CN202297244U - Sewage treatment system with combination of biochemical flocculation and aerated biofilter - Google Patents
Sewage treatment system with combination of biochemical flocculation and aerated biofilter Download PDFInfo
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- 238000005189 flocculation Methods 0.000 title claims abstract description 45
- 230000016615 flocculation Effects 0.000 title claims abstract description 45
- 239000010865 sewage Substances 0.000 title claims abstract description 45
- 238000005273 aeration Methods 0.000 claims abstract description 103
- 239000010802 sludge Substances 0.000 claims abstract description 81
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 238000006243 chemical reaction Methods 0.000 claims abstract description 29
- 238000004062 sedimentation Methods 0.000 claims abstract description 27
- 230000004913 activation Effects 0.000 claims abstract description 21
- 239000000701 coagulant Substances 0.000 claims abstract description 9
- 239000000126 substance Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 238000011001 backwashing Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 244000005700 microbiome Species 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000013043 chemical agent Substances 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Activated Sludge Processes (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
生物化学絮凝与曝气生物滤池组合污水处理系统,它涉及一种污水处理系统。本实用新型为了解决现有污水深度处理系统存在高负荷所带来的运行费用增加和管理不便的问题。加药管的两端分别与污水进水管和混凝剂罐连通,生物化学絮凝反应池与沉淀池通过流经管连通,第一曝气头设置在生物化学絮凝反应池内,第一曝气管的两端分别与第一曝气头和第一曝气泵连通;第一污泥回流管两端分别与污泥流出管和污泥活化池连通,第二曝气头设置在污泥活化池内,第二曝气管两端分别与第二曝气头和第二曝气泵连通,污泥活化池与生物化学絮凝反应池通过第二污泥回流管连通,沉淀池与曝气生物滤池通过第一出水管连通。本实用新型用于生活污水处理中。
The utility model relates to a combined sewage treatment system of biochemical flocculation and biological aeration filter, which relates to a sewage treatment system. The utility model aims to solve the problems of increased operation cost and inconvenient management caused by the high load of the existing advanced sewage treatment system. The two ends of the dosing pipe are respectively connected with the sewage inlet pipe and the coagulant tank. The biochemical flocculation reaction tank and the sedimentation tank are connected through the flow-through pipe. The first aeration head is set in the biochemical flocculation reaction tank. The first aeration pipe The two ends are respectively connected with the first aeration head and the first aeration pump; the two ends of the first sludge return pipe are respectively connected with the sludge outflow pipe and the sludge activation tank, and the second aeration head is set in the sludge activation tank. The two ends of the second aeration pipe are respectively connected with the second aeration head and the second aeration pump, the sludge activation tank is connected with the biochemical flocculation reaction tank through the second sludge return pipe, and the sedimentation tank is connected with the biological aerated filter through the second sludge return pipe. The first water outlet pipe is connected. The utility model is used in domestic sewage treatment.
Description
技术领域 technical field
本实用新型涉及一种污水处理系统,具体涉及一种生物化学絮凝与曝气生物滤池组合污水处理系统,属于水处理技术领域。The utility model relates to a sewage treatment system, in particular to a combined sewage treatment system of biochemical flocculation and aerated biological filter, which belongs to the technical field of water treatment.
背景技术 Background technique
随着工业化的发展和人民物质生活水平的提高,大量工业废水和生活污水等的排入对给水水源造成了不同程度的污染。微量有机物和有毒有害物质的存在,加剧了水质的恶化,污染的程度日趋严重。With the development of industrialization and the improvement of people's material living standards, the discharge of a large amount of industrial wastewater and domestic sewage has caused varying degrees of pollution to water sources. The existence of trace organic matter and toxic and harmful substances has exacerbated the deterioration of water quality, and the degree of pollution has become increasingly serious.
曝气生物滤池(BAF)工艺是20世纪80年代末欧美发展起来的一种新型的生物处理工艺,世界上首座曝气生物滤池于1981在法国投产,90年代初国外BAF(曝气生物滤池)工艺已经基本成熟,尤其在欧美和日本得到广泛的推广。该工艺具有去除SS(浮游物质量)、COD(化学需氧量)、BOD(生物化学的酸素要求量)、硝化、脱氮、除磷、去除AOX(有害物质)的作用,其特点是集生物氧化和截留悬浮固体于一体,节省了后续二沉池,其容积负荷大、水力负荷大,水力停留时间短,所需基建投资少,出水水质好,运行能耗低,运行费用省。BAF主要缺点为对进水SS要求较高,为使之在较短的水力停留时间内处理较高的有机负荷并具有截留SS功能,BAF填料粒径一般都比较小。进水SS过高,会使滤池在短时间内达到设计的水头损失而发生堵塞,导致频繁反冲洗而会增加运行费用和带来管理的不便。综上,现有的污水深度处理系统存在高负荷所带来的运行费用增加和管理不便的问题。The biological aerated filter (BAF) process is a new type of biological treatment process developed in Europe and the United States in the late 1980s. The world's first biological aerated filter was put into operation in France in 1981. In the early 1990s, BAF (aerated biological filter) technology has been basically mature, especially in Europe, America and Japan have been widely promoted. This process has the functions of removing SS (substance mass), COD (chemical oxygen demand), BOD (biochemical acid requirement), nitrification, nitrogen removal, phosphorus removal, and AOX (harmful substance) removal. Its characteristics are integrated Bio-oxidation and interception of suspended solids are integrated, saving the subsequent secondary settling tank, which has large volume load, large hydraulic load, short hydraulic retention time, less infrastructure investment, good effluent quality, low energy consumption and low operating costs. The main disadvantage of BAF is that it has higher requirements for SS in the influent. In order to make it handle higher organic loads in a shorter hydraulic retention time and have the function of intercepting SS, the particle size of BAF fillers is generally relatively small. If the water SS is too high, the filter will reach the designed head loss in a short period of time and blockage will occur, resulting in frequent backwashing, which will increase operating costs and bring inconvenience to management. To sum up, the existing advanced sewage treatment system has the problems of increased operating costs and inconvenient management due to high load.
实用新型内容 Utility model content
本实用新型的目的是为了解决现有污水深度处理系统存在高负荷所带来的运行费用增加和管理不便的问题,进而提供一种生物化学絮凝与曝气生物滤池组合污水处理系统。The purpose of the utility model is to solve the problems of increased operating costs and inconvenient management caused by the high load of the existing sewage advanced treatment system, and further provide a combined sewage treatment system of biochemical flocculation and biological aerated filter.
本实用新型的技术方案是:生物化学絮凝与曝气生物滤池组合污水处理系统包括污水进水管、第一曝气泵、第一曝气管、加药管、加药泵、混凝剂罐、第一曝气头、生物化学絮凝反应池、流经管、沉淀池、第一出水管和污泥流出管;所述生物化学絮凝与曝气生物滤池组合污水处理系统还包括第一污泥回流管、第一污泥回流泵、第二曝气泵、第二曝气管、第二曝气头、污泥活化池、第二污泥回流泵、第二污泥回流管、曝气生物滤池、反冲洗进水管、第二出水管、反冲洗泵、第三出水管、反冲洗进气管、第三曝气泵、第三曝气管、第三曝气头和第四曝气头;污水进水管与生物化学絮凝反应池连通,加药管的一端与污水进水管连通,加药管的另一端与混凝剂罐连通,加药管上安装有加药泵,流经管的一端与生物化学絮凝反应池连通,流经管的另一端安装在沉淀池中部外壁上,且流经管与沉淀池连通,污泥流出管的一端安装在沉淀池的底端面上,且污泥流出管与沉淀池连通,所述第一曝气头设置在生物化学絮凝反应池内,第一曝气管的一端穿入生物化学絮凝反应池与第一曝气头连通,第一曝气管的另一端连接有第一曝气泵;第一污泥回流管的一端与污泥流出管连通,第一污泥回流管的另一端与污泥活化池连通,第一污泥回流泵安装在第一污泥回流管上,第二曝气头设置在污泥活化池内,第二曝气管的一端穿入污泥活化池与第二曝气头连通,第二曝气管的另一端连接有第二曝气泵,污泥活化池与生物化学絮凝反应池之间通过第二污泥回流管连通,第二污泥回流管上安装有第二污泥回流泵,第一出水管的一端安装在沉淀池的上部外壁上,且第一出水管与沉淀池连通,第一出水管的另一端安装在曝气生物滤池的下部外壁上,且第一出水管与曝气生物滤池连通,第三出水管安装在曝气生物滤池的下部外壁上,且第三出水管与曝气生物滤池连通,第二出水管安装在曝气生物滤池的上部外壁上,且第三出水管与曝气生物滤池连通,反冲洗进水管一端与第二出水管连通,反冲洗进水管的另一端与曝气生物滤池的上部连通,反冲洗泵安装在反冲洗进水管上,第三曝气头和第四曝气头由上至下设置在曝气生物滤池内,第三曝气泵置于曝气生物滤池的外部,第三曝气泵通过第三曝气管与第三曝气头连通,第三曝气泵通过反冲洗进气管与第四曝气头连通。The technical scheme of the utility model is: the combined sewage treatment system of biochemical flocculation and biological aerated filter includes a sewage inlet pipe, a first aeration pump, a first aeration pipe, a dosing pipe, a dosing pump, and a coagulant tank , the first aeration head, biochemical flocculation reaction tank, flow-through pipe, sedimentation tank, first outlet pipe and sludge outflow pipe; the combined sewage treatment system of biochemical flocculation and biological aerated filter also includes the first sludge Return pipe, first sludge return pump, second aeration pump, second aeration pipe, second aeration head, sludge activation tank, second sludge return pump, second sludge return pipe, aerated organisms Filter tank, backwash water inlet pipe, second water outlet pipe, backwash pump, third water outlet pipe, backwash inlet pipe, third aeration pump, third aeration pipe, third aeration head and fourth aeration head The sewage inlet pipe is connected with the biochemical flocculation reaction tank, one end of the dosing pipe is connected with the sewage water inlet pipe, the other end of the dosing pipe is connected with the coagulant tank, and the dosing pump is installed on the dosing pipe, and flows through one end of the pipe It is connected with the biochemical flocculation reaction tank, the other end of the flow-through pipe is installed on the outer wall of the middle part of the sedimentation tank, and the flow-through pipe is connected with the sedimentation tank, and one end of the sludge outflow pipe is installed on the bottom end surface of the sedimentation tank, and the sludge outflow pipe is connected with the sedimentation tank The sedimentation tank is connected, the first aeration head is set in the biochemical flocculation reaction tank, one end of the first aeration pipe penetrates into the biochemical flocculation reaction tank and communicates with the first aeration head, and the other end of the first aeration pipe is connected to There is a first aeration pump; one end of the first sludge return pipe is connected to the sludge outflow pipe, the other end of the first sludge return pipe is connected to the sludge activation tank, and the first sludge return pump is installed on the first sludge On the return pipe, the second aeration head is set in the sludge activation tank, one end of the second aeration tube penetrates into the sludge activation tank and communicates with the second aeration head, and the other end of the second aeration tube is connected to the second aeration tank. The air pump, the sludge activation tank and the biochemical flocculation reaction tank are connected through the second sludge return pipe, the second sludge return pipe is installed with the second sludge return pump, and one end of the first outlet pipe is installed in the sedimentation tank. On the outer wall of the upper part, and the first water outlet pipe is connected with the sedimentation tank, the other end of the first water outlet pipe is installed on the lower outer wall of the biological aerated filter, and the first water outlet pipe is connected with the biological aerated filter tank, and the third water outlet pipe Installed on the lower outer wall of the biological aerated filter, and the third outlet pipe communicates with the biological aerated filter, the second outlet pipe is installed on the upper outer wall of the biological aerated filter, and the third outlet pipe communicates with the biological aerated filter The filter tank is connected, one end of the backwashing water inlet pipe is connected with the second water outlet pipe, the other end of the backwashing water inlet pipe is connected with the upper part of the biological aerated filter, the backwashing pump is installed on the backwashing water inlet pipe, the third aeration head and The fourth aeration head is installed in the biological aeration filter from top to bottom, the third aeration pump is placed outside the biological aeration filter, and the third aeration pump passes through the third aeration pipe and the third aeration head The third aeration pump communicates with the fourth aeration head through the backwash intake pipe.
本实用新型与现有技术相比具有以下效果:1、本实用新型的生物化学絮凝与曝气生物滤池组合污水处理系统对生物化学絮凝反应池进行曝气,发挥活化污泥的微生物活性,同时与化学药剂协同作用吸附部分降解污水中溶解性物质和微细不可沉悬的固体,提升了污水处理效果。2、生物化学絮凝反应池进行的强化反应时间短,大幅度提高了生活污水的处理能力。3、污水在生物化学絮凝反应池中停留时间较短,在沉淀池中的污泥微生物不能够充分进行代谢,增设一个污泥活化池,通过曝气对污泥活化池中的污泥进行活化,进一步恢复了污泥中微生物的活性,再将活化后活性增强的污泥回流至生物化学絮凝反应池中。4、本实用新型对污水处理分为两个阶段:生物化学絮凝强化阶段和曝气生物滤池深度处理阶段,通过强化处理减轻了曝气生物滤池处理污水的负荷,使出水达标或回用。本实用新型的生物化学絮凝与曝气生物滤池组合污水处理系统基建投资和运行费用较低,易于管理,无须复杂的操作系统,且不受气候条件的限制,适应水量和水质的波动,实现了生活污水中有机污染物的有效去除。Compared with the prior art, the utility model has the following effects: 1. The biochemical flocculation and aerated biological filter combined sewage treatment system of the utility model aerates the biochemical flocculation reaction pool to exert the microbial activity of the activated sludge, At the same time, it cooperates with chemical agents to adsorb and partially degrade the dissolved substances and fine unsuspendable solids in sewage, which improves the sewage treatment effect. 2. The enhanced reaction time of the biochemical flocculation reaction tank is short, which greatly improves the treatment capacity of domestic sewage. 3. The residence time of sewage in the biochemical flocculation reaction tank is short, and the sludge microorganisms in the sedimentation tank cannot fully metabolize. A sludge activation tank is added to activate the sludge in the sludge activation tank through aeration , to further restore the activity of microorganisms in the sludge, and then return the activated sludge with enhanced activity to the biochemical flocculation reaction tank. 4. The utility model divides sewage treatment into two stages: biochemical flocculation intensification stage and biological aerated filter advanced treatment stage. Through enhanced treatment, the load of sewage treatment in biological aerated filter is reduced, so that the effluent can reach the standard or be reused . The biochemical flocculation and biological aerated filter combined sewage treatment system of the utility model has low infrastructure investment and operating costs, is easy to manage, does not require a complicated operating system, and is not limited by climatic conditions, adapts to fluctuations in water volume and water quality, and realizes Effective removal of organic pollutants in domestic sewage.
附图说明 Description of drawings
图1是本实用新型的生物化学絮凝与曝气生物滤池组合污水处理系统的整体结构示意图(图中箭头表示介质走向)。Fig. 1 is a schematic diagram of the overall structure of the biochemical flocculation and biological aerated filter combined sewage treatment system of the present invention (the arrow in the figure indicates the direction of the medium).
具体实施方式 Detailed ways
具体实施方式一:结合图1说明本实施方式,本实施方式的生物化学絮凝与曝气生物滤池组合污水处理系统包括污水进水管1、第一曝气泵3、第一曝气管4、加药管8、加药泵9、混凝剂罐10、第一曝气头12、生物化学絮凝反应池13、流经管14、沉淀池15、第一出水管16和污泥流出管17;所述生物化学絮凝与曝气生物滤池组合污水处理系统还包括第一污泥回流管18、第一污泥回流泵19、第二曝气泵21、第二曝气管22、第二曝气头6、污泥活化池23、第二污泥回流泵24、第二污泥回流管25、曝气生物滤池2、反冲洗进水管26、第二出水管27、反冲洗泵28、第三出水管29、反冲洗进气管30、第三曝气泵31、第三曝气管32、第三曝气头33和第四曝气头34;污水进水管1与生物化学絮凝反应池13连通,加药管8的一端与污水进水管1连通,加药管8的另一端与混凝剂罐10连通,加药管8上安装有加药泵9,流经管14的一端与生物化学絮凝反应池13连通,流经管14的另一端安装在沉淀池15中部外壁上,且流经管14与沉淀池15连通,污泥流出管17的一端安装在沉淀池15的底端面上,且污泥流出管17与沉淀池15连通,所述第一曝气头12设置在生物化学絮凝反应池13内,第一曝气管4的一端穿入生物化学絮凝反应池13与第一曝气头12连通,第一曝气管4的另一端连接有第一曝气泵3;第一污泥回流管18的一端与污泥流出管17连通,第一污泥回流管18的另一端与污泥活化池23连通,第一污泥回流泵19安装在第一污泥回流管18上,第二曝气头6设置在污泥活化池23内,第二曝气管22的一端穿入污泥活化池23与第二曝气头6连通,第二曝气管22的另一端连接有第二曝气泵21,污泥活化池23与生物化学絮凝反应池13之间通过第二污泥回流管25连通,第二污泥回流管25上安装有第二污泥回流泵24,第一出水管16的一端安装在沉淀池15的上部外壁上,且第一出水管16与沉淀池15连通,第一出水管16的另一端安装在曝气生物滤池2的下部外壁上,且第一出水管16与曝气生物滤池2连通,第三出水管29安装在曝气生物滤池2的下部外壁上,且第三出水管29与曝气生物滤池2连通,第二出水管27安装在曝气生物滤池2的上部外壁上,且第三出水管29与曝气生物滤池2连通,反冲洗进水管26一端与第二出水管27连通,反冲洗进水管26的另一端与曝气生物滤池2的上部连通,反冲洗泵28安装在反冲洗进水管26上,第三曝气头33和第四曝气头34由上至下设置在曝气生物滤池2内,第三曝气泵31置于曝气生物滤池2的外部,第三曝气泵31通过第三曝气管30与第三曝气头33连通,第三曝气泵31通过反冲洗进气管30与第四曝气头34连通。Specific Embodiment 1: This embodiment is described in conjunction with FIG. 1. The biochemical flocculation and biological aerated filter combined sewage treatment system of this embodiment includes a sewage inlet pipe 1, a first aeration pump 3, a first aeration pipe 4, Dosing pipe 8,
具体实施方式二:结合图1说明本实施方式,本实施方式的生物化学絮凝与曝气生物滤池组合污水处理系统还包括第一流量计5和第二流量计20,所述第一流量计5安装在第一曝气管4上,第二流量计20安装在第二曝气管22上。如此设置,便于控制曝气量。其它组成和连接关系与具体实施方式一相同。Specific embodiment two: this embodiment is described in conjunction with Fig. 1, the biochemical flocculation and biological aerated filter combined sewage treatment system of this embodiment also includes a
工作过程:结合图1说明本实用新型的工作过程,生活污水通过污水进水管1流入生物化学絮凝反应池13,同时混凝剂罐10内的絮凝剂与混凝剂通过加药管8投加进入生物化学絮凝反应池13内,进行曝气,化学药剂与具有活性的污泥协同作用进行短期强化反应,反应后的污水进入沉淀池15泥水分离。将沉淀池15中的未能充分代谢的污泥微生物通过第一污泥回流管18注入污泥活化池23内,进行曝气,恢复污泥中微生物的活性后,将污泥再次注入生物化学絮凝反应池13内,降低了污泥产量和化学药剂的消耗。经过沉淀后的水由第一出水管16进入曝气生物滤池2内进行深处里,通过强化处理和深处里两个阶段,使污水达到排放标准或回用。Working process: The working process of the utility model is illustrated in conjunction with Fig. 1. The domestic sewage flows into the biochemical
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| CN105948251A (en) * | 2016-06-24 | 2016-09-21 | 中国科学院生态环境研究中心 | Multistage A/O (anoxic/oxic) biomembrane-sludge activation coupled denitrification and dephosphorization device and application thereof |
| CN118239579A (en) * | 2024-03-01 | 2024-06-25 | 华中农业大学 | A biogas slurry treatment system using activated sludge to prepare high-efficiency bioflocculant coupled with aerated biological filter technology |
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Cited By (2)
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| CN105948251A (en) * | 2016-06-24 | 2016-09-21 | 中国科学院生态环境研究中心 | Multistage A/O (anoxic/oxic) biomembrane-sludge activation coupled denitrification and dephosphorization device and application thereof |
| CN118239579A (en) * | 2024-03-01 | 2024-06-25 | 华中农业大学 | A biogas slurry treatment system using activated sludge to prepare high-efficiency bioflocculant coupled with aerated biological filter technology |
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