anaerobic biofilms side by side, and the bottom of the first porous plate is filled with natural organic A flocculation tube of a polymer flocculant, the flocculation tube is provided with a flow hole, one end of the first flow tube is communicated with the filtration area, and the other end is communicated with the flocculation tube, and the aerobic tank is arranged side by side with Several aerobic biofilms;
所述收集净化池内顶部设置有紫外线灯,所述收集净化池内相对侧壁上设置有光触媒板,所述收集净化池的侧壁上还设置有排水管;The inner top of the collection and purification pool is provided with an ultraviolet lamp, the opposite side walls of the collection and purification pool are provided with photocatalyst plates, and the side walls of the collection and purification pool are also provided with drainage pipes;
所述收集净化池上还设置有反冲洗管,所述反冲洗管依次贯穿所述厌氧池、所述好氧池并向所述过滤池内部延伸,且端部连通设置有喷淋头,所述喷淋头位于所述细孔过滤网板上方,位于所述厌氧池及所述好氧池内的所述反冲洗管上设置有若干透水孔,所述反冲洗管上设置有反冲洗泵;The collection and purification tank is also provided with a backwashing pipe, the backwashing pipe runs through the anaerobic tank and the aerobic tank and extends to the inside of the filter tank in sequence, and the ends are connected with a sprinkler head, so the The sprinkler head is located above the fine-pore filter screen plate, and the backwash pipes located in the anaerobic tank and the aerobic tank are provided with a number of water permeable holes, and the backwash pipes are provided with a backwash pump. ;
所述垃圾出排通道及所述排水管上均设置有阀门。Valves are provided on both the garbage discharge channel and the drain pipe.
优选的,所述过滤池外侧壁上还设置有回流管,所述回流管的一端与所述垃圾存储区连通,另一端与所述过滤区连通,位于所述过滤区内的所述回流管在所述细孔过滤网板上方,所述回流管上设置有单向阀和用于将垃圾存储区内的污水吸入至过滤区内的第二抽水泵,靠近所述垃圾存储区的所述回流管内设置有滤网。Preferably, a return pipe is also provided on the outer side wall of the filter tank, one end of the return pipe is communicated with the garbage storage area, and the other end is communicated with the filter area. The return pipe located in the filter area Above the fine-hole filter screen plate, the return pipe is provided with a one-way valve and a second pump for sucking sewage in the garbage storage area into the filter area. A filter screen is arranged in the return pipe.
优选的,所述第一流通管上设置有第一抽水泵。Preferably, a first pump is provided on the first circulation pipe.
优选的,所述好氧池内设置有第二多孔板,所述第二多孔板的顶部并排设置有若干所述好氧生物膜,所述第二多孔板的底部设置有呈蛇形排列的曝气管,所述曝气管的任一端贯穿所述好氧池的侧壁向外延伸,并与排气泵的排气口连接,伸入至所述好氧池内的所述曝气管上设置有排气孔。Preferably, a second perforated plate is arranged in the aerobic tank, a plurality of the aerobic biofilms are arranged side by side on the top of the second perforated plate, and a serpentine shape is arranged at the bottom of the second perforated plate Arranged aeration pipes, either end of the aeration pipes extends outward through the side wall of the aerobic tank, and is connected with the exhaust port of the exhaust pump, extending into the aeration pipe in the aerobic tank A vent hole is provided on the pipe.
优选的,所述曝气管内、位于所述排气泵与所述好氧池之间还设置有用于将外界细菌进行过滤的微孔膜过滤器。Preferably, a microporous membrane filter for filtering external bacteria is further provided in the aeration pipe and between the exhaust pump and the aerobic tank.
优选的,每组所述厌氧生物膜均由的两个厌氧生物瓣膜组成,且所述厌氧生物瓣膜呈十字交叉设置。Preferably, each group of the anaerobic biological membranes is composed of two anaerobic biological valves, and the anaerobic biological valves are arranged in a crisscross pattern.
优选的,所述收集净化池的侧壁上还设置有控制器及控制面板,所述排气泵、所述反冲洗泵、所述第一抽水泵、所述第二抽水泵、所述紫外线灯及所述控制面板分别与所述控制器电性连接,所述控制器与外接电源电性连接。Preferably, a controller and a control panel are also provided on the side wall of the collection and purification tank, the exhaust pump, the backwash pump, the first suction pump, the second suction pump, the ultraviolet lamp and the control panel is respectively electrically connected to the controller, and the controller is electrically connected to an external power supply.
优选的,所述厌氧池的底部侧壁上设置有挂环,所述絮凝管通过所述挂环在所述厌氧池的底部呈弓形排列。Preferably, a hanging ring is provided on the bottom side wall of the anaerobic tank, and the flocculation tube is arranged in an arcuate shape at the bottom of the anaerobic tank through the hanging ring.
优选的,所述第二流通管上还设置有控制阀门。Preferably, a control valve is also provided on the second flow pipe.
与现有技术相比,本发明具有的有益效果是:Compared with the prior art, the present invention has the following beneficial effects:
1、本发明设置有过滤池、厌氧池、好氧池及收集净化池,过滤池内进行通过物理法进行过滤,厌氧池内通过厌氧菌分解污水中呈胶体和溶解状态的有机污染物质,使污水的有机污染物达到排放标准,且厌氧池内设置填充有天然有机高分子絮凝剂的絮凝管,天然有机高分子絮凝剂不仅不会对厌氧菌和好氧菌造成伤害,而且能够辅助吸附污水中的杂质,同时厌氧池中每组厌氧生物膜均由两个厌氧生物瓣膜组成,且厌氧生物瓣膜呈十字交叉设置,增大了与污水的接触面积,提高了污水处理效率;好氧池中的好氧生物膜进一步去除难降解的有机物及氮、磷等能够导致水体富营养化的可溶性无机物等,使污水的无机污染物达到排放标准,好氧池内底部设置有曝气管,由微孔膜过滤器过滤外界细菌后的空气由排气泵和曝气管排入至好氧池内,不仅便于好氧池内的好氧菌的生长而且吹入的气体使好氧池内的污水发生搅动,也提升了污水处理的效率,且不会使厌氧生物膜和好氧生物膜上的好氧菌和厌氧菌发生脱落,增大了好氧菌和厌氧菌对污水的氧化作用;最后在收集净化池内通过紫外线灯和光触媒板实现了光催化作用,将未分解的有机物进行氧化分解,破坏细菌的细胞膜和固化病毒的蛋白质,同时杀灭细菌和分解有机污染物,把有机污染物分解成无污染的水和二氧化碳,对污水中的有机物和无机物进行了有效的去除。1. The present invention is provided with a filter tank, an anaerobic tank, an aerobic tank and a collection and purification tank, the filter tank is filtered by a physical method, and the anaerobic bacteria decompose the organic pollutants in the colloidal and dissolved state in the sewage in the anaerobic tank, The organic pollutants in the sewage meet the discharge standard, and the anaerobic tank is equipped with a flocculation tube filled with natural organic polymer flocculants. Absorb impurities in sewage, and at the same time, each group of anaerobic biofilms in the anaerobic tank is composed of two anaerobic biological valves, and the anaerobic biological valves are arranged in a crisscross pattern, which increases the contact area with sewage and improves sewage treatment. Efficiency; the aerobic biofilm in the aerobic tank further removes refractory organic matter and soluble inorganic substances such as nitrogen and phosphorus that can lead to eutrophication of the water body, so that the inorganic pollutants in the sewage meet the discharge standard. The aeration pipe, the air after filtering the external bacteria by the microporous membrane filter is discharged into the aerobic tank by the exhaust pump and the aeration pipe, which not only facilitates the growth of aerobic bacteria in the aerobic tank, but also makes the air in the aerobic tank easy to blow. The aerobic and anaerobic bacteria on the anaerobic biofilm and aerobic biofilm will not fall off, which increases the effect of aerobic and anaerobic bacteria on sewage. Finally, in the collection and purification tank, the photocatalytic effect is realized through the ultraviolet lamp and the photocatalyst plate, the undecomposed organic matter is oxidized and decomposed, the cell membrane of the bacteria and the protein of the solidified virus are destroyed, and the bacteria are killed and decomposed. Organic pollutants, The organic pollutants are decomposed into pollution-free water and carbon dioxide, and the organic and inorganic substances in the sewage are effectively removed.
2、本发明还设置有反冲洗泵和反冲洗管,且反冲洗管的另一端依次贯穿厌氧池、好氧池并向过滤池内部延伸,且端部连通设置有喷淋头,喷淋头位于细孔过滤网板上方,位于厌氧池及好氧池内的反冲洗管上设置有若干透水孔,当反冲洗泵运行时,污水经由反冲洗管和喷淋头由过滤池的顶部及透水孔喷出,实现了对细孔过滤网板的冲洗,也实现了对厌氧池及好氧池的冲洗,从而无需人工将细孔过滤网板拆洗而进行拆洗,降低了人工的消耗,且冲洗后的污水还会经由上述的过滤池、厌氧池、好氧池及收集净化池再次进行净化,实现了污水的二次利用,也避免了细孔过滤网板的网孔堵塞问题,增大了净水的效率。2. The present invention is also provided with a backwash pump and a backwash pipe, and the other end of the backwash pipe runs through the anaerobic tank and the aerobic tank and extends into the filter tank in turn, and the end is connected with a spray head, which sprays The head is located above the fine-hole filter screen plate, and the backwash pipe located in the anaerobic tank and the aerobic tank is provided with a number of permeable holes. The water permeable hole is sprayed out, which realizes the flushing of the fine-porous filter screen plate, and also realizes the flushing of the anaerobic tank and aerobic tank, so that there is no need to manually disassemble and wash the fine-porous filter screen plate for disassembly and washing, which reduces labor consumption. And the washed sewage will be purified again through the above-mentioned filter tank, anaerobic tank, aerobic tank and collection purification tank, realizing the secondary utilization of sewage and avoiding the problem of mesh blockage of the fine-porous filter screen. Increase the efficiency of water purification.
附图说明Description of drawings
图1为本发明一种生物膜污水处理设备的内部结构剖视图;1 is a cross-sectional view of the internal structure of a biofilm sewage treatment equipment of the present invention;
图2为本发明一种生物膜污水处理设备的外部结构图;Fig. 2 is the external structure diagram of a kind of biofilm sewage treatment equipment of the present invention;
图3为本发明一种生物膜污水处理设备的絮凝管排布俯视图;3 is a top view of the arrangement of the flocculation pipes of a biofilm sewage treatment equipment according to the present invention;
图4为本发明一种生物膜污水处理设备的电连接关系图。FIG. 4 is an electrical connection diagram of a biofilm sewage treatment equipment according to the present invention.
附图标记说明:Description of reference numbers:
1、过滤池;2、厌氧池;3、好氧池;4、收集净化池;5、第一流通管;6、控制器;7、控制面板;8、横板;9、过滤区;10、垃圾存储区;11、细孔过滤网板;12、污水入口;13、第一多孔板;14、厌氧生物膜;15、絮凝管;16、第一抽水泵;17、第二多孔板;18、好氧生物膜;19、紫外线灯;20、光触媒板;21、排水管;22、喷淋头;23、反冲洗管;24、反冲洗泵;25、微孔膜过滤器;26、出排通道;27、回流管;28、单向阀;29、第二抽水泵;30、滤网;31、曝气管;32、排气泵。1. Filter tank; 2. Anaerobic tank; 3. Aerobic tank; 4. Collection purification tank; 5. First flow pipe; 6. Controller; 7. Control panel; 8. Horizontal plate; 9. Filter area; 10. Garbage storage area; 11. Fine-porous filter screen plate; 12. Sewage inlet; 13. The first porous plate; 14. Anaerobic biofilm; 15. Flocculation tube; 16. The first pump; Porous plate; 18, aerobic biofilm; 19, ultraviolet lamp; 20, photocatalyst plate; 21, drain pipe; 22, sprinkler head; 23, backwash pipe; 24, backwash pump; 25, microporous membrane filtration 26, outlet channel; 27, return pipe; 28, one-way valve; 29, second suction pump; 30, filter screen; 31, aeration pipe; 32, exhaust pump.
具体实施方式Detailed ways
下面结合本发明实施例中的附图,用以较佳的实施例及附图1-4配合详细的说明。The following is a detailed description of the preferred embodiment and accompanying drawings 1-4 in conjunction with the accompanying drawings in the embodiments of the present invention.
一种生物膜污水处理设备,包括过滤池1、厌氧池2、好氧池3及收集净化池4,过滤池1内将污水中的杂质和污水进行物理分离,厌氧池2用于将污水中呈胶体和溶解状态的有机污染物质通过厌氧菌分解,好氧池3能够去除难降解的有机物及氮、磷等能够导致水体富营养化的可溶性无机物,收集净化池4用于将未分解的有机物分解成水和二氧化碳再进行排放,过滤池1与厌氧池2通过第一流通管5贯通连接,厌氧池2、好氧池3和收集净化池4通过第二流通管贯通连接,污水通过第一流通管5及第二流通管由过滤池1、厌氧池2、好氧池3及收集净化池4依次流通。A biofilm sewage treatment equipment, including a filter tank 1, an anaerobic tank 2, an aerobic tank 3 and a collection and purification tank 4, the filter tank 1 physically separates impurities in the sewage from the sewage, and the anaerobic tank 2 is used to The organic pollutants in the colloidal and dissolved state in the sewage are decomposed by anaerobic bacteria, the aerobic tank 3 can remove the refractory organic matter and the soluble inorganic substances such as nitrogen and phosphorus that can lead to eutrophication of the water body, and the collection and purification tank 4 is used for Undecomposed organic matter is decomposed into water and carbon dioxide and then discharged. The filter tank 1 and the anaerobic tank 2 are connected through the first flow pipe 5, and the anaerobic tank 2, the aerobic tank 3 and the collection purification tank 4 are connected through the second flow pipe. Connected, the sewage flows from the filter tank 1, the anaerobic tank 2, the aerobic tank 3 and the collection and purification tank 4 through the first flow pipe 5 and the second flow pipe in sequence.
过滤池1的顶部设置有污水入口12,污水由污水入口12进入至过滤池1内,过滤池1由横板8由上至下分隔为过滤区9及垃圾存储区10,过滤区9内设置有漏斗状的细孔过滤网板11,过滤区9内的细孔过滤网板11将污水和杂质进行分离,使得污水位于横板8上,第一流通管5上设置有第一抽水泵16,在第一抽水泵16的辅助作用下,污水经由第一流通管5进入厌氧池2内,细孔过滤网板11的底部贯穿横板8并与垃圾存储区10贯通,此时污水中的杂质及部分污水进入至垃圾存储区10内;过滤池1外侧壁上还设置有回流管27,回流管27的一端与垃圾存储区10连通,另一端与过滤区9连通,垃圾存储区10内的污水经由回流管27被吸入至过滤区9内,位于过滤区9内的回流管27在细孔过滤网板11上方,回流管27上设置有单向阀28和用于将垃圾存储区10内的污水吸入至过滤区9内的第二抽水泵29,单向阀28使得污水在回流管27内只能够由垃圾存储区10进入过滤区9内,靠近垃圾存储区10的回流管27内设置有滤网30,滤网30用于将垃圾存储区10内的污水与垃圾进行分离,便于将垃圾存储区10内的水经由回流管27流入至过滤池1内再次进行过滤,位于垃圾存储区10的过滤池1侧壁上还设置有用于排垃圾的出排通道26。The top of the filter tank 1 is provided with a sewage inlet 12. The sewage enters the filter tank 1 from the sewage inlet 12. The filter tank 1 is divided into a filter area 9 and a garbage storage area 10 by the horizontal plate 8 from top to bottom. There is a funnel-shaped fine-porous filter screen plate 11, and the fine-pored filter screen plate 11 in the filter area 9 separates sewage and impurities, so that the sewage is located on the horizontal plate 8, and the first circulation pipe 5 is provided with a first pump 16. , under the assistance of the first pump 16, the sewage enters the anaerobic tank 2 through the first circulation pipe 5, and the bottom of the fine-porous filter screen plate 11 penetrates the horizontal plate 8 and communicates with the garbage storage area 10. The impurities and part of the sewage enter the garbage storage area 10; the outer side wall of the filter tank 1 is also provided with a return pipe 27, one end of the return pipe 27 is communicated with the garbage storage area 10, and the other end is communicated with the filter area 9, and the garbage storage area 10 The sewage inside is sucked into the filter area 9 through the return pipe 27. The return pipe 27 in the filter area 9 is above the fine-hole filter screen plate 11. The sewage in 10 is sucked into the second pump 29 in the filter area 9, and the one-way valve 28 makes the sewage in the return pipe 27 only enter the filter area 9 from the garbage storage area 10, and is close to the return pipe 27 of the garbage storage area 10. A filter screen 30 is arranged inside, and the filter screen 30 is used to separate the sewage in the garbage storage area 10 from the garbage, so as to facilitate the water in the garbage storage area 10 to flow into the filter tank 1 through the return pipe 27 to be filtered again. The side wall of the filter tank 1 of the storage area 10 is also provided with a discharge channel 26 for discharging garbage.
厌氧池2的底部设置有第一多孔板13,第一多孔板13的顶部并排设置有若干组厌氧生物膜14,厌氧生物膜14上的厌氧菌分解污水中呈胶体和溶解状态的有机污染物质,每组厌氧生物膜14均由的两个厌氧生物瓣膜组成,且厌氧生物瓣膜呈十字交叉,增大了厌氧生物膜14与污水的接触面积,提高了厌氧微生物的净水效率,第一多孔板13的底部设置填充有天然有机高分子絮凝剂的絮凝管15,絮凝管15上设置有流通孔,第一多孔板13及流通孔便于絮凝管15内的有机高分子絮凝剂对污水中的有机物进行絮凝,第一流通管5的一端穿管过滤池1的侧壁并向过滤区9内延伸,另一端贯穿厌氧池2的侧壁并与絮凝管15贯通;厌氧池2的底部侧壁上设置有挂环,絮凝管15通过挂环在厌氧池2的底部呈弓形排列,增大了与污水的接触面积,且絮凝管15内的天然有机高分子絮凝剂的主要成分为天然有机高分子,不仅不会污染厌氧微生物,而且实现了辅助净水的目的。The bottom of the anaerobic tank 2 is provided with a first perforated plate 13, and the top of the first perforated plate 13 is provided with several groups of anaerobic biofilms 14 side by side. Dissolved organic pollutants, each group of anaerobic biofilms 14 is composed of two anaerobic biological valves, and the anaerobic biological valves are crossed, which increases the contact area between the anaerobic biofilm 14 and the sewage, and improves the The water purification efficiency of anaerobic microorganisms, the bottom of the first porous plate 13 is provided with a flocculation tube 15 filled with a natural organic polymer flocculant, and the flocculation tube 15 is provided with a flow hole, and the first porous plate 13 and the flow hole are convenient for flocculation The organic polymer flocculant in the pipe 15 flocculates the organic matter in the sewage. One end of the first flow pipe 5 penetrates the side wall of the filter tank 1 and extends into the filter area 9, and the other end penetrates the side wall of the anaerobic tank 2. And it is connected with the flocculation tube 15; the bottom side wall of the anaerobic tank 2 is provided with a hanging ring, and the flocculation pipe 15 is arranged in an arcuate shape at the bottom of the anaerobic tank 2 through the hanging ring, which increases the contact area with the sewage, and the flocculation pipe The main component of the natural organic polymer flocculant in 15 is natural organic polymer, which not only does not pollute anaerobic microorganisms, but also achieves the purpose of assisting water purification.
好氧池3内并排设置有若干好氧生物膜18,好氧池3内设置有第二多孔板17,第二多孔板17的顶部并排设置有若干好氧生物膜18,好氧生物膜18上的好氧菌进一步去除难降解的有机物及氮、磷等能够导致水体富营养化的可溶性无机物等,第二多孔板17的底部设置有呈蛇形排列的曝气管31,曝气管31的任一端贯穿好氧池3的侧壁向外延伸,并与排气泵32的排气口连接,伸入至好氧池3内的曝气管32上设置有排气孔,排气泵能够向好氧池3内吹入空气,不仅为好氧池3内的好氧菌提供氧气,而且使得好氧池3内的污水发生搅动,增大了好氧生物膜14与污水的接触面积,提高了好氧微生物的净水效率;排气泵32与好氧池3之间的曝气管31内设置有微孔膜过滤器25,微孔膜过滤器25能够过滤空气中的菌种,避免空气中的细菌进入至好氧池3中,从而影响到好氧池3中好氧菌的生长。A number of aerobic biofilms 18 are arranged side by side in the aerobic tank 3, a second porous plate 17 is arranged in the aerobic tank 3, and a number of aerobic biofilms 18 are arranged side by side on the top of the second perforated plate 17. The aerobic bacteria on the membrane 18 further removes the refractory organic matter and the soluble inorganic matter that can lead to eutrophication of the water body, such as nitrogen and phosphorus. Either end of the aeration pipe 31 extends outward through the side wall of the aerobic tank 3, and is connected with the exhaust port of the exhaust pump 32, and an exhaust hole is provided on the aeration pipe 32 extending into the aerobic tank 3, The exhaust pump can blow air into the aerobic tank 3, which not only provides oxygen for the aerobic bacteria in the aerobic tank 3, but also agitates the sewage in the aerobic tank 3, which increases the difference between the aerobic biofilm 14 and the sewage. The contact area improves the water purification efficiency of aerobic microorganisms; a microporous membrane filter 25 is arranged in the aeration pipe 31 between the exhaust pump 32 and the aerobic tank 3, and the microporous membrane filter 25 can filter bacteria in the air. It can prevent the bacteria in the air from entering the aerobic tank 3, thereby affecting the growth of aerobic bacteria in the aerobic tank 3.
收集净化池4上还设置有反冲洗管23,反冲洗管23依次贯穿厌氧池2、好氧池3并向过滤池1内部延伸,位于收集净化池4的处理后的水经由反冲洗管23进入至过滤池1、厌氧池2及好氧池3内,并对过滤池1、厌氧池2及好氧池3进行清洗,且反冲洗管23端部连通设置有喷淋头22,喷淋头22位于细孔过滤网板11上方,处理后的水经由喷淋头22喷洒而出,并通过处理后的水对细孔过滤网板11进行冲洗,实现了细孔过滤网板11自净的目的,有效避免了细孔过滤网板11的堵塞,增大了净水的效率;位于厌氧池2及好氧池3内的反冲洗管23上设置有若干透水孔,处理后的水经由透水孔进入至厌氧池2及好氧池3内,并对厌氧池2及好氧池3进行清洗,反冲洗管23上设置有反冲洗泵24,反冲洗泵24便于处理后的水进入至过滤池1、厌氧池2及好氧池3内;收集净化池4的侧壁上还设置有控制器6及控制面板7,控制面板7上设置有开关,排气泵32、反冲洗泵24、第一抽水泵16、第二抽水泵29、紫外线灯19及控制面板7分别与控制器6电性连接,控制器6与外接电源电性连接,外接电源给用电器供电;本发明中的控制器6的型号为:MAM-100,控制面板7的型号为:LL86-4J-LN,排气泵32的型号为:4A12B25R37,反冲洗泵24的型号为:ISG50-160,第一抽水泵16的吸力高于第二抽水泵29,第一抽水泵16的型号为:GD32-20,第二抽水泵16的型号为:NMDP41。The collection and purification tank 4 is also provided with a backwash pipe 23. The backwash pipe 23 runs through the anaerobic tank 2 and the aerobic tank 3 and extends to the interior of the filter tank 1 in turn. The treated water located in the collection and purification tank 4 passes through the backwash pipe. 23 enters the filter tank 1, the anaerobic tank 2 and the aerobic tank 3, and cleans the filter tank 1, the anaerobic tank 2 and the aerobic tank 3, and the end of the backwash pipe 23 is connected with a spray head 22 , the shower head 22 is located above the fine hole filter screen plate 11, the treated water is sprayed out through the shower head 22, and the fine hole filter screen plate 11 is washed by the treated water, so as to realize the fine hole filter screen plate 11. The purpose of self-cleaning can effectively avoid the blockage of the fine-porous filter screen plate 11 and increase the efficiency of water purification; the backwash pipes 23 located in the anaerobic tank 2 and the aerobic tank 3 are provided with a number of permeable holes. The water enters into the anaerobic tank 2 and the aerobic tank 3 through the permeable holes, and cleans the anaerobic tank 2 and the aerobic tank 3. The backwashing pipe 23 is provided with a backwashing pump 24, which is convenient for processing. The back water enters into the filter tank 1, the anaerobic tank 2 and the aerobic tank 3; the side wall of the collection purification tank 4 is also provided with a controller 6 and a control panel 7, the control panel 7 is provided with a switch, an exhaust pump 32 , the backwash pump 24, the first water pump 16, the second water pump 29, the ultraviolet lamp 19 and the control panel 7 are respectively electrically connected to the controller 6, and the controller 6 is electrically connected to an external power supply, and the external power supply supplies power to the electrical appliances The model of the controller 6 in the present invention is: MAM-100, the model of the control panel 7 is: LL86-4J-LN, the model of the exhaust pump 32 is: 4A12B25R37, the model of the backwash pump 24 is: ISG50-160, The suction force of the first suction pump 16 is higher than that of the second suction pump 29 , the model of the first suction pump 16 is: GD32-20, and the model of the second suction pump 16 is: NMDP41.
第二流通管上还设置有控制阀门,厌氧池2与好氧池3之间的控制阀门用于使污水进行充分的好样反应,及便于通过絮凝管15内的天然有机高分子絮凝剂对污水中的杂质进行充分絮凝,好氧池3与收集净化池4之间的控制阀门便于污水在好氧池3通过好氧菌进行充分的分解;垃圾出排通道26及排水管21上均设置有阀门,便于随时排水和排垃圾。The second flow pipe is also provided with a control valve. The control valve between the anaerobic tank 2 and the aerobic tank 3 is used to make the sewage conduct a sufficient good reaction, and to facilitate the passage of the natural organic polymer flocculant in the flocculation pipe 15. The impurities in the sewage are fully flocculated, and the control valve between the aerobic tank 3 and the collection and purification tank 4 facilitates the sewage to be fully decomposed by aerobic bacteria in the aerobic tank 3; A valve is provided to facilitate drainage and waste discharge at any time.
本发明在使用时,将控制器33与电源电性连接,然后使第一抽水泵16、第二抽水泵29及排气泵32发生运行,由污水入口12将污水排入至过滤池1内,污水先经细孔过滤网板11进行过滤,滤液在细孔过滤网板11和横板8之间,滤渣掉入至垃圾存储区10内,并位于垃圾存储区10内的污水还可以经由回流管27被第二抽水泵29吸入至过滤区9内,然后再进行过滤,位于细孔过滤网板11和横板8之间的污水经由絮凝管15进行简单的絮凝的同时,在厌氧池2内进行厌氧反应,当厌氧池2内的厌氧反应进行一定时间后,打开厌氧池2与好氧池3之间的控制阀门,污水流入至好氧池3内并与好氧菌进行反应,待好氧池3内的好氧反应进行一定时间后,打开好氧池3与收集净化池4之间的控制阀门,污水再次进入到净化池,并通过光触媒板20将有机分子进行光催化分解并形成水和二氧化碳,此时得到了纯净的水,纯净的水经由排水管21排出即可,待装置运行一段时间后就需要对过滤池1、厌氧池2及好氧池3进行清洁,此时打开反冲洗泵24的控制开关,使得反冲洗泵24发生运行,并使得收集净化池4内的处理后的水经由反冲洗管23倒流至过滤池1、厌氧池2及好氧池3,位于过滤池1内的处理后的水经由喷淋头22喷淋而下,对细孔过滤网板11进行清洗,清洗后的污水会再有上述操作进行净化即可。When the present invention is in use, the controller 33 is electrically connected to the power supply, and then the first suction pump 16, the second suction pump 29 and the exhaust pump 32 are operated, and the sewage is discharged into the filter tank 1 through the sewage inlet 12, The sewage is first filtered through the fine-hole filter screen plate 11, the filtrate is between the fine-hole filter screen plate 11 and the horizontal plate 8, and the filter residue falls into the garbage storage area 10, and the sewage located in the garbage storage area 10 can also be returned through the backflow. The pipe 27 is sucked into the filter area 9 by the second suction pump 29, and then filtered again. The sewage located between the fine-porous filter screen plate 11 and the horizontal plate 8 is simply flocculated through the flocculation pipe 15, and then in the anaerobic tank. Anaerobic reaction is carried out in 2, when the anaerobic reaction in anaerobic tank 2 is carried out for a certain period of time, the control valve between anaerobic tank 2 and aerobic tank 3 is opened, and sewage flows into aerobic tank 3 and is mixed with aerobic tank 3. The bacteria react, and after the aerobic reaction in the aerobic tank 3 is carried out for a certain period of time, the control valve between the aerobic tank 3 and the collection purification tank 4 is opened, and the sewage enters the purification tank again, and the organic molecules are removed by the photocatalyst plate 20. Photocatalytic decomposition is carried out to form water and carbon dioxide. At this time, pure water is obtained, and the pure water can be discharged through the drain pipe 21. After the device has been running for a period of time, the filter tank 1, the anaerobic tank 2 and the aerobic tank need to be cleaned. 3. Cleaning is carried out, at this time, the control switch of the backwash pump 24 is turned on, so that the backwash pump 24 is operated, and the treated water in the collection purification tank 4 flows back to the filter tank 1 and the anaerobic tank 2 through the backwash pipe 23 And the aerobic tank 3, the treated water located in the filter tank 1 is sprayed down by the spray head 22 to clean the fine-porous filter screen plate 11, and the cleaned sewage will be purified by the above-mentioned operations.
显然,本领域的技术人员可以对本发明进行各种改动和变型而不脱离本发明的精神和范围。这样,倘若本发明的这些修改和变型属于本发明权利要求及其等同技术的范围之内,则本发明也意图包含这些改动和变型在内。It will be apparent to those skilled in the art that various modifications and variations can be made in the present invention without departing from the spirit and scope of the invention. Thus, provided that these modifications and variations of the present invention fall within the scope of the claims of the present invention and their equivalents, the present invention is also intended to include these modifications and variations.
Claims (9)
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Application publication date: 20191220 |