CN206767872U - A kind of Domestic sewage treatment device - Google Patents
A kind of Domestic sewage treatment device Download PDFInfo
- Publication number
- CN206767872U CN206767872U CN201720402264.9U CN201720402264U CN206767872U CN 206767872 U CN206767872 U CN 206767872U CN 201720402264 U CN201720402264 U CN 201720402264U CN 206767872 U CN206767872 U CN 206767872U
- Authority
- CN
- China
- Prior art keywords
- contact oxidation
- tank
- water
- pipe
- sewage
- 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 70
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 239000012528 membrane Substances 0.000 claims abstract description 41
- 230000003647 oxidation Effects 0.000 claims abstract description 40
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 40
- 238000004062 sedimentation Methods 0.000 claims abstract description 23
- 239000000126 substance Substances 0.000 claims abstract description 23
- 238000006243 chemical reaction Methods 0.000 claims abstract description 20
- 238000012856 packing Methods 0.000 claims abstract description 11
- 238000003860 storage Methods 0.000 claims abstract description 11
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 7
- 239000010935 stainless steel Substances 0.000 claims abstract description 7
- 239000000945 filler Substances 0.000 claims description 13
- 238000005273 aeration Methods 0.000 claims description 10
- 238000009826 distribution Methods 0.000 claims description 8
- 239000004744 fabric Substances 0.000 claims description 3
- 239000000835 fiber Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000005516 engineering process Methods 0.000 description 8
- 238000000746 purification Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 238000013461 design Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 3
- 238000009388 chemical precipitation Methods 0.000 description 3
- 229910052698 phosphorus Inorganic materials 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- -1 polypropylene Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 238000000108 ultra-filtration Methods 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 239000004695 Polyether sulfone Substances 0.000 description 1
- 239000006004 Quartz sand Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 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
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000531 effect on virus Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 125000001477 organic nitrogen group Chemical group 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
一种家用污水处理器,包括沿污水行进路线依次设置的可拆卸式滤芯、化学沉淀池、接触氧化池以及膜反应区,其中可拆卸式滤芯侧面带有不锈钢外壳,内部自上而下依次为粗滤层、精滤层和填料滤层,化学沉淀池上方设置有开孔顶板,可拆卸式滤芯上方有污水储室,污水储室的底部为开孔底板,可拆卸式滤芯底部设置于开孔顶板上,顶部通过卡扣卡在开孔底板下,化学沉淀池通过底部的出水口连接接触氧化池的进水管一端,进水管的另一端与接触氧化池内水平设置的开孔式进水管连通,接触氧化池通过底部的排水管与设置有膜组件的膜反应区连通,本实用新型可除去污水中的大小颗粒物、沉淀物和有机磷,实现污水标准化排放,并可实现污水回用,节约水资源。
A domestic sewage processor, including a detachable filter element, a chemical sedimentation tank, a contact oxidation tank, and a membrane reaction area arranged in sequence along the sewage traveling route, wherein the detachable filter element has a stainless steel shell on the side, and the interior is sequentially from top to bottom. Coarse filter layer, fine filter layer and packing filter layer. There is a perforated roof above the chemical sedimentation tank. There is a sewage storage room above the detachable filter element. The bottom of the sewage storage room is a perforated bottom plate. On the top plate of the hole, the top is clamped under the bottom plate of the hole through a buckle. The chemical sedimentation tank is connected to one end of the water inlet pipe of the contact oxidation tank through the water outlet at the bottom, and the other end of the water inlet pipe is connected with the horizontally arranged open-hole water inlet pipe in the contact oxidation tank. , the contact oxidation tank communicates with the membrane reaction zone provided with the membrane module through the drainage pipe at the bottom. water resources.
Description
技术领域technical field
本实用新型属于污水处理技术领域,特别涉及一种家用污水处理器。The utility model belongs to the technical field of sewage treatment, in particular to a household sewage processor.
背景技术Background technique
污水处理设备的改进与创新是当前社会发展和减少水污染的主要方向,我国污水处理技术发展较晚,但也一直致力于污水处理设备的研究。由传统的污水处理技术到现在的生物接触和膜分离技术,取得了重大的进步,提高了污水处理能力和出水质量。目前,国内通常采用曝气管设在填料下的生物接触氧化池技术,接触氧化池和膜是其中的关键技术。The improvement and innovation of sewage treatment equipment is the main direction of current social development and water pollution reduction. The development of sewage treatment technology in my country is relatively late, but it has been committed to the research of sewage treatment equipment. From the traditional sewage treatment technology to the current biological contact and membrane separation technology, significant progress has been made, and the sewage treatment capacity and effluent quality have been improved. At present, the biological contact oxidation tank technology in which the aeration pipe is placed under the filler is usually adopted in China, and the contact oxidation tank and membrane are the key technologies.
对于上述关键技术的研究已经取得了不少进展,但是,现有的污水处理设备研究,多集中在大型专业污水处理领域,适用于工厂、车间等场合,对于家庭使用的小型化污水处理,尚无较好的应用先例。A lot of progress has been made in the research of the above-mentioned key technologies. However, the existing research on sewage treatment equipment is mostly concentrated in the field of large-scale professional sewage treatment, which is suitable for factories, workshops and other occasions. For small-scale sewage treatment for household use, there is still a lot of progress. There is no good application precedent.
发明内容Contents of the invention
为了克服上述现有技术的缺点,本实用新型的目的在于提供一种家用污水处理器,该设备体积小,质量轻,可分步进行污水处理,初级净化装置可以除去污水中的大小颗粒物、沉淀物和有机磷,实现污水的标准化排放,而接触氧化池和膜反应区则可进行进一步高效净化,实现污水回用,从而减少污水排放,节约水资源。In order to overcome the above-mentioned shortcomings of the prior art, the purpose of this utility model is to provide a household sewage processor, which is small in size and light in weight, and can carry out sewage treatment step by step. The primary purification device can remove large and small particles, sediments and and organic phosphorus to realize the standardized discharge of sewage, while the contact oxidation tank and membrane reaction zone can carry out further efficient purification and realize the reuse of sewage, thereby reducing sewage discharge and saving water resources.
为了实现上述目的,本实用新型采用的技术方案是:In order to achieve the above object, the technical solution adopted by the utility model is:
一种家用污水处理器,包括沿污水行进路线依次设置的可拆卸式滤芯1、化学沉淀池2、接触氧化池3以及膜反应区4,其中,所述可拆卸式滤芯1侧面带有不锈钢外壳,内部自上而下依次为粗滤层11、精滤层12和填料滤层13,所述化学沉淀池2上方设置有开孔顶板14,可拆卸式滤芯1上方有污水储室5,污水储室5的底部为开孔底板15,可拆卸式滤芯1底部设置于开孔顶板14上,顶部通过卡扣16卡在开孔底板15下,所述化学沉淀池2通过底部的出水口21连接接触氧化池3的进水管31一端,进水管31的另一端与接触氧化池3内水平设置的开孔式进水管32连通,所述接触氧化池3通过底部的排水管33与设置有膜组件41的膜反应区4连通。A household sewage processor, comprising a detachable filter element 1, a chemical sedimentation tank 2, a contact oxidation tank 3, and a membrane reaction zone 4 arranged sequentially along the sewage traveling route, wherein the detachable filter element 1 has a stainless steel shell on its side , inside from top to bottom are coarse filter layer 11, fine filter layer 12 and packing filter layer 13 successively, the top plate 14 with perforation is arranged on the top of described chemical sedimentation tank 2, there is sewage storage room 5 above detachable filter element 1, sewage The bottom of the storage chamber 5 is a perforated bottom plate 15, the bottom of the detachable filter element 1 is set on the perforated top plate 14, and the top is stuck under the perforated bottom plate 15 through a buckle 16, and the chemical sedimentation tank 2 passes through the water outlet 21 at the bottom One end of the water inlet pipe 31 connected to the contact oxidation tank 3, the other end of the water inlet pipe 31 communicates with the open-hole water inlet pipe 32 arranged horizontally in the contact oxidation tank 3, and the contact oxidation tank 3 connects with the drain pipe 33 at the bottom and is provided with a membrane The membrane reaction zone 4 of the module 41 communicates.
所述粗滤层11由开若干小孔的不锈钢板分层设置而成,层间留有一定的空隙,所述精滤层12为斜纹滤布,所述填料滤层13为纤维填料层。The coarse filter layer 11 is formed by layers of stainless steel plates with a number of small holes, with certain gaps between the layers, the fine filter layer 12 is a twill filter cloth, and the filler filter layer 13 is a fiber filler layer.
所述化学沉淀池2底部设置有填料层22,所述出水口21设置在填料层22下方。A packing layer 22 is arranged at the bottom of the chemical precipitation tank 2 , and the water outlet 21 is arranged below the packing layer 22 .
所述化学沉淀池2上部设置有吸气口23,吸气口23连接有吸气泵25。The upper part of the chemical sedimentation tank 2 is provided with a suction port 23, and the suction port 23 is connected with a suction pump 25.
所述化学沉淀池2中部设置有溢流槽24。An overflow tank 24 is arranged in the middle of the chemical precipitation tank 2 .
所述接触氧化池3中,曝气管34设置在填料下方,曝气管34连接鼓气机35且在连接管路上设置有转子流量计一36,排水管33设置在曝气管34下方。In the contact oxidation tank 3 , the aeration pipe 34 is arranged below the filler, the aeration pipe 34 is connected to the air blower 35 and a rotameter one 36 is arranged on the connecting pipeline, and the drain pipe 33 is arranged below the aeration pipe 34 .
所述接触氧化池3的底部设置有排泥口37,所述排水管33从接触氧化池3的上方经过再接至膜反应区4,其中,排水管33在接触氧化池3上方的部分接有向下的分水管38,分水管38朝向接触氧化池3,在排水管33上位于分水管38之后设置有抽水泵一39和转子流量计二310。The bottom of the contact oxidation tank 3 is provided with a sludge outlet 37, and the drainage pipe 33 is connected to the membrane reaction zone 4 through the top of the contact oxidation tank 3, wherein the drain pipe 33 is connected to the part above the contact oxidation tank 3. There is a downward water distribution pipe 38, and the water distribution pipe 38 faces the contact oxidation tank 3. After the water distribution pipe 38 on the drain pipe 33, a water pump one 39 and a rotameter two 310 are arranged.
所述排水管33从上方接入膜反应区4,所述膜组件41为双端出水膜组件,即,其集水管411连接有两个出水口412,两个出水口412均与带有抽水泵二43的出水管路42连接。The drainage pipe 33 is connected to the membrane reaction zone 4 from above, and the membrane module 41 is a double-ended water outlet membrane module, that is, its water collecting pipe 411 is connected with two water outlets 412, and the two water outlets 412 are connected with The outlet pipeline 42 of water pump two 43 is connected.
所述两个出水口412均位于膜组件41的顶部。The two water outlets 412 are located at the top of the membrane module 41 .
所述可拆卸式滤芯1与化学沉淀池2集成在一个壳体中,所述接触氧化池3与膜反应区4集成在另一个带有加热装置的壳体中,两个壳体水平设置,共用一个侧壁。The detachable filter element 1 and the chemical precipitation tank 2 are integrated in one housing, the contact oxidation tank 3 and the membrane reaction zone 4 are integrated in another housing with a heating device, and the two housings are arranged horizontally. share a side wall.
与现有技术相比,本实用新型的有益效果是:Compared with the prior art, the beneficial effects of the utility model are:
(1)能大幅度的降低污水中的BOD、COD含量,除去率达90%以上,提高了难降解有机物的降解效率;(1) It can greatly reduce the content of BOD and COD in sewage, with a removal rate of over 90%, improving the degradation efficiency of refractory organic matter;
(2)采用膜分离技术可以对污水中的病毒、细菌有较大的截留作用;(2) The use of membrane separation technology can have a greater interception effect on viruses and bacteria in sewage;
(3)污水中的氮、磷去除效率能达80%以上;(3) The removal efficiency of nitrogen and phosphorus in sewage can reach more than 80%;
(4)该设备可分部进行,经初级部分处理过的污水可直接排放,完全达到国家排放标准,不会造成水污染,而经全套设备处理的污水,可以达到回用的目的。(4) The equipment can be carried out in sections, and the sewage treated by the primary part can be discharged directly, which fully meets the national discharge standards and will not cause water pollution, and the sewage treated by a complete set of equipment can achieve the purpose of reuse.
(5)该设备满足不同家庭对污水处理的要求,如果是对污水处理后能达标排放的要求,可购买设备的初级部分,如果是对处理后的污水起到回用的目的,可购买全套设备;(5) The equipment meets the requirements of different households for sewage treatment. If the sewage treatment can meet the discharge requirements, the primary part of the equipment can be purchased. If the treated sewage is reused, a complete set can be purchased. equipment;
(6)设备占地面积小、运行成本低、操作简单。(6) The equipment occupies a small area, low operating cost and simple operation.
附图说明Description of drawings
图1是本实用新型结构示意图。Fig. 1 is the structural representation of the utility model.
图2是本实用新型可拆卸式的滤芯设计简图。Fig. 2 is a schematic design diagram of the detachable filter element of the present invention.
图3是本实用新型初级净化装置设计简图。Fig. 3 is a schematic diagram of the design of the primary purification device of the present invention.
图4是本实用新型初级净化装置图的俯视图。Fig. 4 is a top view of the primary purification device diagram of the utility model.
图5是本实用新型接触氧化池与膜反应区的设计简图。Fig. 5 is a schematic diagram of the design of the contact oxidation tank and the membrane reaction zone of the present invention.
图6是本实用新型膜反应区膜组件的设计简图。Fig. 6 is a schematic design diagram of the membrane module in the membrane reaction zone of the present invention.
具体实施方式detailed description
下面结合附图和实施例详细说明本实用新型的实施方式。The implementation of the utility model will be described in detail below in conjunction with the accompanying drawings and examples.
如图1所示,本实用新型为一种家用污水处理器,主要包括沿污水行进路线依次设置的可拆卸式滤芯1、化学沉淀池2、接触氧化池3以及膜反应区4,其中,可拆卸式滤芯1与化学沉淀池2集成在一个壳体中,构成初级净化装置。接触氧化池3与膜反应区4集成在另一个带有加热装置的壳体中,两个壳体水平设置,共用一个侧壁。As shown in Figure 1, the utility model is a household sewage processor, which mainly includes a detachable filter element 1, a chemical sedimentation tank 2, a contact oxidation tank 3 and a membrane reaction zone 4 arranged sequentially along the sewage traveling route, wherein, The detachable filter element 1 and the chemical sedimentation tank 2 are integrated in a housing to form a primary purification device. The contact oxidation tank 3 and the membrane reaction zone 4 are integrated in another housing with a heating device. The two housings are arranged horizontally and share a side wall.
如图2、图3和图4所示,可拆卸式滤芯1侧面带有不锈钢外壳,内部自上而下依次为粗滤层11、精滤层12和填料滤层13,粗滤层11由开若干小孔的不锈钢板分层设置而成,层间留有一定的空隙,精滤层12为斜纹滤布,其各项性能居中、抗摩擦力强、过滤速度快,比起其它滤布有更突出的优点。填料滤层13为纤维填料层,其质量轻、强度高、过滤阻力小、滤速快、填料面积小,截污量大,相比于传统的石英砂填料,更能满足家庭用的需求。As shown in Fig. 2, Fig. 3 and Fig. 4, the side of the detachable filter element 1 has a stainless steel shell, and the inside is a coarse filter layer 11, a fine filter layer 12 and a packing filter layer 13 from top to bottom, and the coarse filter layer 11 consists of Stainless steel plates with a number of small holes are arranged in layers, and there are certain gaps between the layers. The fine filter layer 12 is a twill filter cloth, which has moderate performance, strong friction resistance, and fast filtration speed. Compared with other filter cloths There are more prominent advantages. The filler filter layer 13 is a fiber filler layer, which is light in weight, high in strength, small in filtration resistance, fast in filtration speed, small in filler area, and large in interception capacity. Compared with traditional quartz sand fillers, it can better meet the needs of household use.
化学沉淀池2上方设置有开孔顶板14,可拆卸式滤芯1上方有污水储室5,污水储室5的底部为开孔底板15,可拆卸式滤芯1底部设置于开孔顶板14上,顶部通过卡扣16卡在开孔底板15下,化学沉淀池2底部设置有填料层22,填料层22材料选用活性炭和炉渣,具有去除有机物、沉淀污水的作用,而炉渣中含有许多碱性氧化物,经水解后使污水呈碱性,更有利于有机磷的除去。化学沉淀池2的出水口21设置在填料层22处,化学沉淀池2上部设置有吸气口23,吸气口23连接有吸气泵25,保证空间内压力,化学沉淀池2中部设置有溢流槽24,污水经可拆卸式滤芯1后先滴入溢流槽24,再由溢流槽24通过溢流方式进入填料层22。A perforated top plate 14 is arranged above the chemical sedimentation tank 2, and a sewage storage chamber 5 is arranged above the detachable filter element 1. The bottom of the sewage storage chamber 5 is a perforated bottom plate 15, and the bottom of the detachable filter element 1 is arranged on the perforated top plate 14. The top is stuck under the bottom plate 15 through the buckle 16. The bottom of the chemical sedimentation tank 2 is provided with a packing layer 22. The material of the packing layer 22 is activated carbon and slag, which can remove organic matter and precipitate sewage, and the slag contains many alkaline oxides. After hydrolysis, the sewage becomes alkaline, which is more conducive to the removal of organic phosphorus. The water outlet 21 of the chemical sedimentation tank 2 is arranged at the filler layer 22, the upper part of the chemical sedimentation tank 2 is provided with an air suction port 23, and the air suction port 23 is connected with an air suction pump 25 to ensure the pressure in the space, and the middle part of the chemical sedimentation tank 2 is provided with a The overflow tank 24 , the sewage first drips into the overflow tank 24 after passing through the detachable filter element 1 , and then enters the packing layer 22 through the overflow tank 24 by way of overflow.
如图5和图6所示,接触氧化池3中,曝气管34设置在填料下方,不仅供氧充分,而且对生物膜起到搅动作用,能够加速生物膜的更新,提高生物膜活性,将污水中的更多有机物进行氧化分解。曝气管34连接鼓气机35且在连接管路上设置有转子流量计一36,排水管33设置在曝气管34下方。接触氧化池3的底部设置有排泥口37,排水管33从接触氧化池3的上方经过再接至膜反应区4,其中,排水管33在接触氧化池3上方的部分接有向下的分水管38,分水管38朝向接触氧化池3,在排水管33上位于分水管38之后设置有抽水泵一39和转子流量计二310。As shown in Figures 5 and 6, in the contact oxidation tank 3, the aeration pipe 34 is arranged below the filler, which not only supplies sufficient oxygen, but also stirs the biofilm, which can accelerate the renewal of the biofilm and improve the activity of the biofilm. Oxidize and decompose more organic matter in sewage. The aeration pipe 34 is connected to the air blower 35 and a rotameter 1 36 is arranged on the connection pipe, and the drain pipe 33 is arranged below the aeration pipe 34 . The bottom of the contact oxidation tank 3 is provided with a mud outlet 37, and the drainage pipe 33 is connected to the membrane reaction zone 4 through the top of the contact oxidation tank 3, wherein, the part of the drainage pipe 33 above the contact oxidation tank 3 is connected with a The water distribution pipe 38 faces the contact oxidation tank 3 , and the drain pipe 33 is provided with a water pump 1 39 and a rotameter 2 310 after the water distribution pipe 38 .
沉淀池2的出水口21连接接触氧化池3的进水管31一端,进水管31的另一端与接触氧化池3内水平设置的开孔式进水管32连通,接触氧化池3通过底部的排水管33与设置有膜组件41的膜反应区4连通。The water outlet 21 of the sedimentation tank 2 is connected to one end of the water inlet pipe 31 of the contact oxidation tank 3, and the other end of the water inlet pipe 31 communicates with the open-hole water inlet pipe 32 arranged horizontally in the contact oxidation tank 3, and the contact oxidation tank 3 passes through the drain pipe at the bottom 33 communicates with the membrane reaction zone 4 provided with the membrane module 41.
其中,排水管33从上方接入膜反应区4,膜组件41为双端出水膜组件,截留量大,产水快。即,其集水管411连接有两个出水口412,两个出水口412均位于膜组件41的顶部,且两个出水口412均与带有抽水泵二43的出水管路42连接。Among them, the drainage pipe 33 is connected to the membrane reaction zone 4 from above, and the membrane module 41 is a double-ended water outlet membrane module, which has a large retention capacity and fast water production. That is, its water collecting pipe 411 is connected with two water outlets 412, and the two water outlets 412 are located at the top of the membrane module 41, and the two water outlets 412 are connected with the water outlet pipeline 42 with the water pump 2 43.
膜组件41采用聚氯乙烯和聚丙烯合成的中空纤维超滤膜,超滤膜可以有效截留细菌病毒等粒径更小的有机物。用聚偏氟乙烯与聚醚砜虽然有更高的截留性和过滤性,但价格较贵,不易合成,选用聚氯乙烯和聚丙烯的原因是价格便宜,易合成,有较好的性能。The membrane module 41 adopts a hollow fiber ultrafiltration membrane synthesized by polyvinyl chloride and polypropylene, and the ultrafiltration membrane can effectively retain bacteria and viruses and other organic substances with smaller particle sizes. Although polyvinylidene fluoride and polyethersulfone have higher interception and filterability, they are more expensive and difficult to synthesize. The reason for choosing polyvinylidene fluoride and polypropylene is that they are cheap, easy to synthesize, and have good performance.
采用上述结构,其工作过程及原理如下:With the above structure, its working process and principle are as follows:
(1)家庭污水从污水储室5顶部的污水入口6进入污水储室5,在污水储室5短暂储存后进入可拆卸式滤芯1,对污水进行初步过滤。(1) Household sewage enters the sewage storage chamber 5 from the sewage inlet 6 at the top of the sewage storage chamber 5, and enters the detachable filter element 1 after being stored in the sewage storage chamber 5 for a short period of time to perform preliminary filtration of the sewage.
(2)由步骤(1)处理过的污水进入化学沉淀池2,在化学沉淀池2对污水进行沉淀,起到沉淀色素和澄清污水的作用。(2) The sewage treated in step (1) enters the chemical sedimentation tank 2, where the sewage is precipitated to play the role of precipitating pigments and clarifying sewage.
(3)将步骤(2)处理过的污水转入接触氧化池3,在接触氧化池3将污水与空气充分接触,对有机物进行氧化分解。(3) The sewage treated in step (2) is transferred to the contact oxidation tank 3, and the sewage is fully contacted with air in the contact oxidation tank 3 to oxidize and decompose the organic matter.
(4)将步骤(3)处理过的污水转入膜反应区4,采用膜分离技术,对污水中的残余污染物进行有效截留,达到污水回用的目的。(4) The sewage treated in step (3) is transferred to the membrane reaction zone 4, and membrane separation technology is used to effectively intercept the residual pollutants in the sewage to achieve the purpose of sewage reuse.
综上,本实用新型的的初级净化装置可满足污水达标排放的要求,而全套设备能有效除去家庭污水中的COD和有机氮,对污水处理后能达到回用的目的。To sum up, the primary purification device of the utility model can meet the requirements of sewage discharge standards, and the complete set of equipment can effectively remove COD and organic nitrogen in domestic sewage, and can achieve the purpose of recycling sewage after treatment.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720402264.9U CN206767872U (en) | 2017-04-18 | 2017-04-18 | A kind of Domestic sewage treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720402264.9U CN206767872U (en) | 2017-04-18 | 2017-04-18 | A kind of Domestic sewage treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206767872U true CN206767872U (en) | 2017-12-19 |
Family
ID=60630776
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720402264.9U Expired - Fee Related CN206767872U (en) | 2017-04-18 | 2017-04-18 | A kind of Domestic sewage treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206767872U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108328769A (en) * | 2018-02-28 | 2018-07-27 | 佛山市蓝瑞欧特信息服务有限公司 | A kind of energy-saving household apparatus for treating sewage |
| CN116947247A (en) * | 2023-07-27 | 2023-10-27 | 成都飞创科技有限公司 | Household miniature sewage treatment system and sewage treatment using method |
-
2017
- 2017-04-18 CN CN201720402264.9U patent/CN206767872U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108328769A (en) * | 2018-02-28 | 2018-07-27 | 佛山市蓝瑞欧特信息服务有限公司 | A kind of energy-saving household apparatus for treating sewage |
| CN116947247A (en) * | 2023-07-27 | 2023-10-27 | 成都飞创科技有限公司 | Household miniature sewage treatment system and sewage treatment using method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104649519A (en) | Sewage treatment device and method by combining bio-ferric process and anaerobic MBR method | |
| CN202390287U (en) | Internal iron-carbon UASB-SBR (Upflow Anaerobic Sludge Blanket-Sequencing Batch Reactor) coupling system for treatment of printing and dyeing wastewater | |
| CN107285495A (en) | A kind of lithium ion battery production wastewater treatment device | |
| CN206767872U (en) | A kind of Domestic sewage treatment device | |
| CN201056512Y (en) | Film component integrated oxidation ditch | |
| CN109354304A (en) | A method of sewage treatment and energy recovery based on three-stage membrane separation technology | |
| CN208055154U (en) | Sewage purifying and treating device | |
| CN103341285A (en) | Advection sedimentation/immersion type ultrafiltration integrated water treatment device | |
| CN104261603B (en) | The integrated drinking water advanced treatment device of a kind of electric coagulation-electro-flotation/immersion ultrafiltration | |
| CN202482156U (en) | Advanced oxidation and air-flotation treatment combined reverse osmosis concentrated water system | |
| CN205133284U (en) | Industrial wastewater treatment equipment | |
| CN205258241U (en) | Printing and dyeing wastewater treatment system | |
| CN211078799U (en) | Garbage transfer station leachate multistage treatment device | |
| CN210945232U (en) | A new type of rural sewage treatment device | |
| CN104529087B (en) | A kind of sewage recycling, energy are processed into complete equipment and technique | |
| CN204569609U (en) | Industrial sewage pretreatment system | |
| CN202465364U (en) | Compound type biological carbon filtering device | |
| CN207659195U (en) | A kind of environment-protection wastewater processing equipment | |
| CN105776652B (en) | A kind of residual sludge enhanced adsorption-membrane separation water treatment device and method | |
| CN201825825U (en) | Textile sewage treatment system | |
| CN204999776U (en) | Sewage treatment system | |
| CN201512455U (en) | Organic Wastewater Treatment System | |
| CN207294530U (en) | Full-automatic sewage processing unit monitoring system | |
| CN112028400A (en) | A system and method for urban sewage recycling | |
| CN206109038U (en) | Track ditch aeration sedimentation tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20171219 Termination date: 20180418 |