CN105481142A - Copper sheet grinding wastewater treatment and reuse system - Google Patents
Copper sheet grinding wastewater treatment and reuse system Download PDFInfo
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- CN105481142A CN105481142A CN201511002603.6A CN201511002603A CN105481142A CN 105481142 A CN105481142 A CN 105481142A CN 201511002603 A CN201511002603 A CN 201511002603A CN 105481142 A CN105481142 A CN 105481142A
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- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 21
- 239000010949 copper Substances 0.000 title claims abstract description 21
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 357
- 238000004140 cleaning Methods 0.000 claims abstract description 96
- 239000012528 membrane Substances 0.000 claims abstract description 58
- 239000010802 sludge Substances 0.000 claims abstract description 36
- 239000002351 wastewater Substances 0.000 claims abstract description 35
- 238000006243 chemical reaction Methods 0.000 claims abstract description 29
- 239000000706 filtrate Substances 0.000 claims abstract description 16
- 238000000034 method Methods 0.000 claims abstract description 10
- 230000008569 process Effects 0.000 claims abstract description 9
- 239000007788 liquid Substances 0.000 claims description 23
- 239000003814 drug Substances 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 4
- 230000000630 rising effect Effects 0.000 claims 12
- 238000011010 flushing procedure Methods 0.000 claims 6
- 239000003657 drainage water Substances 0.000 claims 4
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims 4
- 239000003513 alkali Substances 0.000 claims 1
- 239000002562 thickening agent Substances 0.000 claims 1
- 238000001471 micro-filtration Methods 0.000 abstract description 32
- 238000004064 recycling Methods 0.000 abstract description 13
- 230000007613 environmental effect Effects 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 238000004134 energy conservation Methods 0.000 abstract 1
- 238000001914 filtration Methods 0.000 abstract 1
- 230000008719 thickening Effects 0.000 description 11
- 150000002500 ions Chemical class 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 229910001385 heavy metal Inorganic materials 0.000 description 5
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 229910019142 PO4 Inorganic materials 0.000 description 2
- 238000009713 electroplating Methods 0.000 description 2
- 238000005374 membrane filtration Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 229910021502 aluminium hydroxide Inorganic materials 0.000 description 1
- 150000001495 arsenic compounds Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000009295 crossflow filtration Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 150000002222 fluorine compounds Chemical class 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 229910001679 gibbsite Inorganic materials 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 229940093920 gynecological arsenic compound Drugs 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000012629 purifying agent Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/16—Use of chemical agents
- B01D2321/162—Use of acids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/16—Use of chemical agents
- B01D2321/164—Use of bases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
技术领域technical field
本发明涉及废水处理领域技术,尤其是指一种铜片研磨废水处理回用系统。The invention relates to the technology in the field of waste water treatment, in particular to a copper sheet grinding waste water treatment and reuse system.
背景技术Background technique
铜片研磨工序中,会产生一些铜粉末,这些铜粉末随着水洗过程被水带走,形成磨板废水,含铜废水排放,会对环境造成危害,也造成了铜及水资源的浪费;现有技术中针对铜片研磨废水的处理系统,存在处理效率较低,难以有效处理达标等不足,同时,在处理流程中,需要添加较多的絮凝剂、水处理药剂(如PAM、PAC等)等。During the copper sheet grinding process, some copper powder will be produced. These copper powders will be taken away by water during the washing process to form grinding plate wastewater. The discharge of copper-containing wastewater will cause harm to the environment and cause waste of copper and water resources; In the existing technology, the treatment system for copper sheet grinding wastewater has low treatment efficiency, and it is difficult to effectively treat the standard. At the same time, in the treatment process, more flocculants and water treatment chemicals (such as PAM, PAC, etc.) need to be added. )Wait.
因此,需要研究出一种新的技术方案来解决上述问题。Therefore, a new technical solution needs to be developed to solve the above problems.
发明内容Contents of the invention
有鉴于此,本发明针对现有技术存在之缺失,其主要目的是提供一种铜片研磨废水处理回用系统,其具有自动化程度高、操作简单、可按需控制间隙运行、可按需调节产水流量、水处理药剂添加少、过滤水质可靠、处理回用效率高、环保节能及资源回用等诸多优势。In view of this, the present invention aims at the deficiencies in the prior art, and its main purpose is to provide a copper sheet grinding wastewater treatment and recycling system, which has a high degree of automation, simple operation, and can control the gap operation on demand and can be adjusted on demand. There are many advantages such as the flow rate of produced water, less addition of water treatment chemicals, reliable filtered water quality, high treatment and reuse efficiency, environmental protection and energy saving, and resource reuse.
为实现上述目的,本发明采用如下之技术方案:To achieve the above object, the present invention adopts the following technical solutions:
一种铜片研磨废水处理回用系统,包括有电控制单元、废水收集池、反应水箱、浓缩水箱、管式微滤膜装置、回用水箱、污泥浓缩装置、滤液箱及滤膜清洗系统;其中,该废水收集池、反应水箱、浓缩水箱、管式微滤膜装置、回用水箱依工艺流程依次连接;A system for treating and recycling copper sheet grinding wastewater, including an electric control unit, a wastewater collection tank, a reaction water tank, a concentration water tank, a tubular microfiltration membrane device, a reuse water tank, a sludge concentration device, a filtrate tank, and a filter membrane cleaning system; Among them, the wastewater collection tank, reaction water tank, concentrated water tank, tubular microfiltration membrane device, and reuse water tank are connected in sequence according to the process flow;
该废水收集池的出水端连接反应水箱的入水端,该反应水箱的出水端连接浓缩水箱的入水端,该浓缩水箱具有出水端和湿污泥输出端,该浓缩水箱的出水端连接管式微滤膜装置入水端,该管式微滤膜装置的出水端包括有滤水出水端和浓水出水端,该管式微滤膜装置的滤水出水端连接回用水箱的入水端,该管式微滤膜装置的浓水出水端连接前述浓缩水箱的入水端;The water outlet of the wastewater collection tank is connected to the water inlet of the reaction water tank, the water outlet of the reaction water tank is connected to the water inlet of the concentrated water tank, the concentrated water tank has a water outlet and a wet sludge output, and the water outlet of the concentrated water tank is connected to the tubular microfiltration The water inlet end of the membrane device. The water outlet end of the tubular microfiltration membrane device includes a filtered water outlet end and a concentrated water outlet end. The filtered water outlet end of the tubular microfiltration membrane device is connected to the water inlet end of the reuse water tank. The concentrated water outlet end of the device is connected to the water inlet end of the aforementioned concentrated water tank;
该浓缩水箱的湿污泥输出端经污泥泵连接至污泥浓缩装置,该污泥浓缩装置具有污泥滤水输出端和浓缩污泥输出端,该污泥滤水输出端连接于滤液箱,该滤液箱的出水端经滤液泵连接前述浓缩水箱的入水端;The wet sludge output end of the concentrated water tank is connected to the sludge thickening device through the sludge pump, and the sludge thickening device has a sludge filter water output end and a concentrated sludge output end, and the sludge filter water output end is connected to the filtrate tank , the water outlet end of the filtrate tank is connected to the water inlet end of the aforementioned concentrated water tank through the filtrate pump;
该滤膜清洗系统包括有第一清洗水箱、第二清洗水箱、第三清洗水箱及清洗水泵,前述管式微滤膜装置的滤水出水端还连接有第一清洗出水管,前述管式微滤膜装置的浓水出水端还连接有第二清洗出水管,该第一清洗出水管、第二清洗出水管的出水侧共同连接于共用管道上,该共用管道具有清洗废水排放口,该清洗废水排放口连接至前述废水收集池;该第一清洗水箱的入水端经第一进水管连接共用管道,该第二清洗水箱的入水端经第二进水管连接共用管道,该第三清洗水箱的入水端经第三进水管连接共用管道,该第一清洗水箱的出水端经第一出水管连接至清洗水泵的入水端,该第二清洗水箱的出水端经第二出水管连接至清洗水泵的入水端,该第三清洗水箱的出水端经第三出水管连接至清洗水泵的入水端,该清洗水泵的出水端经清洗入水管连接至管式微滤膜装置入水端;管式微滤膜装置的浓水出水端与浓缩水箱之间的连接管道上、浓缩水箱的出水端与管式微滤膜装置入水端之间的连接管道上、管式微滤膜装置的滤水出水端与回用水箱之间的连接管道上、清洗入水管上、第一清洗出水管、第二清洗出水管、第一进水管、第二进水管、第三进水管、共用管道、第一出水管、第二出水管及第三出水管均设置有开关。The filter membrane cleaning system includes a first cleaning water tank, a second cleaning water tank, a third cleaning water tank and a cleaning water pump. The concentrated water outlet end of the device is also connected with a second cleaning outlet pipe, the water outlet sides of the first cleaning outlet pipe and the second cleaning outlet pipe are jointly connected to a common pipeline, and the shared pipeline has a cleaning wastewater discharge port, and the cleaning wastewater is discharged The water inlet of the first cleaning water tank is connected to the common pipeline through the first water inlet pipe, the water inlet of the second cleaning water tank is connected to the common pipeline through the second water inlet pipe, and the water inlet of the third cleaning water tank is connected to the common pipeline through the second water inlet pipe. Connect the common pipeline through the third water inlet pipe, the water outlet end of the first cleaning water tank is connected to the water inlet end of the cleaning water pump through the first water outlet pipe, and the water outlet end of the second cleaning water tank is connected to the water inlet end of the cleaning water pump through the second water outlet pipe , the water outlet end of the third cleaning water tank is connected to the water inlet end of the cleaning water pump through the third water outlet pipe, and the water outlet end of the cleaning water pump is connected to the water inlet end of the tubular microfiltration membrane device through the cleaning water inlet pipe; the concentrated water of the tubular microfiltration membrane device On the connecting pipe between the water outlet and the concentrated water tank, on the connecting pipe between the water outlet of the concentrated water tank and the water inlet of the tubular microfiltration membrane device, and between the filtered water outlet of the tubular microfiltration membrane device and the reuse water tank On the pipeline, on the cleaning water inlet pipe, on the first cleaning water outlet pipe, on the second cleaning water outlet pipe, on the first water inlet pipe, on the second water inlet pipe, on the third water inlet pipe, on the common pipe, on the first water outlet pipe, on the second water outlet pipe and on the third The outlet pipes are all provided with switches.
作为一种优选方案,所述清洗水泵的出水端还连接有药水排放管,该排放管上设置有排放开关。As a preferred solution, the water outlet of the cleaning water pump is also connected with a liquid medicine discharge pipe, and a discharge switch is arranged on the discharge pipe.
作为一种优选方案,所述废水收集池的出水端与反应水箱的入水端之间通过提升泵连接,所述反应水箱的出水端高于浓缩水箱的入水端。As a preferred solution, the water outlet of the wastewater collection tank is connected to the water inlet of the reaction water tank through a lift pump, and the water outlet of the reaction water tank is higher than the water inlet of the concentrated water tank.
作为一种优选方案,所述污泥浓缩装置为污泥浓缩池或压滤机,所述污泥泵为气动隔膜泵。As a preferred solution, the sludge thickening device is a sludge thickening tank or a filter press, and the sludge pump is a pneumatic diaphragm pump.
作为一种优选方案,所述浓缩水箱里设置有液位计,该液位计的信息反馈至前述电控制单元;前述浓缩水箱的出水端经循环泵连接至管式微滤膜装置入水端,前述电控制单元根据液位计的信息控制循环泵的启闭。As a preferred solution, a liquid level gauge is provided in the concentrated water tank, and the information of the liquid level gauge is fed back to the aforementioned electric control unit; the water outlet end of the aforementioned concentrated water tank is connected to the water inlet end of the tubular microfiltration membrane device through a circulation pump, and the aforementioned The electric control unit controls the opening and closing of the circulation pump according to the information of the liquid level gauge.
作为一种优选方案,所述反应水箱连接有碱液加药箱和PAC加药箱,所述反应水箱内设置有液位计和PH计。As a preferred solution, the reaction water tank is connected with a lye dosing box and a PAC dosing box, and a liquid level gauge and a pH meter are arranged in the reaction water tank.
作为一种优选方案,所述回用水箱连接有酸液加药箱,所述回用水箱内设置有液位计和PH计,所述回用水箱连接有回用水排放管,该回用水排放管连接有回用水泵。As a preferred solution, the reclaimed water tank is connected with an acid dosing tank, a liquid level gauge and a PH meter are arranged in the reclaimed water tank, a reclaimed water discharge pipe is connected to the reclaimed water tank, and the reclaimed water is discharged The pipe is connected to the return water pump.
本发明与现有技术相比具有明显的优点和有益效果,具体而言,由上述技术方案可知,其主要是通过电控制单元、废水收集池、反应水箱、浓缩水箱、管式微滤膜装置、回用水箱、污泥浓缩装置、滤液箱及滤膜清洗系统的设计及相互配合,使得本发明之铜片研磨废水处理回用系统具有自动化程度高、操作简单、可按需控制间隙运行、可按需调节产水流量、水处理药剂添加少、过滤水质可靠、处理回用效率高、环保节能及资源回用等诸多优势,适于推广应用。Compared with the prior art, the present invention has obvious advantages and beneficial effects. Specifically, it can be seen from the above technical scheme that it is mainly through the electric control unit, waste water collection pool, reaction water tank, concentrated water tank, tubular microfiltration membrane device, The design and mutual cooperation of the reuse water tank, the sludge thickening device, the filtrate tank and the filter membrane cleaning system make the copper sheet grinding wastewater treatment and reuse system of the present invention have a high degree of automation, simple operation, and can control the gap operation as required. Adjusting the flow rate of produced water on demand, adding less water treatment chemicals, reliable filtered water quality, high treatment and recycling efficiency, environmental protection, energy saving and resource recycling, etc., are suitable for popularization and application.
为更清楚地阐述本发明的结构特征和功效,下面结合附图与具体实施例来对本发明进行详细说明。In order to more clearly illustrate the structural features and functions of the present invention, the present invention will be described in detail below in conjunction with the accompanying drawings and specific embodiments.
附图说明Description of drawings
图1是本发明之实施例的大致结构连接示意图。Fig. 1 is a schematic structural connection diagram of an embodiment of the present invention.
附图标识说明:Explanation of the accompanying drawings:
1、废水收集池2、反应水箱1. Wastewater collection pool 2. Reaction water tank
3、浓缩水箱4、管式微滤膜装置3. Concentrated water tank 4. Tubular microfiltration membrane device
5、回用水箱6、污泥浓缩装置5. Reuse water tank 6. Sludge thickening device
7、滤液箱8、提升泵7. Filtrate tank 8. Lift pump
9、循环泵10、污泥泵9. Circulation pump 10. Sludge pump
11、滤液泵12、清洗水泵11. Filtrate pump 12. Cleaning water pump
13、第一清洗水箱14、第二清洗水箱13. The first cleaning water tank 14. The second cleaning water tank
15、第三清洗水箱16、清洗入水管15. The third cleaning water tank 16. Cleaning water inlet pipe
17、第一清洗出水管18、第二清洗出水管17. The first cleaning outlet pipe 18. The second cleaning outlet pipe
19、共用管道20、清洗废水排放口19. Shared pipeline 20. Cleaning waste water discharge port
21、第一进水管22、第二进水管21. The first water inlet pipe 22. The second water inlet pipe
23、第三进水管24、药水排放管23. The third water inlet pipe 24. The liquid medicine discharge pipe
25、药水排放开关26、回用水排放管25. Potion discharge switch 26. Recycled water discharge pipe
27、回用水泵28、液位计27. Reuse water pump 28. Liquid level gauge
29、PH计30、碱液加药箱29, PH meter 30, lye dosing box
31、PAC加药箱32、酸液加药箱31. PAC dosing box 32. Acid dosing box
33、第一出水管34、第二出水管33. The first water outlet pipe 34. The second water outlet pipe
35、第三出水管。35. The third outlet pipe.
具体实施方式detailed description
请参照图1所示,其显示出了本发明之实施例的具体结构,其包括有电控制单元、废水收集池1、反应水箱2、浓缩水箱3、管式微滤膜装置4、回用水箱5、污泥浓缩装置6、滤液箱7及滤膜清洗系统。Please refer to shown in Fig. 1, it has shown the specific structure of the embodiment of the present invention, and it comprises electric control unit, waste water collection pool 1, reaction water tank 2, concentrated water tank 3, tubular microfiltration membrane device 4, reuse water tank 5. Sludge thickening device 6, filtrate tank 7 and membrane cleaning system.
其中,该废水收集池1、反应水箱2、浓缩水箱3、管式微滤膜装置4、回用水箱5依工艺流程依次连接,该废水收集池1的出水端连接反应水箱2的入水端,反应水箱2的入水端会高于废水收集池1的出水端,所述废水收集池1的出水端与反应水箱2的入水端之间通过提升泵8连接,该反应水箱2的出水端连接浓缩水箱3的入水端,所述反应水箱2的出水端高于浓缩水箱3的入水端,如此,反应水箱2的出水是靠重力流入浓缩水箱3内。所述反应水箱2连接有碱液加药箱30和PAC加药箱31(此处所述的PAC是指聚合氯化铝,也称碱式氯化铝,其通常用作净水剂或混凝剂,它是介于AlCl3和Al(OH)3之间的一种水溶性无机高分子聚合物,化学通式为[Al2(OH)nCl6-n]m,其中m代表聚合程度,n表示PAC产品的中性程度),所述反应水箱2内设置有液位计28和PH计29。Wherein, the waste water collection tank 1, the reaction water tank 2, the concentrated water tank 3, the tubular microfiltration membrane device 4, and the reuse water tank 5 are sequentially connected according to the process flow, and the water outlet end of the waste water collection tank 1 is connected to the water inlet end of the reaction water tank 2, and the reaction The water inlet end of the water tank 2 will be higher than the water outlet end of the waste water collection tank 1, and the water outlet end of the waste water collection tank 1 and the water inlet end of the reaction water tank 2 are connected by a lift pump 8, and the water outlet end of the reaction water tank 2 is connected to the concentrated water tank 3, the water outlet end of the reaction water tank 2 is higher than the water inlet end of the concentrated water tank 3, so that the water outlet of the reaction water tank 2 flows into the concentrated water tank 3 by gravity. Described reaction water tank 2 is connected with lye dosing box 30 and PAC dosing box 31 (PAC described here refers to polyaluminum chloride, also claims basic aluminum chloride, and it is usually used as water purifying agent or mixed Coagulant, it is a water-soluble inorganic high molecular polymer between AlCl3 and Al(OH)3, the general chemical formula is [Al2(OH)nCl6-n]m, where m represents the degree of polymerization, n represents neutrality of PAC products), the reaction water tank 2 is provided with a liquid level gauge 28 and a pH gauge 29.
该浓缩水箱3具有出水端和湿污泥输出端,该浓缩水箱3的出水端连接管式微滤膜装置4入水端,所述浓缩水箱3里设置有液位计28,该液位计28的信息反馈至前述电控制单元;前述浓缩水箱3的出水端经循环泵9连接至管式微滤膜装置4入水端,前述电控制单元根据浓缩水箱3里液位计28的信息控制循环泵9的启闭,浓缩水箱3的设置主要是用于确保进入到管式微滤膜装置4内的水固定浓度在3%-5%之间;该管式微滤膜装置4的出水端包括有滤水出水端和浓水出水端,该管式微滤膜装置4的滤水出水端连接回用水箱5的入水端,此处,所述回用水箱5连接有酸液加药箱32,以在回用水箱5内对滤水进行PH调节,所述回用水箱5内设置有液位计28和PH计29,所述回用水箱5连接有回用水排放管26,该回用水排放管26连接有回用水泵27;该管式微滤膜装置4的浓水出水端连接前述浓缩水箱3的入水端。The concentrated water tank 3 has a water outlet and a wet sludge output end, the water outlet of the concentrated water tank 3 is connected to the water inlet of the tubular microfiltration membrane device 4, the concentrated water tank 3 is provided with a liquid level gauge 28, and the liquid level gauge 28 The information is fed back to the aforementioned electric control unit; the outlet end of the aforementioned concentrated water tank 3 is connected to the water inlet end of the tubular microfiltration membrane device 4 through the circulation pump 9, and the aforementioned electric control unit controls the flow of the circulating pump 9 according to the information of the liquid level gauge 28 in the concentrated water tank 3 Opening and closing, the setting of the concentrated water tank 3 is mainly used to ensure that the fixed concentration of water entering the tubular microfiltration membrane device 4 is between 3% and 5%; the water outlet of the tubular microfiltration membrane device 4 includes a filtered water outlet end and the concentrated water outlet end, the water outlet end of the tubular microfiltration membrane device 4 is connected to the water inlet end of the reuse water tank 5, and here, the reuse water tank 5 is connected with an acid liquid dosing tank 32 to The pH of the filtered water is adjusted in the tank 5, and a liquid level gauge 28 and a pH gauge 29 are arranged in the reuse water tank 5. The reuse water tank 5 is connected with a reuse water discharge pipe 26, and the reuse water discharge pipe 26 is connected with a Recycled water pump 27; the concentrated water outlet end of the tubular microfiltration membrane device 4 is connected to the water inlet end of the aforementioned concentrated water tank 3 .
该浓缩水箱3的湿污泥输出端经污泥泵10连接至污泥浓缩装置6,该污泥浓缩装置6具有污泥滤水输出端和浓缩污泥输出端,该污泥滤水输出端连接于滤液箱7,该滤液箱7的出水端经滤液泵11连接前述浓缩水箱3的入水端;所述污泥浓缩装置6为污泥浓缩池或压滤机(如板框压滤机),所述污泥泵10为气动隔膜泵,操作人员通常需要从前述浓缩水箱3里取样做一个简单的沉降测试,通过这个测试结果按需对气动隔膜泵进行现场调节,以控制气动隔膜泵的周期和频率。The wet sludge output end of the concentrated water tank 3 is connected to the sludge thickening device 6 through the sludge pump 10, and the sludge thickening device 6 has a sludge filter water output end and a concentrated sludge output end, and the sludge filter water output end Connected to the filtrate tank 7, the water outlet end of the filtrate tank 7 is connected to the water inlet end of the aforementioned concentrated water tank 3 through the filtrate pump 11; the sludge thickening device 6 is a sludge thickening tank or a filter press (such as a plate and frame filter press) , the sludge pump 10 is an air-operated diaphragm pump, and the operator usually needs to take a sample from the aforementioned concentrated water tank 3 to do a simple sedimentation test. Through this test result, the air-operated diaphragm pump is adjusted on-site as needed to control the air-operated diaphragm pump. period and frequency.
本技术中是采用了管式微滤膜工艺,其处理流程不添加任何絮凝剂,前述管式微滤膜装置4是依靠管式微滤膜将固体从溶液中分离出来的低压(0.7–7bar,10-100psig)分离设备,在实际应用中,可以根据实际需要通过增减膜的数量来获得相应产水流量;管式微滤膜装置是采用低压条件下通过管式膜过滤技术实现废水循环回用及物料回收,流过膜表面的水流能将截下来的颗粒物带走,而不聚集在膜表面,该膜系统在运行时,经过化学加药预处理后的废水高速流过管式膜,以保持湍流,在操作压力为20-80psi的条件下,干净的液体通过膜孔过滤出来,同时悬浮固体颗粒留在回流的液体中,回流液体保持湍流以防止颗粒物在膜的内层表面堆积,因此可以使该膜系统获得非常高的膜过滤通量,同时延长膜的使用寿命,这种湍流错流过滤以及大通道膜管去掉了对预处理的需求,可以处理重量比高达5%的高固体含量的液体。In this technology, the tubular microfiltration membrane process is adopted, and its treatment process does not add any flocculant. The aforementioned tubular microfiltration membrane device 4 is a low-pressure (0.7-7bar, 10- 100psig) separation equipment, in practical applications, the corresponding water flow rate can be obtained by increasing or decreasing the number of membranes according to actual needs; the tubular microfiltration membrane device uses tubular membrane filtration technology under low pressure to realize waste water recycling and material Recycling, the water flowing through the membrane surface can take the intercepted particles away without accumulating on the membrane surface. When the membrane system is in operation, the wastewater pretreated by chemical dosing flows through the tubular membrane at high speed to maintain turbulent flow. , under the condition of operating pressure of 20-80psi, the clean liquid is filtered out through the membrane pores, while the suspended solid particles remain in the return liquid, and the return liquid maintains turbulent flow to prevent particles from accumulating on the inner surface of the membrane, so it can make The membrane system achieves very high membrane filtration flux and prolongs the service life of the membrane. This turbulent cross-flow filtration and large channel membrane tube remove the need for pretreatment, and can handle high solids content up to 5% by weight. liquid.
前述管式微滤膜装置4在运行一段时间后,其膜需要清洗,本实施例中是通过对产水流量连续监测(可以通过产水压力计、流量计等来监测),当所监测到的流量低至预定值时,可以由电控单元自动控制下述滤膜清洗系统进行工作对膜进行化学清洗,利用酸性清洗液来清洗无机污垢,利用碱性清洗液(如NaClO)来去除有机物,在重新投入运行前,需要用新鲜水冲洗膜;可以根据膜组件的排列布置,对全部或部分膜进行自动清洗,清洗一次一般需要2~3个小时完成。After the aforementioned tubular microfiltration membrane device 4 has been in operation for a period of time, its membrane needs to be cleaned. In this embodiment, the flow rate of the product water is continuously monitored (it can be monitored by a pressure gauge of the product water, a flow meter, etc.), when the monitored flow rate When the value is lower than the predetermined value, the electronic control unit can automatically control the following filter membrane cleaning system to work to chemically clean the membrane, use acidic cleaning solution to clean inorganic dirt, and use alkaline cleaning solution (such as NaClO) to remove organic matter. Before putting into operation again, the membrane needs to be rinsed with fresh water; all or part of the membrane can be automatically cleaned according to the arrangement of the membrane modules, and it usually takes 2 to 3 hours to complete one cleaning.
具体而言,该滤膜清洗系统是就地清洗系统,其包括有第一清洗水箱13、第二清洗水箱14、第三清洗水箱15及清洗水泵12。Specifically, the membrane cleaning system is an in-situ cleaning system, which includes a first cleaning water tank 13 , a second cleaning water tank 14 , a third cleaning water tank 15 and a cleaning water pump 12 .
前述管式微滤膜装置4的滤水出水端还连接有第一清洗出水管17,前述管式微滤膜装置4的浓水出水端还连接有第二清洗出水管18,该第一清洗出水管17、第二清洗出水管18的出水侧共同连接于共用管道19上,该共用管道19具有清洗废水排放口20,该清洗废水排放口20连接至前述废水收集池1;该第一清洗水箱13的入水端经第一进水管21连接共用管道19,该第二清洗水箱14的入水端经第二进水管22连接共用管道19,该第三清洗水箱15的入水端经第三进水管23连接共用管道19,该第一清洗水箱13的出水端经第一出水管33连接至清洗水泵12的入水端,该第二清洗水箱的出水端经第二出水管34连接至清洗水泵的入水端,该第三清洗水箱15的出水端经第三出水管35连接至清洗水泵12的入水端,该清洗水泵12的出水端经清洗入水管16连接至管式微滤膜装置4入水端,以及,所述清洗水泵12的出水端还连接有药水排放管24,该药水排放管24上设置有排放开关,经药水排放管24排出的液体可以排至洗板废水处理系统中。The filtered water outlet end of the aforementioned tubular microfiltration membrane device 4 is also connected with a first cleaning outlet pipe 17, and the concentrated water outlet end of the aforementioned tubular microfiltration membrane device 4 is also connected with a second cleaning outlet pipe 18. The first cleaning outlet pipe 17. The water outlet side of the second cleaning outlet pipe 18 is jointly connected to the common pipeline 19, the common pipeline 19 has a cleaning wastewater discharge port 20, and the cleaning wastewater discharge port 20 is connected to the aforementioned wastewater collection tank 1; the first cleaning water tank 13 The water inlet end of the second cleaning water tank 14 is connected to the shared pipeline 19 through the first water inlet pipe 21, the water inlet end of the second cleaning water tank 14 is connected to the common pipeline 19 through the second water inlet pipe 22, and the water inlet end of the third cleaning water tank 15 is connected through the third water inlet pipe 23 Shared pipeline 19, the water outlet end of the first cleaning water tank 13 is connected to the water inlet end of the cleaning water pump 12 through the first water outlet pipe 33, and the water outlet end of the second cleaning water tank is connected to the water inlet end of the cleaning water pump through the second water outlet pipe 34, The water outlet end of the third cleaning water tank 15 is connected to the water inlet end of the cleaning water pump 12 through the third water outlet pipe 35, and the water outlet end of the cleaning water pump 12 is connected to the water inlet end of the tubular microfiltration membrane device 4 through the cleaning water inlet pipe 16, and, The water outlet of the cleaning water pump 12 is also connected with a liquid medicine discharge pipe 24, and the liquid medicine discharge pipe 24 is provided with a discharge switch, and the liquid discharged through the liquid medicine discharge pipe 24 can be discharged into the plate washing wastewater treatment system.
管式微滤膜装置4的浓水出水端与浓缩水箱3之间的连接管道上、浓缩水箱3的出水端与管式微滤膜装置4入水端之间的连接管道上、管式微滤膜装置4的滤水出水端与回用水箱5之间的连接管道上、清洗入水管16上、第一清洗出水管17、第二清洗出水管18、第一进水管21、第二进水管22、第二进水管23、共用管道19、第一出水管33、第二出水管34及第三出水管35均设置有开关。On the connecting pipeline between the concentrated water outlet end of the tubular microfiltration membrane device 4 and the concentrated water tank 3, on the connecting pipeline between the water outlet end of the concentrated water tank 3 and the water inlet end of the tubular microfiltration membrane device 4, on the connecting pipeline between the tubular microfiltration membrane device 4 On the connecting pipe between the filtered water outlet end and the reuse water tank 5, on the cleaning water inlet pipe 16, the first cleaning water outlet pipe 17, the second cleaning water outlet pipe 18, the first water inlet pipe 21, the second water inlet pipe 22, the first water inlet pipe 22, the The two water inlet pipes 23, the common pipe 19, the first water outlet pipe 33, the second water outlet pipe 34 and the third water outlet pipe 35 are all provided with switches.
前述铜片研磨废水处理回用系统可广泛应用于诸多领域,例如:(1)、金属电镀:主要用于去除重金属离子,经处理后离子浓度低于0.1ppm;(2)、印刷电路板:主要用于去除重金属离子,经处理后离子浓度低于0.1ppm;(3)、半导体:经处理后砷化合物浓度低于0.1ppm,经处理后氟化合物浓度低于5ppm,减少硅的流失,去离子,从铅到锡的电镀废水中回收金属等;(4)回灌地下水:主要去除重金属离子,经处理后离子浓度低于0.1ppm;(5)电池制造:去除污水中的铅与镉;(6)汽车制造:主要去除磷酸盐处理工程中含有的锌与磷酸盐;(7)工业一般用途:主要去除焚烧清洗水中的重金属物质,用于废水回用中在反渗透前的预处理,在循环水中用于软化水,整体的重金属去除率达到0.1ppm,在砂滤工艺后代替澄清池等。The aforementioned copper sheet grinding wastewater treatment and recycling system can be widely used in many fields, such as: (1), metal electroplating: mainly used to remove heavy metal ions, and the ion concentration after treatment is lower than 0.1ppm; (2), printed circuit board: It is mainly used to remove heavy metal ions, and the ion concentration after treatment is lower than 0.1ppm; (3), semiconductor: after treatment, the concentration of arsenic compounds is lower than 0.1ppm, and after treatment, the concentration of fluorine compounds is lower than 5ppm, which reduces the loss of silicon and removes ions, recovery of metals, etc. from electroplating wastewater from lead to tin; (4) recharge groundwater: mainly remove heavy metal ions, after treatment, the ion concentration is lower than 0.1ppm; (5) battery manufacturing: remove lead and cadmium in sewage; (6) Automobile manufacturing: mainly removes zinc and phosphate contained in phosphate treatment engineering; (7) General industrial use: mainly removes heavy metal substances in incineration and cleaning water, and is used for pretreatment before reverse osmosis in wastewater reuse, It is used to soften water in circulating water, and the overall heavy metal removal rate reaches 0.1ppm. It can replace clarification tank after sand filtration process.
本发明的设计重点在于,其主要是通过电控制单元、废水收集池、反应水箱、浓缩水箱、管式微滤膜装置、回用水箱、污泥浓缩装置、滤液箱及滤膜清洗系统的设计及相互配合,使得本发明之铜片研磨废水处理回用系统具有自动化程度高、操作简单、可按需控制间隙运行、可按需调节产水流量、水处理药剂添加少、过滤水质可靠、处理回用效率高、环保节能及资源回用等诸多优势,适于推广应用。The design focus of the present invention is, it is mainly through the design and the Cooperating with each other, the copper sheet grinding wastewater treatment and recycling system of the present invention has a high degree of automation, simple operation, can control the gap operation as required, can adjust the flow rate of produced water as required, adds less water treatment chemicals, and has reliable filtered water quality. It has many advantages such as high efficiency, environmental protection and energy saving, and resource reuse, and is suitable for popularization and application.
以上所述,仅是本发明的较佳实施例而已,并非对本发明的技术范围作任何限制,故凡是依据本发明的技术实质对以上实施例所作的任何细微修改、等同变化与修饰,均仍属于本发明技术方案的范围内。The above descriptions are only preferred embodiments of the present invention, and do not limit the technical scope of the present invention in any way, so any minor modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention are still valid. It belongs to the scope of the technical solutions of the present invention.
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