CN201501817U - Small car wash car wash wastewater treatment equipment - Google Patents
Small car wash car wash wastewater treatment equipment Download PDFInfo
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- CN201501817U CN201501817U CN2009201766703U CN200920176670U CN201501817U CN 201501817 U CN201501817 U CN 201501817U CN 2009201766703 U CN2009201766703 U CN 2009201766703U CN 200920176670 U CN200920176670 U CN 200920176670U CN 201501817 U CN201501817 U CN 201501817U
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- 238000004065 wastewater treatment Methods 0.000 title abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 64
- 238000005273 aeration Methods 0.000 claims abstract description 58
- 238000004140 cleaning Methods 0.000 claims abstract description 22
- 239000006260 foam Substances 0.000 claims abstract description 11
- 239000002351 wastewater Substances 0.000 claims description 23
- 238000004659 sterilization and disinfection Methods 0.000 claims description 17
- 238000005406 washing Methods 0.000 claims description 15
- 239000003814 drug Substances 0.000 claims description 13
- 238000005276 aerator Methods 0.000 claims description 11
- 238000001914 filtration Methods 0.000 claims description 9
- 239000010865 sewage Substances 0.000 claims description 9
- 238000001556 precipitation Methods 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims 2
- 230000000630 rising effect Effects 0.000 claims 2
- 230000001954 sterilising effect Effects 0.000 claims 2
- 238000011001 backwashing Methods 0.000 claims 1
- 230000007423 decrease Effects 0.000 claims 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims 1
- 239000000377 silicon dioxide Substances 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 38
- 238000003756 stirring Methods 0.000 abstract description 21
- 238000005345 coagulation Methods 0.000 abstract description 17
- 230000015271 coagulation Effects 0.000 abstract description 17
- 238000004062 sedimentation Methods 0.000 abstract description 12
- 239000010802 sludge Substances 0.000 abstract description 11
- 230000001590 oxidative effect Effects 0.000 abstract description 7
- 239000012528 membrane Substances 0.000 abstract description 6
- 238000012423 maintenance Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 11
- 238000007254 oxidation reaction Methods 0.000 description 9
- 239000002131 composite material Substances 0.000 description 7
- 239000003921 oil Substances 0.000 description 7
- 230000003647 oxidation Effects 0.000 description 7
- 238000005352 clarification Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 229940079593 drug Drugs 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 239000007800 oxidant agent Substances 0.000 description 3
- 239000004094 surface-active agent Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- 239000000645 desinfectant Substances 0.000 description 2
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 2
- 239000003623 enhancer Substances 0.000 description 2
- 238000005188 flotation Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 229920002401 polyacrylamide Polymers 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000004155 Chlorine dioxide Substances 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 description 1
- CYUOWZRAOZFACA-UHFFFAOYSA-N aluminum iron Chemical compound [Al].[Fe] CYUOWZRAOZFACA-UHFFFAOYSA-N 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 235000019398 chlorine dioxide Nutrition 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 230000035790 physiological processes and functions Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
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- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
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Classifications
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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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- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Physical Water Treatments (AREA)
Abstract
本实用新型属于废水处理设备领域,具体是一种小型洗车场洗车废水处理设备,该设备主要结构是一个曝气氧化混凝沉淀反应器(32),它由反应罐(33)、搅拌设备和曝气系统构成,搅拌设备位于反应罐(33)罐内的上部,曝气系统的膜片式曝气头(3)位于反应罐(33)罐内的下部,搅拌设备由搅拌电机(10)、搅拌叶片(11)构成,搅拌电机(10)的下部设置有刮泥板(12)、下部设置有污泥罩(19),反应罐(33)的侧壁设置有水位探测器(9)和半圆型泡沫浮渣收集槽(13)、反应罐(33)的一侧还设置有进、出水系统以及自清洗过滤系统,产品的主体设备具有体积小,操作方便,易于维护,便于移动,经济适用的特点。
The utility model belongs to the field of waste water treatment equipment, in particular to a small car wash waste water treatment equipment. The main structure of the equipment is an aeration oxidative coagulation sedimentation reactor (32), which consists of a reaction tank (33), a stirring device and The aeration system is composed of a stirring device located at the top of the reaction tank (33), and the membrane type aeration head (3) of the aeration system is located at the bottom of the reaction tank (33), and the stirring device is controlled by a stirring motor (10) , stirring blades (11), the bottom of the stirring motor (10) is provided with a mud scraper (12), the bottom is provided with a sludge cover (19), and the side wall of the reaction tank (33) is provided with a water level detector (9) One side of the semicircular foam scum collection tank (13) and the reaction tank (33) is also provided with an inlet and outlet system and a self-cleaning filter system. The main equipment of the product has small volume, easy operation, easy maintenance, and convenient movement. Economical and applicable features.
Description
技术领域:本实用新型属于一种废水处理设备领域,具体是一种小型洗车场洗车废水处理设备。Technical field: The utility model belongs to the field of wastewater treatment equipment, in particular to a small car wash wastewater treatment equipment for car washing.
背景技术:现有洗车废水处理回用工艺中,膜生物反应器处理废水工艺虽然出水水质稳定,运行管理简单,但该工艺需采用连续运行方式,以保持活性污泥的活性,同时要求反应器进水温度不能低于8℃,否则活性污泥的活性将会受到一定的影响,此时工艺还需避免微生物新陈代谢有抑制作用的消毒剂,否则微生物的正常生理机能将受到破坏,从而导致出水恶化,故而膜生物反应处理废水工艺不太适合间隙运行方式的小型洗车场的废水处理和气温较低地区和北方冬天使用,其使用范围受到气温和地域的限制。Background technology: In the existing car wash wastewater treatment and reuse process, although the effluent quality of the membrane bioreactor wastewater treatment process is stable and the operation and management are simple, the process needs to adopt a continuous operation mode to maintain the activity of the activated sludge. At the same time, the reactor is required to The temperature of the inlet water should not be lower than 8°C, otherwise the activity of the activated sludge will be affected to a certain extent. At this time, the process needs to avoid disinfectants that can inhibit the metabolism of microorganisms, otherwise the normal physiological functions of microorganisms will be destroyed, resulting in water discharge Therefore, the membrane biological reaction wastewater treatment process is not suitable for the wastewater treatment of small car washes in the intermittent operation mode and the use in low temperature areas and northern winters, and its application range is limited by temperature and region.
此外,目前采用的物理化学处理洗车废水工艺,一般包括沉砂、除油、混凝沉淀、气浮、砂滤、活性炭吸附、膜组件处理、消毒等工序,自动化程度高,出水稳定,能达到洗车场废水回用标准,但设备投资较高,技术要求高,不能被分布分散、经济效益不高的小型洗车场采用;而市场上仅采用简单混凝处理的洗车废水处理设备,对有机物、油类以及表面活性剂处理效果又不理想,很难达到回用水目的。In addition, the current physical and chemical treatment of car wash wastewater generally includes sand settling, oil removal, coagulation sedimentation, air flotation, sand filtration, activated carbon adsorption, membrane module treatment, disinfection and other processes, with a high degree of automation and stable water output. Car wash wastewater reuse standard, but the investment in equipment is high and the technical requirements are high, so it cannot be used by small car washes with scattered distribution and low economic benefits; while the car wash wastewater treatment equipment that only uses simple coagulation treatment on the market is not effective for organic matter, The treatment effect of oil and surfactant is not ideal, and it is difficult to achieve the purpose of water reuse.
发明内容:本实用新型的目的在于克服目前膜生物反应器处理小型洗车场废水工艺及设备的不足和物理化学膜组件处理洗车场废水工艺及设备技术复杂、成本高的问题,为人们提供一种不受气温和地域的限制、经济实用、对有机物、油类以及表面活性剂处理效果较理想的小型洗车场洗车废水处理设备。Summary of the invention: The purpose of this utility model is to overcome the current membrane bioreactor's lack of technology and equipment for treating small-scale car wash wastewater and the problems of complex technology and high cost of physical and chemical membrane modules for treating car wash wastewater, and to provide people with a It is not limited by temperature and region, economical and practical, and has an ideal treatment effect on organic matter, oil and surfactants. It is a small-scale car wash wastewater treatment equipment for car washes.
本实用新型的目的是通过下述技术方案来实现的:The purpose of this utility model is achieved through the following technical solutions:
本实用新型的小型洗车场洗车废水处理设备,主要是一个曝气氧化混凝沉淀反应器32,它由反应罐33、搅拌设备和曝气系统构成,搅拌设备位于反应罐33罐内的上部,曝气系统的膜片式曝气头3位于反应罐33罐内的下部,反应罐33上还设置有加药孔34.The utility model's small-scale car wash waste water treatment equipment is mainly an aeration oxidative
上述方案中,所述搅拌设备由搅拌电机10、搅拌叶片11构成,搅拌电机10的下部设置有刮泥板12、下部设置有污泥罩19。In the above solution, the stirring equipment is composed of a stirring motor 10 and a stirring blade 11 , a
上述方案中,所述反应罐33的侧壁设置有水位探测器9和半圆型泡沫浮渣收集槽13、泡沫浮渣收集槽13与泡沫水溢流管14连通。In the above scheme, the side wall of the
上述方案中,所述曝气系统由膜片式微曝气头3、曝气机4、进气阀5构成,曝气机4和进气阀5位于反应罐33底部的外侧。In the above solution, the aeration system is composed of a
上述方案中,所述加药孔34与加药系统连接,加药系统由抽药泵6、加药阀a7、加药阀b15、加药阀c17、加药箱a8、加药箱b16、加药箱c18构成,加药系统通过抽药泵6与反应罐33上的加药孔34连接。In the above scheme, the dosing hole 34 is connected to the dosing system, and the dosing system consists of a dosing pump 6, a dosing valve a7, a dosing valve b15, a dosing valve c17, a dosing box a8, a dosing box b16, The dosing box c18 is formed, and the dosing system is connected with the dosing hole 34 on the
上述方案中,所述反应罐33的一侧还设置有进、出水系统,进、出水系统由废水进水阀2、抽水泵1、余水放水阀20构成,并通过抽水泵1与反应罐33相连。In the above scheme, one side of the
上述方案中,所述反应罐33的一侧还设置有自清洗过滤系统,自清洗过滤系统由自清洗过滤器21、过滤器进水阀22、排污口30、出水管23构成,自清洗过滤系统经过滤器进水阀22、进、出水系统的抽水泵1与反应罐33相连。自清洗过滤系统的出水管23与消毒曝气澄清池24连通。In the above scheme, one side of the
上述方案中,所述反应罐33的一侧还设置有反冲洗阀29、底部设置有排泥阀28。In the above solution, the
上述方案中,所述消毒曝气澄清池24上分别设置有多孔曝气管26、排污阀27、澄清液溢流出水口31,多孔曝气管26与曝气澄清池进气阀25连通。In the above scheme, the
上述方案中,曝气氧化混凝沉淀反应器32、曝气系统、加药系统、进、出水系统、反冲洗系统、自清洗过滤系统集成一体构成洗车废水处理设备主体,设置在同一机架上。消毒澄清池24离机设置。In the above scheme, the aeration oxidative
上述方案中,外围设施构筑物集水井进水口与洗车场地下网格式过水沟相连,出水口设置格栅和吸油毡,通过废水进水阀2与抽水泵1相连。In the above scheme, the water inlet of the water collection well of the peripheral facilities and structures is connected to the underground mesh ditch of the car wash site, and the outlet is provided with a grille and oil-absorbing felt, and is connected to the water pump 1 through the waste water inlet valve 2 .
本实用新型小型洗车场废水处理设备是发明人通过长期实践摸索出来的科学实用的技术方案,采用本实用新型的设备后,小型洗车场废水处理技术即可结合本设备采用复合氧化剂进行曝气氧化,强化对有机物、油类、表面活性剂的氧化降解,增强多元复合无机絮凝剂-有机助凝剂混凝沉淀效果,且采用由多功能搅拌器和曝气系统构成的曝气氧化混凝沉淀反应器,将氧化反应、气浮、混凝沉淀集为一体的反应器以及5μ自清洗过滤器,和辅以集水井出口格栅除渣、吸油毡除油,消毒曝气澄清池曝气消毒处理,使得处理出水水质好于以往仅采用简单混凝、过滤、消毒处理工艺出水水质,其主体设备体积小,操作方便,易于维护,便于移动,经济适用。The utility model of small-scale car wash wastewater treatment equipment is a scientific and practical technical solution explored by the inventor through long-term practice. After adopting the utility model, the small-scale car wash wastewater treatment technology can be combined with this equipment to use composite oxidants for aeration and oxidation , strengthen the oxidative degradation of organic matter, oils, and surfactants, enhance the coagulation and sedimentation effect of the multi-component composite inorganic flocculant-organic coagulant aid, and adopt an aerated oxidative coagulation sedimentation system composed of a multifunctional agitator and an aeration system Reactor, a reactor that integrates oxidation reaction, air flotation, coagulation and sedimentation, and a 5μ self-cleaning filter, supplemented by grid removal at the outlet of the water collection well, oil removal with linoleum, and aeration disinfection in the aeration and clarification tank The treatment makes the water quality of the treated water better than that of the past with only simple coagulation, filtration, and disinfection treatment processes. The main equipment is small in size, easy to operate, easy to maintain, easy to move, and economical and applicable.
附图说明:Description of drawings:
图1本实用新型废水处理设备结构示意图。Fig. 1 is a structural schematic diagram of the wastewater treatment equipment of the utility model.
图中:1、抽水泵;2、废水进水阀;3、膜片式微曝气头;4、曝气机;5、进气阀;6、抽药泵;7、加药阀a;8、加药箱a;9、水位探测器;10、搅拌电机;11、搅拌叶片;12、刮泥板;13、泡沫浮渣收集槽;14、泡沫水溢流管;15、加药阀b;16、加药箱b;17、加药阀c;18、加药箱c;19、污泥罩;20、余水放水阀;21、自清洗过滤器;22、过滤器进水阀;23、过滤器出水管;24、消毒曝气澄清池;25、进气阀;26、多孔曝气管;27、排污阀;28、排泥阀;29、自来水反冲洗阀;30、过滤器排污口;31、澄清液溢流出水口;32、曝气氧化混凝沉淀反应器;33、反应罐;34、加药孔。In the figure: 1. Suction pump; 2. Waste water inlet valve; 3. Diaphragm micro-aeration head; 4. Aerator; 5. Air intake valve; 6. Pumping pump; 7. Dosing valve a; 8 1. Dosing box a; 9. Water level detector; 10. Stirring motor; 11. Stirring blade; 12. Scraper; 13. Foam scum collection tank; 14. Foam water overflow pipe; 15. Dosing valve b ; 16. Dosing box b; 17. Dosing valve c; 18. Dosing box c; 19. Sludge cover; 20. Remaining water discharge valve; 21. Self-cleaning filter; 22. Filter inlet valve; 23. Filter outlet pipe; 24. Disinfection aeration clarifier; 25. Air intake valve; 26. Porous aeration pipe; 27. Sewage valve; 28. Mud discharge valve; 29. Tap water backwash valve; 30. Filter Sewage outlet; 31. Clarified liquid overflow outlet; 32. Aeration oxidation coagulation sedimentation reactor; 33. Reaction tank; 34. Dosing hole.
具体实施方式:Detailed ways:
下面结合实施例进一步详述本实用新型,但本实用新型不仅限于所述实施例。Further describe the utility model in detail below in conjunction with embodiment, but the utility model is not limited to described embodiment.
实施例1:Example 1:
如图1所示:本实用新型应用于小型洗车场洗车废水处理的设备,主要结构是一个曝气氧化混凝沉淀反应器32,它由反应罐33、搅拌设备和曝气系统构成,搅拌设备位于反应罐33罐内的上部,曝气系统的膜片式曝气头3位于反应罐33罐内的下部,反应罐33上还设置有加药孔34。本例也可以不设置加药孔34,直接通过反应罐33顶部开孔进行人工加药。As shown in Figure 1: the utility model is applied to the equipment for the treatment of car washing wastewater in small car washes. It is located at the upper part of the
如图1所示:本例所述搅拌设备由搅拌电机10、搅拌叶片11构成,搅拌电机10的下部设置有刮泥板12、下底部设置有污泥罩19。As shown in FIG. 1 : the mixing equipment described in this example is composed of a stirring motor 10 and a stirring blade 11 , a
如图1所示:本例所述反应罐33的侧壁设置有水位探测器9和半圆型泡沫浮渣收集槽13、泡沫浮渣收集槽13与泡沫水溢流管14连通。As shown in FIG. 1 : the side wall of the
如图1所示:本例所述曝气系统由膜片式微曝气头3、曝气机4、进气阀5构成,曝气机4和进气阀5位于反应罐33底部的外侧。As shown in Figure 1: the aeration system described in this example consists of a
如图1所示:本例所述加药孔34与加药系统连接,加药系统由抽药泵6、加药阀a7、加药阀b15、加药箱c17、加药箱a8、加药箱b16、加药箱c18构成,加药系统通过抽药泵6与反应罐33上的加药孔34连接。As shown in Figure 1: the dosing hole 34 described in this example is connected to the dosing system, and the dosing system consists of a dosing pump 6, a dosing valve a7, a dosing valve b15, a dosing box c17, a dosing box a8, a dosing system The medicine box b16 and the medicine adding box c18 are formed, and the medicine adding system is connected with the medicine adding hole 34 on the
如图1所示:本例所述反应罐33的一侧还设置有进、出水系统,进、出水系统由废水进水阀2、抽水泵1、余水放水阀20构成,并通过抽水泵1与反应罐33相连。As shown in Figure 1: one side of the
如图1所示:本例所述反应罐33的一侧还设置有自清洗过滤系统,自清洗过滤系统由自清洗过滤器21、过滤器进水阀22、排污口30、出水管23构成,自清洗过滤系统经过滤器进水阀22、进、出水系统的抽水泵1与反应罐33相连。自清洗过滤系统的出水管23与消毒曝气澄清池24连通。As shown in Figure 1: one side of the
如图1所示:本例所述反应罐33的一侧还设置有反冲洗阀29、底部设置有排泥阀28。As shown in FIG. 1 , a
如图1所示:本例所述消毒曝气澄清池24上分别设置有多孔曝气管26、排污阀27、澄清液溢流出水口31,多孔曝气管26与曝气澄清池进气阀25连通。As shown in Figure 1: the disinfection
如图1所示:本例曝气氧化混凝沉淀反应器32、曝气系统、加药系统、进、出水系统、反冲洗系统、自清洗过滤系统集成一体构成洗车废水处理设备主体,设置在同一机架上。本例所述曝气氧化混凝沉淀反应器32、曝气系统、加药系统、进、出水系统、反冲洗系统、自清洗过滤系统的具体结构也可以进行任意改进和设计,不仅限于上述实施例。消毒澄清池24离机设置。As shown in Figure 1: In this example, the aeration oxidative
如图1所示:本例外围设施构筑物集水井进水口与洗车场地下网格式过水沟相连,出水口设置格栅和吸油毡,通过废水进水阀2与抽水泵1相连。As shown in Figure 1: the water inlet of the water collection well of the peripheral facilities and structures in this example is connected to the underground mesh ditch of the car wash, the outlet is provided with a grille and oil-absorbing felt, and is connected to the pump 1 through the waste water inlet valve 2.
下面通过处理方法及工作过程进一步描述本实用新型的设备。The equipment of the present utility model is further described below through processing method and working process.
本例采用如下方法对废水进行处理:In this example, the following methods are used to treat wastewater:
(1)用2%浓度复合氧化剂4ml/L,在中性至微碱性下,曝气氧化30min;本例所述复合氧化剂由成都市光洁环保生物科技有限公司提供。(1) Use 4 ml/L of 2% composite oxidant, and aerate and oxidize for 30 minutes under neutral to slightly alkaline conditions; the composite oxidant described in this example is provided by Chengdu Guangjie Environmental Protection Biotechnology Co., Ltd.
(2)用9%浓度复合无机絮凝剂聚合硅酸铝铁25ml/L,控制PH8.5左右搅拌絮凝5min;(2) Use 25ml/L of composite inorganic flocculant to polymerize ferric aluminum silicate at a concentration of 9%, and control the pH to about 8.5 to stir and flocculate for 5 minutes;
(3)用0.1%浓度聚丙烯酰胺20ml/L,控制PH8.5左右混凝沉淀10min;(3) Use 0.1% polyacrylamide 20ml/L to control pH8.5 for coagulation and precipitation for 10 minutes;
(4)处理水上清液抽至5μ自清洗过滤器过滤;(4) The treated water supernatant is pumped to a 5μ self-cleaning filter for filtration;
(5)过滤出水进入消毒曝气池,投加有效氯为20mg/L的二氧化氯碱性曝气消毒,澄清液回用洗车。(5) Filter the water into the disinfection aeration tank, add chlorine dioxide alkaline aeration disinfection with an available chlorine of 20 mg/L, and reuse the clarified liquid for car washing.
以上实例所述组分不仅限于本例。The components described in the above examples are not limited to this example.
具体废水处理步骤如下所述:The specific wastewater treatment steps are as follows:
1)洗车废水通过洗车场地下格网过水沟收集至集水井,进行初沉;1) The car washing wastewater is collected through the underground grid of the car washing site through the ditch to the water collection well for primary sedimentation;
2)启动抽水泵1,洗车废水经格栅和隔油毡进一步去除固体杂物和浮油后,经进水阀2被抽入反应罐33底部,当进水淹没膜片式微曝气头3时,曝气机4启动,进气阀5打开,开始进行曝气,与此同时,抽药泵6启动,加药阀a7打开,开始投加加药箱a8中的复合氧化增强剂进行曝气氧化反应,此时搅拌电机10也同步启动,进行搅拌,复合氧化增强剂按预定药量加毕后,抽药泵6和加药阀a7关闭,刮泥板12将液面的泡沫和悬浮杂物刮至半圆型收集槽13中,经溢流管14排放至地下过水沟流回集水井,曝气氧化处理30min后,关闭曝气机4和进气阀5,与此同时,抽药泵6启动,加药阀b15打开,开始投加加药箱b16中多元复合无机高分子絮凝剂聚合硅酸铝铁进行凝聚反应,按预定药量投加完毕,关闭抽药泵6及加药阀b15,在35r/min、PH8.5左右凝聚反应5min,凝聚反应后,抽药泵6重新启动,打开加药阀c17,开始投加加药箱c18中的有机助凝剂聚丙烯酰胺进行混凝反应,按预定药量投加完毕,关闭抽药泵6及加药阀c17,在35r/min、PH8.5左右凝聚反应2min;混凝反应结束后,关闭搅拌电机10,多功能搅拌叶片11停止搅拌;静置10min进行沉淀,膜片式微曝气头3上方安装在多功能搅拌器11下端的污泥罩19挡着沉淀污泥,避免微曝气头3被污泥覆盖堵塞;沉降结束后,再次启动抽水泵1,打开余水阀20,放出管道中剩余污水,5s后关闭余水阀20,同时打开过滤器进水阀22,对氧化强化混凝出水进行过滤,过滤出水经自清洗过滤器21出水管23排至消毒曝气澄清池24;自清洗过滤器21中浓缩的浓渣液定期从其排污口30不停机直接排放至地下过水沟回流到集水井中;反应罐33中处理水排放至水位探测器9的下水位时,抽水泵1和自清洗过滤器21进水阀22关闭,打开反应罐33排泥阀28放泥,泥放完后,打开自来水反冲洗阀29冲洗5s分钟,排放的污泥和反冲洗经地下过水沟回流到集水井中。泥水排完后关闭排泥阀28和反冲洗阀29,第一循环处理过程结束后,重复上述2)过程进行第二循环处理,如此往复,对废水进行不间断处理。2) Start the water pump 1, and after the car wash waste water is further removed from solid debris and slick oil through the grille and oil separator, it is drawn into the bottom of the
收集至曝气澄清池24中的处理水经投消毒剂,打开消毒曝气池24的曝气阀25,通过多孔曝气管26进行间隙曝气、澄清,澄清水从消毒曝气澄清池上部溢流出水口31溢流出去,回用于洗车;沉淀则从漏斗状底部的排泥口27排至地下过水沟回流到集水井中;集水井定期清掏,污泥外运处理。The treated water collected in the aeration and
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