CN207845453U - Microorganism sewage water processing unit - Google Patents
Microorganism sewage water processing unit Download PDFInfo
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- CN207845453U CN207845453U CN201820145908.5U CN201820145908U CN207845453U CN 207845453 U CN207845453 U CN 207845453U CN 201820145908 U CN201820145908 U CN 201820145908U CN 207845453 U CN207845453 U CN 207845453U
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- 239000010865 sewage Substances 0.000 title claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 19
- 244000005700 microbiome Species 0.000 title claims 6
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 54
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 42
- 238000006243 chemical reaction Methods 0.000 claims abstract description 28
- 239000007788 liquid Substances 0.000 claims abstract description 24
- 238000005273 aeration Methods 0.000 claims abstract description 13
- 238000005374 membrane filtration Methods 0.000 claims abstract description 11
- 239000012528 membrane Substances 0.000 claims abstract description 7
- 238000001914 filtration Methods 0.000 claims abstract description 5
- 230000000694 effects Effects 0.000 claims abstract description 3
- 229910052799 carbon Inorganic materials 0.000 claims abstract 4
- 238000007667 floating Methods 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 238000001556 precipitation Methods 0.000 claims description 3
- 241000220317 Rosa Species 0.000 claims 4
- 238000006385 ozonation reaction Methods 0.000 claims 3
- 239000003610 charcoal Substances 0.000 claims 1
- 239000002351 wastewater Substances 0.000 claims 1
- 230000000813 microbial effect Effects 0.000 abstract description 16
- 238000000605 extraction Methods 0.000 abstract description 8
- 238000004062 sedimentation Methods 0.000 description 6
- 239000006228 supernatant Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 238000004891 communication Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
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- Treatment Of Water By Oxidation Or Reduction (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
本实用新型提供一种微生物污水处理装置,它包括通过抽液泵依次相连通的沉淀罐、臭氧处理罐和生物过滤罐;所述沉淀罐内设置有上层液抽取机构;所述臭氧处理罐包括臭氧反应箱、活性炭过滤箱及溢流箱;所述臭氧反应箱的底部还设置有臭氧曝气装置,所述活性炭过滤箱内设置有用于物理过滤的活性炭层;所述生物过滤罐包括生物反应箱和膜过滤箱,所述生物反应箱内设置有多个微生物载体层;所述膜过滤箱内设置有多组过滤管,所述过滤管上覆盖有过滤膜层。该装置结构简单、污水处理效果好。
The utility model provides a microbial sewage treatment device, which comprises a settling tank, an ozone treatment tank and a biological filter tank which are sequentially connected through a liquid pump; the settling tank is provided with an upper liquid extraction mechanism; the ozone treatment tank includes Ozone reaction box, active carbon filter box and overflow box; The bottom of described ozone reaction box is also provided with ozone aeration device, and the activated carbon layer that is used for physical filtration is arranged in described active carbon filter box; Described biological filter tank includes biological reaction A box and a membrane filtration box, the biological reaction box is provided with multiple microbial carrier layers; the membrane filtration box is provided with multiple groups of filter tubes, and the filter tubes are covered with filter membrane layers. The device has simple structure and good sewage treatment effect.
Description
技术领域technical field
本实用新型涉及一种污水处理设备,具体的说,涉及了一种微生物污水处理装置。The utility model relates to a sewage treatment device, in particular to a microbial sewage treatment device.
背景技术Background technique
臭氧具有很强的氧化性,可以氧化多种化合物,而且具有耗量小,反应速度快、不产生污泥等优点,因此被成功地应用于饮用水、工业废水及循环冷却水处理工艺中。尽管臭氧具有极强的氧化性,但也存在一定的局限性。事实上,对于某些有机物,仅仅使用臭氧很难将其完全氧化,此时单独使用臭氧来处理水并不是最佳的方法。另外,现有的生物污水处理设备投资费用过高,从而导致了中国目前的生物污水处理能力尚跟不上用水规模的迅速扩张,配套设施建设严重滞后。Ozone has strong oxidizing properties, can oxidize various compounds, and has the advantages of small consumption, fast reaction speed, and no sludge generation, so it has been successfully used in drinking water, industrial wastewater and circulating cooling water treatment processes. Although ozone is extremely oxidizing, it also has certain limitations. In fact, for some organic substances, it is difficult to completely oxidize them only by using ozone, so using ozone alone to treat water is not the best method at this time. In addition, the investment cost of existing biological sewage treatment equipment is too high, which has led to the fact that China's current biological sewage treatment capacity cannot keep up with the rapid expansion of water consumption, and the construction of supporting facilities is seriously lagging behind.
为了解决以上存在的问题,人们一直在寻求一种理想的技术解决方案。In order to solve the above existing problems, people have been seeking an ideal technical solution.
发明内容Contents of the invention
本实用新型的目的是针对现有技术的不足,从而提供一种微生物污水处理装置。The purpose of the utility model is to provide a microbial sewage treatment device aiming at the deficiencies of the prior art.
为了实现上述目的,本实用新型所采用的技术方案是:一种微生物污水处理装置,它包括通过多个抽液泵依次相连通的沉淀罐、臭氧处理罐和生物过滤罐;In order to achieve the above object, the technical solution adopted by the utility model is: a microbial sewage treatment device, which includes a settling tank, an ozone treatment tank and a biological filter tank connected in sequence through a plurality of pumping pumps;
所述沉淀罐内设置有上层液抽取机构,所述上层液抽取机构包括软管和设置在所述沉淀罐的内侧壁的导向槽;所述软管底部伸出所述沉淀罐设置并通过第一抽液泵与所述臭氧处理罐相连通,所述软管顶部固定连接有浮球,所述浮球下部开设有抽液孔,所述浮球上部通过一软质连接线连接有定位球,所述定位球活动设置在所述导向槽内;The settling tank is provided with an upper layer liquid extraction mechanism, the upper layer liquid extraction mechanism includes a hose and a guide groove arranged on the inner side wall of the settling tank; the bottom of the hose protrudes from the settling tank and passes through the first A liquid suction pump is connected with the ozone treatment tank, the top of the hose is fixedly connected with a floating ball, the lower part of the floating ball is provided with a liquid suction hole, and the upper part of the floating ball is connected with a positioning ball through a soft connecting line , the positioning ball is movably arranged in the guide groove;
所述臭氧处理罐包括臭氧反应箱、活性炭过滤箱及溢流箱;所述臭氧反应箱的侧壁设置有第一溢流槽,所述臭氧反应箱通过所述第一溢流槽连通所述活性炭过滤箱;所述活性炭过滤箱的底部与所述溢流箱的底部相连通;所述臭氧反应箱的底部开设有臭氧反应箱入水口,所述溢流箱顶部开设有溢流箱出水口;所述第一抽液泵的一端连接在所述臭氧反应箱入水口上,所述臭氧反应箱的底部还设置有臭氧曝气装置,所述臭氧曝气装置连接有臭氧瓶,所述活性炭过滤箱内设置有用于物理过滤的活性炭层,所述活性炭层位于所述第一溢流槽的下方;The ozone treatment tank includes an ozone reaction box, an activated carbon filter box and an overflow box; the side wall of the ozone reaction box is provided with a first overflow tank, and the ozone reaction box communicates with the Activated carbon filter box; the bottom of the activated carbon filter box is connected with the bottom of the overflow box; the bottom of the ozone reaction box is provided with an ozone reaction box water inlet, and the top of the overflow box is provided with an overflow box water outlet One end of the first liquid suction pump is connected to the water inlet of the ozone reaction box, and the bottom of the ozone reaction box is also provided with an ozone aeration device, and the ozone aeration device is connected with an ozone bottle, and the activated carbon An activated carbon layer for physical filtration is arranged in the filter box, and the activated carbon layer is located below the first overflow tank;
所述生物过滤罐包括生物反应箱和膜过滤箱,所述生物反应箱内设置有多层微生物载体层;所述生物反应箱的侧壁设置有第二溢流槽,且所述第二溢流槽位于最顶层所述微生物载体层的上方,所述生物反应箱通过所述第二溢流槽连通所述膜过滤箱;所述生物反应箱设置有生物反应箱入口,所述生物反应箱入口通过第二抽液泵连通所述溢流箱出水口;所述膜过滤箱内设置有多组过滤管,所述过滤管上覆盖有过滤膜层,多组所述过滤管通过汇流管连通有第三抽液泵。The biofiltration tank includes a bioreactor box and a membrane filtration box, the bioreactor box is provided with a multi-layer microbial carrier layer; the side wall of the bioreactor box is provided with a second overflow tank, and the second overflow tank The launder is located above the microbial carrier layer on the top floor, and the bioreactor is connected to the membrane filtration box through the second overflow tank; the bioreactor is provided with a bioreactor inlet, and the bioreactor The inlet is connected to the outlet of the overflow box through the second pump; the membrane filter box is provided with multiple sets of filter tubes, the filter tubes are covered with a filter film layer, and the multiple sets of filter tubes are connected through a confluence pipe There is a third suction pump.
基于上述,所述臭氧曝气装置为曝气头、溶气泵、水射器、管道混合器、穿孔管或滤头。Based on the above, the ozone aeration device is an aeration head, a dissolved air pump, a water ejector, a pipeline mixer, a perforated pipe or a filter head.
基于上述,所述沉淀罐底部开设有排污阀。Based on the above, a drain valve is provided at the bottom of the sedimentation tank.
基于上述,所述沉淀罐顶部开设有污水进口,所述污水进口上连通有污水泵。Based on the above, a sewage inlet is opened on the top of the sedimentation tank, and a sewage pump is connected to the sewage inlet.
本实用新型相对现有技术具有实质性特点和进步,具体的说,本实用新型所提供的微生物污水处理装置,首先将污水抽至沉淀罐进行沉淀,并通过上层液抽取机构将沉淀了污泥和大颗粒的污水上层液抽至臭氧曝气装置中,随后采用臭氧曝气装置氧化部分有机物,提高有机污染物的可生化性,最后与生物过滤罐联合进行处理,充分利用臭氧分解产生的氧气,提高了附着在过滤膜层上的各种优势细菌所获得的氧气量,可大幅度提高膜过滤箱内细菌的工作活力,增强对污水的有效处理。该装置结构简单、污水处理效果好。Compared with the prior art, the utility model has substantive characteristics and progress. Specifically, the microbial sewage treatment device provided by the utility model firstly pumps the sewage into the sedimentation tank for precipitation, and then through the supernatant liquid extraction mechanism, the precipitated sludge The supernatant of sewage and large particles is pumped into the ozone aeration device, and then the ozone aeration device is used to oxidize part of the organic matter to improve the biodegradability of the organic pollutants, and finally it is combined with the biological filter tank to make full use of the oxygen generated by the decomposition of the ozone , It increases the amount of oxygen obtained by various dominant bacteria attached to the filter membrane layer, which can greatly improve the working activity of bacteria in the membrane filter box and enhance the effective treatment of sewage. The device has simple structure and good sewage treatment effect.
附图说明Description of drawings
图1是本实用新型提供的微生物污水处理装置整体结构示意图。Fig. 1 is a schematic diagram of the overall structure of the microbial sewage treatment device provided by the utility model.
图2是本实用新型提供的微生物污水处理装置中的上层液抽取机构结构示意图。Fig. 2 is a schematic structural diagram of the supernatant liquid extraction mechanism in the microbial sewage treatment device provided by the present invention.
图3是本实用新型提供的微生物污水处理装置中的导向槽结构示意图。Fig. 3 is a structural schematic diagram of the guide groove in the microbial sewage treatment device provided by the utility model.
图4是本实用新型提供的微生物污水处理装置中的过滤管结构示意图。Fig. 4 is a structural schematic diagram of the filter tube in the microbial sewage treatment device provided by the utility model.
图中:1、污水泵;2、沉淀罐;3、上层液抽取机构;31、软质连接线;32、定位球;33、抽液孔;34、浮球;35、软管;36、导向槽;4、第一抽液泵;5、臭氧处理罐;6、臭氧曝气装置;7、臭氧供气管;8、活性炭层;9、隔离板;10、溢流箱;11、第二抽液泵;12、生物反应箱;13、微生物载体层;14、第二溢流槽;15、过滤管;16、第三抽液泵;17、过滤膜层;18、第一溢流槽;19、排污阀。In the figure: 1. Sewage pump; 2. Sedimentation tank; 3. Supernatant liquid extraction mechanism; 31. Soft connection line; 32. Positioning ball; 33. Liquid pumping hole; 34. Floating ball; 35. Flexible hose; Guide groove; 4. The first suction pump; 5. Ozone treatment tank; 6. Ozone aeration device; 7. Ozone gas supply pipe; 8. Activated carbon layer; 9. Isolation plate; 10. Overflow box; 11. The second Liquid suction pump; 12. Biological reaction tank; 13. Microbial carrier layer; 14. Second overflow tank; 15. Filter tube; 16. Third liquid suction pump; 17. Filtration membrane layer; 18. First overflow tank ; 19, blowdown valve.
具体实施方式Detailed ways
下面通过具体实施方式,对本实用新型的技术方案做进一步的详细描述。The technical solutions of the present invention will be further described in detail through specific implementation methods below.
实施例1Example 1
如图1、图2、图3和图4所示,本实施例提供了一种微生物污水处理装置,它包括通过多个抽液泵依次相连通的沉淀罐2、臭氧处理罐5和生物过滤罐。As shown in Fig. 1, Fig. 2, Fig. 3 and Fig. 4, the present embodiment provides a microbial sewage treatment device, which includes a settling tank 2, an ozone treatment tank 5, and a biological filter that are sequentially connected through a plurality of pumps. Can.
所述沉淀罐2内设置有上层液抽取机构3。具体地,如图2和图3所示,所述上层液抽取机构3包括软管35和设置在所述沉淀罐2的内侧壁的导向槽36;所述软管35底部伸出所述沉淀罐2设置并通过第一抽液泵4与所述臭氧处理罐5相连通。所述软管35顶部固定连接有浮球34,所述浮球34下部开设有抽液孔33,所述浮球34上部通过一软质连接线31连接有定位球32。所述定位球32活动设置在所述导向槽36内。The sedimentation tank 2 is provided with a supernatant liquid extraction mechanism 3 . Specifically, as shown in Fig. 2 and Fig. 3, the upper layer liquid extraction mechanism 3 includes a hose 35 and a guide groove 36 arranged on the inner side wall of the sedimentation tank 2; the bottom of the hose 35 extends out of the sediment The tank 2 is set and communicated with the ozone treatment tank 5 through the first liquid suction pump 4 . The top of the hose 35 is fixedly connected with a floating ball 34 , the lower part of the floating ball 34 is provided with a suction hole 33 , and the upper part of the floating ball 34 is connected with a positioning ball 32 through a soft connecting wire 31 . The positioning ball 32 is movably disposed in the guide groove 36 .
所述臭氧处理罐5包括臭氧反应箱、活性炭过滤箱及溢流箱10。所述臭氧反应箱朝向于所述活性炭过滤箱的侧壁设置有第一溢流槽18,且所述第一溢流槽18位于所述活性炭过滤箱的上方,所述臭氧反应箱通过所述第一溢流槽18连通所述活性炭过滤箱。所述活性炭过滤箱和所述溢流箱10之间通过隔离板9相隔离,且所述隔离板9的底部开设有连通孔使得所述活性炭过滤箱的底部和所述溢流箱10底部相连通。所述臭氧反应箱底部开设有臭氧反应箱入水口,所述溢流箱顶部开设有溢流箱出水口;所述第一抽液泵4连通所述臭氧反应箱入水口。所述臭氧反应箱的底部还设置有臭氧曝气装置6,所述臭氧曝气装置6通过臭氧供气管7连接有臭氧瓶。所述活性炭过滤箱内设置有用于物理过滤的活性炭层8。The ozone treatment tank 5 includes an ozone reaction box, an activated carbon filter box and an overflow box 10 . The ozone reaction box is provided with a first overflow tank 18 towards the side wall of the activated carbon filter box, and the first overflow tank 18 is located above the activated carbon filter box, and the ozone reaction box passes through the The first overflow tank 18 communicates with the activated carbon filter box. The activated carbon filter box and the overflow box 10 are isolated by a separation plate 9, and the bottom of the separation plate 9 is provided with a communication hole so that the bottom of the activated carbon filter box is connected to the bottom of the overflow box 10 Pass. The bottom of the ozone reaction box is provided with a water inlet of the ozone reaction box, and the top of the overflow box is provided with an outlet of the overflow box; the first pump 4 is connected to the water inlet of the ozone reaction box. The bottom of the ozone reaction box is also provided with an ozone aeration device 6, and the ozone aeration device 6 is connected with an ozone bottle through an ozone supply pipe 7. The activated carbon filter box is provided with an activated carbon layer 8 for physical filtration.
所述生物过滤罐包括生物反应箱12和膜过滤箱,所述生物反应箱12内设置有多层微生物载体层13。所述生物反应箱12朝向于所述膜过滤箱的侧壁设置有第二溢流槽14,且所述第二溢流槽14位于最顶层所述微生物载体层13的上方,所述生物反应箱12通过所述第二溢流槽14连通所述膜过滤箱。所述生物反应箱12设置有生物反应箱入口,所述生物反应箱入口通过第二抽液泵11连通所述溢流箱出水口。所述膜过滤箱内设置有多组过滤管15,所述过滤管上15覆盖有过滤膜层17,多组所述过滤管15通过汇流管连通有第三抽液泵16。The biofiltration tank includes a bioreactor box 12 and a membrane filtration box, and the bioreactor box 12 is provided with multiple microbial carrier layers 13 . The biological reaction box 12 is provided with a second overflow tank 14 towards the side wall of the membrane filtration box, and the second overflow tank 14 is located above the top microbial carrier layer 13, the biological reaction The tank 12 communicates with the membrane filtration tank through the second overflow tank 14 . The bioreactor 12 is provided with an inlet of the bioreactor, and the inlet of the bioreactor is connected to the water outlet of the overflow tank through the second pump 11 . Multiple sets of filter tubes 15 are arranged in the membrane filtration box, and the filter tubes 15 are covered with a filter membrane layer 17, and the multiple sets of filter tubes 15 are connected to a third pump 16 through a confluence tube.
本实施例中,所述臭氧曝气装置6为曝气头。所述沉淀罐2底部开设有排污阀19。所述沉淀罐2顶部开设有污水进口,所述污水进口上连通有污水泵1。In this embodiment, the ozone aeration device 6 is an aeration head. A drain valve 19 is provided at the bottom of the settling tank 2 . A sewage inlet is provided on the top of the settling tank 2, and a sewage pump 1 is connected to the sewage inlet.
最后应当说明的是:以上实施例仅用以说明本实用新型的技术方案而非对其限制;尽管参照较佳实施例对本实用新型进行了详细的说明,所属领域的普通技术人员应当理解:依然可以对本实用新型的具体实施方式进行修改或者对部分技术特征进行等同替换;而不脱离本实用新型技术方案的精神,其均应涵盖在本实用新型请求保护的技术方案范围当中。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present utility model and not limit it; although the utility model has been described in detail with reference to the preferred embodiment, those of ordinary skill in the art should understand that: still The specific implementation of the utility model can be modified or some technical features can be equivalently replaced; without departing from the spirit of the technical solution of the utility model, all of them should be included in the scope of the technical solution claimed by the utility model.
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Cited By (2)
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CN110526552A (en) * | 2019-08-30 | 2019-12-03 | 广东沪利环境科技发展有限公司 | A kind of sludge treating system |
CN112624437A (en) * | 2021-01-18 | 2021-04-09 | 江苏工程职业技术学院 | Municipal pipe network sewage recycling system |
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CN110526552A (en) * | 2019-08-30 | 2019-12-03 | 广东沪利环境科技发展有限公司 | A kind of sludge treating system |
CN112624437A (en) * | 2021-01-18 | 2021-04-09 | 江苏工程职业技术学院 | Municipal pipe network sewage recycling system |
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