CN206318832U - Sewage treatment unit - Google Patents
Sewage treatment unit Download PDFInfo
- Publication number
- CN206318832U CN206318832U CN201621051235.4U CN201621051235U CN206318832U CN 206318832 U CN206318832 U CN 206318832U CN 201621051235 U CN201621051235 U CN 201621051235U CN 206318832 U CN206318832 U CN 206318832U
- Authority
- CN
- China
- Prior art keywords
- layer
- water
- reaction tower
- bacteria
- sewage treatment
- 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 60
- 241000894006 Bacteria Species 0.000 claims abstract description 47
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 238000006243 chemical reaction Methods 0.000 claims abstract description 29
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 25
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 18
- 239000010457 zeolite Substances 0.000 claims abstract description 18
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 17
- 229910052902 vermiculite Inorganic materials 0.000 claims abstract description 17
- 239000010455 vermiculite Substances 0.000 claims abstract description 17
- 235000019354 vermiculite Nutrition 0.000 claims abstract description 17
- 239000006229 carbon black Substances 0.000 claims abstract description 16
- 239000000945 filler Substances 0.000 claims abstract description 15
- 238000003860 storage Methods 0.000 claims abstract description 13
- 239000010902 straw Substances 0.000 claims abstract description 11
- 238000000746 purification Methods 0.000 claims abstract description 9
- 239000010802 sludge Substances 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims description 18
- 238000005273 aeration Methods 0.000 claims description 15
- 238000005276 aerator Methods 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 9
- 239000012528 membrane Substances 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 5
- 239000001301 oxygen Substances 0.000 claims description 5
- 239000003814 drug Substances 0.000 claims description 3
- 229940079593 drug Drugs 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 2
- 238000012856 packing Methods 0.000 claims 2
- 229910052698 phosphorus Inorganic materials 0.000 abstract description 11
- 239000011574 phosphorus Substances 0.000 abstract description 11
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 5
- 239000012982 microporous membrane Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 13
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 12
- 239000006004 Quartz sand Substances 0.000 description 6
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 6
- 229910052622 kaolinite Inorganic materials 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000003344 environmental pollutant Substances 0.000 description 5
- 239000003921 oil Substances 0.000 description 5
- 235000019198 oils Nutrition 0.000 description 5
- 231100000719 pollutant Toxicity 0.000 description 5
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 4
- 229910017604 nitric acid Inorganic materials 0.000 description 4
- GQPLMRYTRLFLPF-UHFFFAOYSA-N nitrous oxide Inorganic materials [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- 239000004094 surface-active agent Substances 0.000 description 4
- 238000005188 flotation Methods 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 238000006213 oxygenation reaction Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000007943 implant Substances 0.000 description 2
- 230000020477 pH reduction Effects 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000004912 1,5-cyclooctadiene Substances 0.000 description 1
- 241000190967 Rhodospirillum Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 238000004176 ammonification Methods 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Water Treatment By Sorption (AREA)
Abstract
本实用新型公开一种生活污水处理装置,升压泵一端与贮水箱连接,另一端与反应塔连通,贮水箱入水管与生活污水排放管道相连;反应塔内部空腔顶层设溢流区、底层设水气混合区,反应塔外壁上位于溢流区位置上设排水管,反应塔顶端设排气孔;溢流区与水气混合区之间自上而下依次设蛭石层、聚磷菌附着生长填料层、负载脱氮菌的生物膜层、白炭黑层、沸石层和农作物秸秆层,反应塔外壁上位于负载脱氮菌的生物膜层位置上设污泥排放口;溢流区、蛭石层、聚磷菌附着生长填料层、负载脱氮菌的生物膜层、白炭黑层、沸石层、农作物秸秆层和水气混合区层与层之间通过微孔滤膜阻隔。该处理装置结构简单、使用方便,净化处理效果好,降低污水处理负荷和处理成本。
The utility model discloses a domestic sewage treatment device. One end of a booster pump is connected with a water storage tank, the other end is connected with a reaction tower, and the water inlet pipe of the water storage tank is connected with a domestic sewage discharge pipe; A water-gas mixing zone is set up, a drainage pipe is set on the outer wall of the reaction tower at the position of the overflow zone, and a vent hole is set on the top of the reaction tower; a vermiculite layer and a polyphosphorus layer are sequentially set up between the overflow zone and the water-gas mixing zone from top to bottom. Bacteria attachment growth filler layer, biofilm layer loaded with denitrification bacteria, white carbon black layer, zeolite layer and crop straw layer, and a sludge discharge port is set on the outer wall of the reaction tower at the position of the biofilm layer loaded with denitrification bacteria; overflow zone, vermiculite layer, phosphorus accumulating bacteria attachment growth filler layer, biofilm layer loaded with denitrification bacteria, white carbon black layer, zeolite layer, crop straw layer and water-gas mixed zone layer and layer are separated by microporous membrane . The treatment device has simple structure, convenient use, good purification treatment effect, and reduces sewage treatment load and treatment cost.
Description
技术领域technical field
本实用新型涉及污水处理设备,具体地,涉及生活污水处理装置。The utility model relates to sewage treatment equipment, in particular to a domestic sewage treatment device.
背景技术Background technique
食堂污水的主要污染物为COD、动植物油、表面活性剂(如洗涤剂)、少量的NH3-N和TP。The main pollutants of canteen sewage are COD, animal and vegetable oils, surfactants (such as detergents), a small amount of NH3-N and TP.
目前,食堂生活污水处理甚少,主要是直接排入下水道进入污水处理厂,或者直接接暗管排出,通入地表水体,如流入湖泊、河流或小溪等。即使处理,也是进行简单的隔油处理,如利用油水分离器,进行简单的水、油和固体等分离,然后排放。At present, domestic sewage from canteens is seldom treated. It is mainly discharged directly into the sewer into the sewage treatment plant, or directly connected to the hidden pipe to discharge into surface water bodies, such as lakes, rivers or streams. Even if it is treated, it is a simple oil separation treatment, such as using an oil-water separator to perform simple separation of water, oil and solids, and then discharge.
在现有的专利文献中公开了生活污水的处理装置和方法。如:申请公布号为CN87102257的餐厅污水处理方法中一种处理高浓度有机物污水的新工艺技术,它革新生物接触氧化法,用5-10厘米粒度的煤渣填装在塔式装置内,分四层,每层间距5厘米,以好气菌、红螺菌挂膜,在气水比8-10∶1曝气量下,使污水与空气混合,经过煤渣与生物膜,停留时间在1小时内,可使COD4500毫克/升以下BOD2 000毫克/升以下的污水。又如:申请公布号:CN105712591A的发明公开了一种生活污水处理总站,它包括从左往右顺次设置的格栅渠、酸化调节池、初滤池、厌氧生物滤池、充氧池、好氧生物滤池、终滤池、植物检测池以及放流渠,厌氧生物滤池中的滤料内填装有厌氧生物载体,好氧生物滤池中的滤料内填装有好氧生物载体;每根长管上且沿长管的长度方向顺次设置有多个小孔,放流渠的侧壁上还设置有达标水排放口,所述的格栅渠与酸化调节池连通;充氧池内还固定安装有充氧泵和立柱。本发明的有益效果是:利用微生物吸附降解有机物、出水品质高、能够准确的检测出水的水质情况。Devices and methods for treating domestic sewage are disclosed in existing patent documents. For example: a new process technology for treating high-concentration organic sewage in the restaurant sewage treatment method with the application publication number CN87102257, which innovates the biological contact oxidation method, and fills the tower device with coal slag with a particle size of 5-10 cm, and divides it into four parts. Layers, with a distance of 5 cm between each layer, with aerobic bacteria and Rhodospirillum hanging on the film, under the air-water ratio of 8-10:1 aeration, the sewage is mixed with air, and the residence time is within 1 hour after passing through the cinder and biofilm. , can make the sewage below COD4500 mg/L and BOD2000 mg/L. Another example: Application Publication No.: CN105712591A The invention discloses a domestic sewage treatment terminal, which includes grille canals, acidification adjustment tanks, primary filter tanks, anaerobic biological filter tanks, and oxygenation tanks arranged in sequence from left to right , aerobic biological filter, final filter, plant detection tank and discharge channel, the filter material in the anaerobic biological filter is filled with anaerobic biological carrier, and the filter material in the aerobic biological filter is filled with good Oxygen biological carrier; each long pipe is provided with a plurality of small holes sequentially along the length direction of the long pipe, and the side wall of the release channel is also provided with a standard water discharge port, and the grid channel is connected with the acidification adjustment pool ; An oxygenation pump and a column are also fixedly installed in the oxygenation pool. The beneficial effect of the present invention is: the use of microorganisms to adsorb and degrade organic matters, the quality of effluent water is high, and the water quality of water can be accurately detected.
其中,如餐厅污水处理方法,仅提出了生物处理理论,但对装置或反应器系统涉及较少,甚至未充分考虑处理装置的制备,方法单一,无法去除大部分污染物等。一种生活污水处理总站,程序繁多,过程复杂,成本巨大,基本与城市污水处理厂相似,不适宜在中小规模污水产生量上应用。Among them, such as the restaurant sewage treatment method, only the theory of biological treatment is proposed, but little is involved in the device or reactor system, and the preparation of the treatment device is not even fully considered. The method is single and cannot remove most pollutants. A general domestic sewage treatment station has numerous procedures, complicated processes, and huge costs. It is basically similar to urban sewage treatment plants and is not suitable for application in small and medium-scale sewage production.
因此,急需要提供一种生活污水处理装置,该装置结构简单、成本很低,用于处理污水的材料便宜且易得,完全达标排放,无需再进入城市污水厂管道,直接排入河道,无任何风险。Therefore, there is an urgent need to provide a domestic sewage treatment device. The device has a simple structure and low cost. The materials used to treat sewage are cheap and easy to obtain. any risk.
实用新型内容Utility model content
本实用新型的目的是提供一种生活污水处理装置,该处理装置结构简单、使用方便,净化处理效果好,降低污水处理负荷和处理成本。The purpose of the utility model is to provide a domestic sewage treatment device, which has a simple structure, convenient use, good purification treatment effect, and reduces sewage treatment load and treatment cost.
为了实现上述目的,本实用新型提供了一种生活污水处理装置,包括贮水箱、升压泵和反应塔;升压泵的一端通过管道与贮水箱的出水管相连接,另一端通过管道与反应塔的底端相连通,并且贮水箱的入水管与生活污水排放管道相连接;其中,In order to achieve the above purpose, the utility model provides a domestic sewage treatment device, including a water storage tank, a booster pump and a reaction tower; one end of the booster pump is connected to the outlet pipe of the water storage tank through a pipeline, and the other end is connected to the reaction tower through a pipeline. The bottom of the tower is connected, and the water inlet pipe of the water storage tank is connected with the domestic sewage discharge pipe; wherein,
反应塔内部空腔的顶层设有溢流区、底层设有水气混合区,反应塔外壁上位于溢流区的位置上设有用于排放净化后的污水的排水管,并且反应塔的顶端开设有排气孔;The top layer of the internal cavity of the reaction tower is provided with an overflow area, and the bottom layer is provided with a water-gas mixing area. The outer wall of the reaction tower is located at the position of the overflow area. with vent holes;
溢流区与水气混合区之间自上而下依次设有蛭石层、聚磷菌附着生长填料层、负载脱氮菌的生物膜层、白炭黑层、沸石层和农作物秸秆层,反应塔外壁上位于负载脱氮菌的生物膜层的位置上设有污泥排放口;Between the overflow area and the water-air mixing area, there are vermiculite layer, phosphorus accumulating bacteria attached growth filler layer, biofilm layer loaded with denitrification bacteria, white carbon black layer, zeolite layer and crop straw layer in sequence from top to bottom. A sludge discharge port is provided on the outer wall of the reaction tower at the position of the biofilm layer loaded with denitrification bacteria;
溢流区、蛭石层、聚磷菌附着生长填料层、负载脱氮菌的生物膜层、白炭黑层、沸石层、农作物秸秆层和水气混合区的层与层之间通过微孔滤膜阻隔,并且微孔滤膜只能够供水分子、气分子通过,而净化处理材料无法通透。The overflow area, vermiculite layer, phosphorus accumulating bacteria attachment growth filler layer, biofilm layer loaded with denitrification bacteria, white carbon black layer, zeolite layer, crop straw layer and water-air mixing area pass through micropores between layers The filter membrane is blocked, and the microporous filter membrane can only allow water molecules and gas molecules to pass through, while the purification treatment materials cannot pass through.
优选地,该生活污水处理装置还包括曝气增氧机,水气混合区通过水管与升压泵的另一端相连接,通过气管与曝气增氧机相连接以使得曝气增氧机向水气混合区内通入氧气。Preferably, the domestic sewage treatment device also includes an aeration aerator, the water-air mixing zone is connected to the other end of the booster pump through a water pipe, and connected to the aeration aerator through an air pipe so that the aeration aerator Oxygen is introduced into the water-air mixing zone.
优选地,负载脱氮菌的生物膜层中的脱氮菌包括氨化菌、亚硝酸菌和硝酸菌。Preferably, the denitrification bacteria in the biofilm layer loaded with denitrification bacteria include ammonifying bacteria, nitrous bacteria and nitric acid bacteria.
优选地,沸石层中还填充有活性炭、高岭石和石英砂。Preferably, the zeolite layer is also filled with activated carbon, kaolinite and quartz sand.
优选地,白炭黑层中还填充有活性炭、高岭石和石英砂。Preferably, the silica layer is also filled with activated carbon, kaolinite and quartz sand.
优选地,蛭石层中还填充有活性炭、高岭石和石英砂。Preferably, the vermiculite layer is also filled with activated carbon, kaolinite and quartz sand.
优选地,反应塔外壁上沿高度方向依次设有多个抽屉口,多个抽屉口内均设有相匹配的抽屉,蛭石层、聚磷菌附着生长填料层、负载脱氮菌的生物膜层、白炭黑层和沸石层均设置在抽屉内。Preferably, the outer wall of the reaction tower is sequentially provided with a plurality of drawer openings along the height direction, and matching drawers are arranged in the plurality of drawer openings. , white carbon black layer and zeolite layer are all arranged in the drawer.
优选地,反应塔的顶端还开设有药品投加口。Preferably, the top of the reaction tower is also provided with a drug dosing port.
根据上述技术方案,本实用新型进行污水处理的基本方案为上流式充氧生物膜处理模式,具体为先将食堂生活污水集中起来,进行沉淀或沉砂处理;然后,通过该生活污水处理装置进行物理化学处理,如秸秆吸收动植物浮油、沸石和白炭黑吸附表面活性剂;再引入生物附着曝气氧化处理,如在生物膜上培育氨化菌、亚硝酸菌、硝酸菌,进行脱氮处理,污泥排出;再植入附着生长填料,培养聚磷菌,进行除磷处理;接着利用物理化学处理,如蛭石吸附一些残余物,如微生物残体、填料、其他未处理彻底的污染物等。最后,简单气浮排出处理过程中产生的气体,处理后的污水通过溢流处理排放,可以达到排放标准。通过该生活污水处理装置的上述多步净化,污水的处理效果好,并且结构设备简单、占地面积小,成本低廉,用于处理污水的材料便宜且易得,完全达标排放,无需再进入城市污水厂管道,直接排入河道,无任何风险,大大降低了污水处理负荷和处理成本。According to the above-mentioned technical scheme, the basic scheme of the utility model for sewage treatment is an upflow oxygenated biofilm treatment mode, specifically, the domestic sewage in the canteen is first collected for sedimentation or grit treatment; then, through the domestic sewage treatment device. Physical and chemical treatment, such as straw absorbing animal and plant slick oil, zeolite and white carbon black to adsorb surfactants; and then introducing bio-attachment aeration and oxidation treatment, such as cultivating ammonifying bacteria, nitrous bacteria, and nitric acid bacteria on biofilm to remove Nitrogen treatment, sludge discharge; then implant attached growth filler, cultivate phosphorus accumulating bacteria, and perform phosphorus removal treatment; then use physical and chemical treatment, such as vermiculite to adsorb some residues, such as microbial residues, fillers, and other untreated thorough Pollutants etc. Finally, simple air flotation discharges the gas generated during the treatment process, and the treated sewage is discharged through overflow treatment, which can meet the discharge standard. Through the above-mentioned multi-step purification of the domestic sewage treatment device, the sewage treatment effect is good, and the structural equipment is simple, the floor area is small, the cost is low, the materials used for sewage treatment are cheap and easy to obtain, and the discharge is completely up to standard, and no need to enter the city again Sewage plant pipelines are directly discharged into the river without any risk, which greatly reduces the load and cost of sewage treatment.
本实用新型的其他特征和优点将在随后的具体实施方式部分予以详细说明。Other features and advantages of the present utility model will be described in detail in the following specific embodiments.
附图说明Description of drawings
附图是用来提供对本实用新型的进一步理解,并且构成说明书的一部分,与下面的具体实施方式一起用于解释本实用新型,但并不构成对本实用新型的限制。在附图中:The accompanying drawings are used to provide a further understanding of the utility model, and constitute a part of the description, together with the following specific embodiments, are used to explain the utility model, but do not constitute a limitation to the utility model. In the attached picture:
图1是根据本实用新型提供的一种实施方式中的生活污水处理装置的结构示意图。Fig. 1 is a schematic structural view of a domestic sewage treatment device according to an embodiment of the present invention.
附图标记说明Explanation of reference signs
1-贮水箱 2-升压泵1-Water storage tank 2-Boost pump
3-反应塔 4-溢流区3-Reaction tower 4-Overflow area
5-蛭石层 6-聚磷菌附着生长填料层5- Vermiculite layer 6- Phosphorus accumulating bacteria attachment growth filler layer
7-负载脱氮菌的生物膜层 8-白炭黑层7-Biofilm layer loaded with denitrification bacteria 8-Silica layer
9-沸石层 10-农作物秸秆层9-Zeolite layer 10-Crop straw layer
11-曝气增氧机 12-水气混合区11-Aeration and aeration machine 12-Water-air mixing zone
13-排水管 14-排气孔13-drain pipe 14-vent hole
15-污泥排放口15-Sludge discharge port
具体实施方式detailed description
以下结合附图对本实用新型的具体实施方式进行详细说明。应当理解的是,此处所描述的具体实施方式仅用于说明和解释本实用新型,并不用于限制本实用新型。The specific embodiment of the utility model will be described in detail below in conjunction with the accompanying drawings. It should be understood that the specific embodiments described here are only used to illustrate and explain the utility model, and are not intended to limit the utility model.
在本实用新型中,在未作相反说明的情况下,“上、下”等包含在术语中的方位词仅代表该术语在常规使用状态下的方位,或为本领域技术人员理解的俗称,而不应视为对该术语的限制。In the present utility model, in the case of no contrary description, the orientation words included in the term such as "upper and lower" only represent the orientation of the term in the normal use state, or are commonly known as understood by those skilled in the art, should not be construed as a limitation of this term.
参见图1,本实用新型提供一种生活污水处理装置,包括贮水箱1、升压泵2和反应塔3;升压泵2的一端通过管道与贮水箱1的出水管相连接,另一端通过管道与反应塔3的底端相连通,并且贮水箱1的入水管与生活污水排放管道相连接;其中,Referring to Fig. 1, the utility model provides a domestic sewage treatment device, including a water storage tank 1, a booster pump 2 and a reaction tower 3; one end of the booster pump 2 is connected with the outlet pipe of the water storage tank 1 through a pipeline, and the other end is connected with the outlet pipe of the water storage tank 1 through a pipeline. The bottom end of the pipeline is connected with the reaction tower 3, and the water inlet pipe of the water storage tank 1 is connected with the domestic sewage discharge pipeline; wherein,
反应塔3内部空腔的顶层设有溢流区4、底层设有水气混合区12,反应塔3外壁上位于溢流区4的位置上设有用于排放净化后的污水的排水管13,并且反应塔3的顶端开设有排气孔14;The top floor of the internal cavity of the reaction tower 3 is provided with an overflow area 4, and the bottom layer is provided with a water-gas mixing area 12, and the outer wall of the reaction tower 3 is provided with a drain pipe 13 for discharging purified sewage at the position of the overflow area 4, And the top of the reaction tower 3 is provided with an exhaust hole 14;
溢流区4与水气混合区12之间自上而下依次设有蛭石层5、聚磷菌附着生长填料层6、负载脱氮菌的生物膜层7、白炭黑层8、沸石层9和农作物秸秆层10,反应塔3外壁上位于负载脱氮菌的生物膜层7的位置上设有污泥排放口15;Between the overflow zone 4 and the water-air mixing zone 12, there are vermiculite layer 5, phosphorus accumulating bacteria attachment growth filler layer 6, biofilm layer 7 loaded with denitrification bacteria, white carbon black layer 8, zeolite layer 9 and crop straw layer 10, and a sludge discharge port 15 is provided on the outer wall of the reaction tower 3 at the position of the biofilm layer 7 loaded with denitrification bacteria;
溢流区4、蛭石层5、聚磷菌附着生长填料层6、负载脱氮菌的生物膜层7、白炭黑层8、沸石层9、农作物秸秆层10和水气混合区12的层与层之间通过微孔滤膜阻隔,并且微孔滤膜只能够供水分子、气分子通过,而净化处理材料无法通透。Overflow area 4, vermiculite layer 5, phosphorus accumulating bacteria attachment growth filler layer 6, biofilm layer 7 loaded with denitrification bacteria, white carbon black layer 8, zeolite layer 9, crop straw layer 10 and water-air mixing area 12 The layers are blocked by microporous membranes, and the microporous membranes can only allow water molecules and gas molecules to pass through, while the purification treatment materials cannot pass through.
通过上述技术方案,进行污水处理的基本方案为上流式充氧生物膜处理模式,具体为先将食堂生活污水集中起来,进行沉淀或沉砂处理;然后,通过该生活污水处理装置进行物理化学处理,如秸秆吸收动植物浮油、沸石和白炭黑吸附表面活性剂;再引入生物附着曝气氧化处理,如在生物膜上培育氨化菌、亚硝酸菌、硝酸菌,进行脱氮处理,污泥排出;再植入附着生长填料,培养聚磷菌,进行除磷处理;接着利用物理化学处理,如蛭石吸附一些残余物,如微生物残体、填料、其他未处理彻底的污染物等。最后,简单气浮排出处理过程中产生的气体,处理后的污水通过溢流处理排放,可以达到排放标准。通过该生活污水处理装置的上述多步净化,污水的处理效果好,并且结构设备简单、占地面积小,成本低廉,用于处理污水的材料便宜且易得,完全达标排放,无需再进入城市污水厂管道,直接排入河道,无任何风险,大大降低了污水处理负荷和处理成本。Through the above technical scheme, the basic scheme for sewage treatment is an upflow oxygenated biofilm treatment mode, specifically, the domestic sewage from the canteen is first collected for sedimentation or grit treatment; then, physical and chemical treatment is carried out through the domestic sewage treatment device , such as straw absorbing animal and plant slick oil, zeolite and white carbon black to adsorb surfactants; and then introducing bio-attachment aeration oxidation treatment, such as cultivating ammonifying bacteria, nitrous bacteria, and nitric acid bacteria on biofilm for denitrification treatment, Sludge discharge; then implant attached growth filler, cultivate phosphorus accumulating bacteria, and perform phosphorus removal treatment; then use physical and chemical treatment, such as vermiculite to adsorb some residues, such as microbial residues, fillers, and other pollutants that have not been treated thoroughly. . Finally, simple air flotation discharges the gas generated during the treatment process, and the treated sewage is discharged through overflow treatment, which can meet the discharge standard. Through the above-mentioned multi-step purification of the domestic sewage treatment device, the sewage treatment effect is good, and the structural equipment is simple, the floor area is small, the cost is low, the materials used for sewage treatment are cheap and easy to obtain, and the discharge is completely up to standard, and no need to enter the city again Sewage plant pipelines are directly discharged into the river without any risk, which greatly reduces the load and cost of sewage treatment.
在本实施方式中,为了向水气混合区提供大量的氧气以提高后续吸收、吸附和生物处理的效率,同时提供污水处理过程中产生的气体气提和气浮的动力气体,优选地,该生活污水处理装置还包括曝气增氧机11,水气混合区12通过水管与升压泵2的另一端相连接,通过气管与曝气增氧机11相连接以使得曝气增氧机11向水气混合区12内通入氧气。这样,污水进入后,进行充分混合,混合动力为曝气增氧机11提供,一方面使污染负荷均一化,另一方面可以预处理一些还原性物质,如COD,BOD等。In this embodiment, in order to provide a large amount of oxygen to the water-gas mixing zone to improve the efficiency of subsequent absorption, adsorption and biological treatment, and to provide the motive gas for gas lift and flotation produced in the process of sewage treatment, preferably, the living The sewage treatment plant also includes an aeration aerator 11, the water-air mixing zone 12 is connected to the other end of the booster pump 2 through a water pipe, and is connected to the aeration aerator 11 through a gas pipe so that the aeration aerator 11 Oxygen is introduced into the water-gas mixing zone 12 . In this way, after the sewage enters, it is fully mixed, and the mixed power is provided by the aeration aerator 11. On the one hand, the pollution load can be uniformed, and on the other hand, some reducing substances can be pretreated, such as COD, BOD, etc.
为了进一步地优化附着生长在生物膜上的脱氮菌利用污水中的营养进行代谢生长(即进行脱氮处理)的效果,优选负载脱氮菌的生物膜层7中的脱氮菌包括氨化菌、亚硝酸菌和硝酸菌。In order to further optimize the denitrification bacteria attached to the biofilm to utilize the nutrients in the sewage to carry out metabolic growth (that is, to perform denitrification treatment), it is preferred that the denitrification bacteria in the biofilm layer 7 loaded with denitrification bacteria include ammonification bacteria, nitrous bacteria and nitric acid bacteria.
该处理装置中,用白炭黑层8和沸石层9吸附污水中的表面活性剂以及残余的浮油分子等。为了提高吸附效果,优选沸石层9中还填充有活性炭、高岭石和石英砂,白炭黑层8中也填充有活性炭、高岭石和石英砂。In the treatment device, the white carbon black layer 8 and the zeolite layer 9 are used to adsorb surfactants and residual slick oil molecules in the sewage. In order to improve the adsorption effect, preferably, the zeolite layer 9 is also filled with activated carbon, kaolinite and quartz sand, and the white carbon black layer 8 is also filled with activated carbon, kaolinite and quartz sand.
该处理装置中,用蛭石吸附处理一些残余物,如微生物残体、填料以及其他未处理彻底的污染物,为了提高吸附效率,优选地,蛭石层5中还填充有活性炭、高岭石和石英砂。In this treatment device, some residues are treated with vermiculite adsorption, such as microbial residues, fillers and other untreated pollutants. In order to improve the adsorption efficiency, preferably, the vermiculite layer 5 is also filled with activated carbon, kaolinite and quartz sand.
此外,在长时间进行污水处理后,蛭石层5、聚磷菌附着生长填料层6、负载脱氮菌的生物膜层7、白炭黑层8和沸石层9中的净化材料处理饱和或污染,应该及时取出更换,为了使得更换更加方便快捷,优选地,反应塔3外壁上沿高度方向依次设有多个抽屉口,多个抽屉口内均设有相匹配的抽屉,蛭石层5、聚磷菌附着生长填料层6、负载脱氮菌的生物膜层7、白炭黑层8和沸石层9均设置在抽屉内。In addition, after a long period of sewage treatment, the purification materials in the vermiculite layer 5, the growth filler layer 6 of phosphorus-accumulating bacteria, the biofilm layer 7 loaded with denitrification bacteria, the white carbon black layer 8 and the zeolite layer 9 are saturated or Contamination should be taken out and replaced in time. In order to make the replacement more convenient and quick, preferably, a plurality of drawer openings are arranged along the height direction on the outer wall of the reaction tower 3, and matching drawers are provided in the plurality of drawer openings. The vermiculite layer 5, The growth filler layer 6 for phosphorus accumulating bacteria, the biofilm layer 7 carrying denitrification bacteria, the white carbon black layer 8 and the zeolite layer 9 are all arranged in the drawer.
另外,为了进一步地提高反应塔3中溢流水的洁净程度,便于根据使用需要向溢流区4内添加净化药品,优选地,反应塔3的顶端还开设有药品投加口。In addition, in order to further improve the cleanliness of the overflow water in the reaction tower 3 and facilitate the addition of purification chemicals into the overflow area 4 according to the needs of use, preferably, the top of the reaction tower 3 is also provided with a drug dosing port.
以上结合附图详细描述了本实用新型的优选实施方式,但是,本实用新型并不限于上述实施方式中的具体细节,在本实用新型的技术构思范围内,可以对本实用新型的技术方案进行多种简单变型,这些简单变型均属于本实用新型的保护范围。The preferred embodiment of the utility model has been described in detail above in conjunction with the accompanying drawings, but the utility model is not limited to the specific details of the above-mentioned embodiment, and within the scope of the technical concept of the utility model, the technical solution of the utility model can be carried out in many ways. These simple modifications all belong to the protection scope of the present utility model.
另外需要说明的是,在上述具体实施方式中所描述的各个具体技术特征,在不矛盾的情况下,可以通过任何合适的方式进行组合,为了避免不必要的重复,本实用新型对各种可能的组合方式不再另行说明。In addition, it should be noted that the various specific technical features described in the above specific embodiments can be combined in any suitable way if there is no contradiction. The combination method will not be explained separately.
此外,本实用新型的各种不同的实施方式之间也可以进行任意组合,只要其不违背本实用新型的思想,其同样应当视为本实用新型所公开的内容。In addition, any combination of various implementations of the present invention can also be made, as long as they do not violate the idea of the present invention, they should also be regarded as the disclosed content of the present invention.
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621051235.4U CN206318832U (en) | 2016-09-13 | 2016-09-13 | Sewage treatment unit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621051235.4U CN206318832U (en) | 2016-09-13 | 2016-09-13 | Sewage treatment unit |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206318832U true CN206318832U (en) | 2017-07-11 |
Family
ID=59263461
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621051235.4U Expired - Fee Related CN206318832U (en) | 2016-09-13 | 2016-09-13 | Sewage treatment unit |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206318832U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107265642A (en) * | 2017-07-18 | 2017-10-20 | 上海理工大学 | A kind of drawer type biofilter using composite slow release carbon source as filler |
CN108341491A (en) * | 2018-03-26 | 2018-07-31 | 浙江灵通道路设施股份有限公司 | A kind of binary pot type bacteria bed |
CN108949739A (en) * | 2018-08-15 | 2018-12-07 | 南宁市黄陈生猪养殖场 | A kind of complex micro organism fungicide and preparation method thereof for advanced treating high concentration livestock breeding wastewater |
-
2016
- 2016-09-13 CN CN201621051235.4U patent/CN206318832U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107265642A (en) * | 2017-07-18 | 2017-10-20 | 上海理工大学 | A kind of drawer type biofilter using composite slow release carbon source as filler |
CN108341491A (en) * | 2018-03-26 | 2018-07-31 | 浙江灵通道路设施股份有限公司 | A kind of binary pot type bacteria bed |
CN108949739A (en) * | 2018-08-15 | 2018-12-07 | 南宁市黄陈生猪养殖场 | A kind of complex micro organism fungicide and preparation method thereof for advanced treating high concentration livestock breeding wastewater |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101560039B (en) | Landfill leachate wastewater treatment system and process thereof | |
CN102775025B (en) | Municipal life wastewater treatment system with high efficiency and low energy consumption | |
CN202898159U (en) | Sewage treatment device | |
CN103880193B (en) | Build the method for vertical current constructed wetland processing breeding wastewater based on waterworks sludge | |
CN105502825A (en) | Integrated domestic sewage treatment equipment and treatment method | |
CN201534811U (en) | Multilayer pre-buried microorganism vertical current constructed wetland sewage treatment device | |
CN101293697B (en) | Biological treatment method of sewage and waste gas produced by livestock and poultry breeding | |
CN104045205B (en) | Low-power-consumption integrated water purifying apparatus and water purifying method | |
CN203768124U (en) | Ecological filter for micro-polluted water treatment | |
CN101186416A (en) | Packaged staged membrane bioreactor device for treating sewage or slightly polluted raw water | |
CN103951064A (en) | Ecological filter used for micro-polluted water treatment | |
CN203212433U (en) | Rural sewage treatment system | |
CN201301254Y (en) | Buried type oligodynamic sewage treatment device | |
CN208454743U (en) | An integrated treatment process of drainage biofilm sewage | |
CN206318832U (en) | Sewage treatment unit | |
CN206289126U (en) | A kind of sanitary sewage AAO processing systems | |
CN101885553B (en) | Fixed reproductive microorganism sewage purifying and treating method and device | |
CN104609663B (en) | Ultraviolet irradiation-biomembrane oxidization combination processes the apparatus and method of municipal wastewater | |
CN208562049U (en) | A kind of three-dimensional rural sewage treatment equipment | |
CN110092467A (en) | Utilize the method and its membrane bioreactor of aerobic granular sludge membrane processing landfill leachate | |
WO2014205588A1 (en) | Treatment for domestic and industrial waste water | |
CN106517677B (en) | Quality of reclaimed water landscape water body keeps structure | |
CN202945124U (en) | Urban sewage treatment system with high efficiency and low energy consumption | |
CN205061810U (en) | Garbage leachate treatment system | |
CN201406361Y (en) | A landfill leachate wastewater treatment device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170711 Termination date: 20190913 |
|
CF01 | Termination of patent right due to non-payment of annual fee |