CN202358976U - Glass wastewater treatment equipment - Google Patents
Glass wastewater treatment equipment Download PDFInfo
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- CN202358976U CN202358976U CN201120426018XU CN201120426018U CN202358976U CN 202358976 U CN202358976 U CN 202358976U CN 201120426018X U CN201120426018X U CN 201120426018XU CN 201120426018 U CN201120426018 U CN 201120426018U CN 202358976 U CN202358976 U CN 202358976U
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- 239000011521 glass Substances 0.000 title claims abstract description 36
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 103
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 52
- 238000004062 sedimentation Methods 0.000 claims abstract description 27
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 23
- 239000010922 glass waste Substances 0.000 claims abstract description 21
- 230000001105 regulatory effect Effects 0.000 claims abstract description 15
- 238000000746 purification Methods 0.000 claims abstract description 14
- 239000010802 sludge Substances 0.000 claims description 44
- 239000007787 solid Substances 0.000 claims description 10
- 238000005273 aeration Methods 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 9
- 208000012826 adjustment disease Diseases 0.000 claims description 8
- 230000001954 sterilising effect Effects 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 8
- 239000000701 coagulant Substances 0.000 claims description 6
- 229910017053 inorganic salt Inorganic materials 0.000 claims description 6
- 229920000642 polymer Polymers 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 5
- 239000003814 drug Substances 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 abstract description 16
- 238000000034 method Methods 0.000 abstract description 5
- 230000008569 process Effects 0.000 abstract description 4
- 238000004064 recycling Methods 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 description 15
- 239000012528 membrane Substances 0.000 description 10
- 239000000084 colloidal system Substances 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 239000002585 base Substances 0.000 description 5
- 238000003912 environmental pollution Methods 0.000 description 4
- 239000004744 fabric Substances 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000003116 impacting effect Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及环保工程领域,特别涉及一种玻璃废水处理设备。 The utility model relates to the field of environmental protection engineering, in particular to glass waste water treatment equipment. the
背景技术 Background technique
随着环境污染问题和水资源短缺问题的加剧,人们越来越意识到保护环境和节约用水的重要性。在玻璃生产过程中会产生大量的废水,这些废水如果直接排放,将会造成严重的环境污染,同时也造成水资源的大量浪费,因此,对玻璃废水的净化和回收利用是企业义不容辞的责任。 With the aggravation of environmental pollution and water shortage, people are increasingly aware of the importance of protecting the environment and saving water. A large amount of waste water will be generated in the glass production process. If the waste water is discharged directly, it will cause serious environmental pollution and a large waste of water resources. Therefore, the purification and recycling of glass waste water is the bounden duty of enterprises. the
随着技术的发展,玻璃行业逐渐产生了玻璃废水处理设备,在现有玻璃废水处理设备的处理过程中,一方面,玻璃废水经调节池、反应池和沉淀池后排放,另一方面,沉淀池的污泥经污泥浓缩池和压滤机后外运。然而,在此种玻璃废水处理设备的处理过程中,由于玻璃废水中不光是含有污泥,还含有悬浮微粒、胶体、微生物等悬浮杂质,而沉淀池仅能够处理污泥这类容易下沉的杂质,对于悬浮微粒、胶体、微生物等杂质则没有效果,因此,经沉淀池后排放的废水依然会造成环境污染;再者,由于现有玻璃废水处理设备处理后的水直接排放,没有回收利用,因此造成水资源的大量浪费,没有达到环保要求节能减排的宗旨。 With the development of technology, the glass industry has gradually produced glass wastewater treatment equipment. In the treatment process of the existing glass wastewater treatment equipment, on the one hand, the glass wastewater is discharged after passing through the regulating tank, reaction tank and sedimentation tank; on the other hand, the sedimentation The sludge in the tank is transported out after going through the sludge thickening tank and filter press. However, in the treatment process of this kind of glass wastewater treatment equipment, since the glass wastewater not only contains sludge, but also contains suspended particles, colloids, microorganisms and other suspended impurities, the sedimentation tank can only deal with sludge, which is easy to sink. Impurities have no effect on suspended particles, colloids, microorganisms and other impurities. Therefore, the wastewater discharged after the sedimentation tank will still cause environmental pollution; moreover, because the water treated by the existing glass wastewater treatment equipment is directly discharged, there is no recycling. , thus causing a large amount of waste of water resources, failing to achieve the purpose of energy saving and emission reduction required by environmental protection. the
实用新型内容 Utility model content
本实用新型要解决的技术问题是针对上述现有技术中的不足,提供一种玻璃废水处理设备,该玻璃废水处理设备不但对玻璃废水净化彻底,而且在处理玻璃废水过程中的水能回调利用。 The technical problem to be solved by the utility model is to provide a kind of glass wastewater treatment equipment for the above-mentioned deficiencies in the prior art. . the
本实用新型的技术方案是:一种玻璃废水处理设备,包括玻璃废水净化系统和中水回用系统,其中: The technical solution of the utility model is: a glass wastewater treatment equipment, including a glass wastewater purification system and a reclaimed water reuse system, wherein:
玻璃废水净化系统,在该玻璃废水净化系统内,玻璃废水依次经调节池、反应池、沉淀池、中间池、过滤器、超滤装置、超滤水池、反渗透装置、反渗透水池后得到净化到达纯水箱; Glass waste water purification system, in the glass waste water purification system, the glass waste water is purified through the regulating tank, reaction tank, sedimentation tank, intermediate tank, filter, ultrafiltration device, ultrafiltration pool, reverse osmosis device, and reverse osmosis pool reach the pure water tank;
中水回用系统,在所述中间池、反渗透水池和纯水箱外分别设有中水回用的水泵。 In the reclaimed water reuse system, water pumps for reclaimed water recycle are respectively provided outside the intermediate pool, the reverse osmosis pool and the pure water tank.
所述沉淀池连接污泥处理系统,在污泥处理系统内依次设置污泥池、污泥泵和压滤机,该污泥池接收所述沉淀池池底的污泥后,经污泥泵抽取到达压滤机,在压滤机内,污泥的固体与液体分离。所述沉淀池池底具有斜斗结构,所述污泥池通过污泥管道与沉淀池的斜斗底部连通。 The sedimentation tank is connected to a sludge treatment system, and a sludge tank, a sludge pump and a filter press are arranged in sequence in the sludge treatment system. After the sludge tank receives the sludge at the bottom of the sedimentation tank, it is pumped through the sludge pump The extraction reaches a filter press where the solids of the sludge are separated from the liquid. The bottom of the sedimentation tank has an inclined bucket structure, and the sludge tank communicates with the bottom of the inclined bucket of the sedimentation tank through a sludge pipeline. the
所述压滤机外安装有对压滤机内进行水冲击的反冲泵以及对压滤机内添加药料的加药装置。 A recoil pump for impacting water in the filter press and a dosing device for adding medicinal materials to the filter press are installed outside the filter press. the
所述调节池内安装有曝气装置。 An aeration device is installed in the regulating tank. the
所述反应池外安装有向反应池内添加药料的加药装置,反应池内安装有搅拌装置。 A dosing device for adding medicinal materials to the reaction tank is installed outside the reaction tank, and a stirring device is installed in the reaction tank. the
所述反应池设置有三套,分别为酸碱调节反应池、PAC无机盐混凝剂反应池和PAM高分子絮凝剂反应池,玻璃废水依次经酸碱调节反应池、PAC无机盐混凝剂反应池和PAM高分子絮凝剂反应池后进入沉淀池。 There are three sets of reaction pools, which are acid-base adjustment reaction pool, PAC inorganic salt coagulant reaction pool and PAM polymer flocculant reaction pool. After pool and PAM polymer flocculant reaction tank, it enters the sedimentation tank. the
所述反渗透装置和反渗透水池之间设置有紫外线杀菌装置。 An ultraviolet sterilizing device is arranged between the reverse osmosis device and the reverse osmosis pool. the
所述反渗透装置和纯水箱之间设置有紫外线杀菌装置。 An ultraviolet sterilizing device is arranged between the reverse osmosis device and the pure water tank. the
所述反渗透装置设置有二套,分别为一级反渗透装置和二级反渗透装置。 The reverse osmosis device is provided with two sets, namely a primary reverse osmosis device and a secondary reverse osmosis device. the
本实用新型的有益效果是:由于本实用新型的玻璃废水净化系统内,玻璃废水依次经调节池、反应池、沉淀池、中间池、过滤器、超滤装置、超滤水池、反渗透装置、反渗透水池后得到净化到达纯水箱,因此,玻璃废水能得到彻底的净化,从纯水箱排放出去的水不会造成环境污染;由于本实用新型设置了中水回用系统,在所述中间池、反渗透水池和纯水箱外分别设有中水回用的水泵,因此,可根据生产车间不同的生产需要调取中间池、反渗透水池和纯水箱的水以作生产用,从而节约大量水资源以及生产成本费用。 The beneficial effects of the utility model are: in the glass wastewater purification system of the utility model, the glass wastewater passes through the regulating tank, the reaction tank, the sedimentation tank, the intermediate tank, the filter, the ultrafiltration device, the ultrafiltration pool, the reverse osmosis device, After the reverse osmosis pool is purified and reaches the pure water tank, the glass waste water can be thoroughly purified, and the water discharged from the pure water tank will not cause environmental pollution; since the utility model is equipped with a reclaimed water reuse system, in the The intermediate pool, reverse osmosis pool and pure water tank are respectively equipped with reclaimed water reuse pumps. Therefore, the water in the intermediate pool, reverse osmosis pool and pure water tank can be used for production according to the different production needs of the production workshop. Thereby saving a lot of water resources and production costs. the
附图说明 Description of drawings
图1为本实用新型的整体结构示意图。 Figure 1 is a schematic diagram of the overall structure of the utility model. the
图中:1.调节池;2.反应池;3.沉淀池;4.中间池;5.过滤器;6.超滤装置;7.超滤水池;8.反渗透装置;9.反渗透水池;10.纯水箱;11.水泵;12.水泵;13.水泵;14.污泥池;15.污泥泵;16.压滤机;17.曝气装置;18.加药装置;19.搅拌装置;20.酸碱调节反应池;21.PAC无机盐混凝剂反应池;22.PAM高分子絮凝剂反应池;23.PH值测试棒;24.斜斗;25.紫外线杀菌装置;26.紫外线杀菌装置;27.反冲泵;28.加药装置;A.玻璃废水;B.污泥;C.厂区自来水;D.厂区压缩空气;E.过滤泥饼;F.滤液。 In the figure: 1. Regulating tank; 2. Reaction tank; 3. Sedimentation tank; 4. Intermediate tank; 5. Filter; 6. Ultrafiltration device; 7. Ultrafiltration pool; 8. Reverse osmosis device; 9. Reverse osmosis Pool; 10. Pure water tank; 11. Water pump; 12. Water pump; 13. Water pump; 14. Sludge tank; 15. Sludge pump; 16. Filter press; 17. Aeration device; 18. Dosing device; 19. Stirring device; 20. Acid-base adjustment reaction tank; 21. PAC inorganic salt coagulant reaction tank; 22. PAM polymer flocculant reaction tank; 23. PH value test stick; 24. Inclined bucket; 25. Ultraviolet sterilization Device; 26. Ultraviolet sterilizing device; 27. Recoil pump; 28. Dosing device; A. Glass waste water; B. Sludge; C. Tap water in the factory area; D. Compressed air in the factory area; E. Filter mud cake; F. Filtrate . the
具体实施方式 Detailed ways
下面结合附图对本实用新型的结构原理和工作原理作进一步详细说明。 Below in conjunction with accompanying drawing, structural principle and working principle of the present utility model are described in further detail. the
如图1所示,本实用新型为一种玻璃废水处理设备,包括玻璃废水净化系统、中水回用系统和污泥处理系统,其中: As shown in Figure 1, the utility model is a glass wastewater treatment equipment, including a glass wastewater purification system, a reclaimed water reuse system and a sludge treatment system, wherein:
玻璃废水净化系统,在所述玻璃废水净化系统内,玻璃废水A依次经调节池1、反应池2、沉淀池3、中间池4、过滤器5、超滤装置6、超滤水池7、反渗透装置8、反渗透水池9后得到净化到达纯水箱10。 Glass waste water purification system, in the glass waste water purification system, the glass waste water A passes through the regulating pool 1, the reaction pool 2, the sedimentation pool 3, the intermediate pool 4, the filter 5, the ultrafiltration device 6, the ultrafiltration water pool 7, the reverse After the osmosis device 8 and the reverse osmosis pool 9 are purified, they reach the pure water tank 10 .
中水回用系统,在所述中间池4、反渗透水池8和纯水箱10外分别设有中水回用的水泵(11、12、13); The reclaimed water reuse system is provided with reclaimed water reuse pumps (11, 12, 13) outside the intermediate pool 4, the reverse osmosis pool 8 and the pure water tank 10;
污泥处理系统,该污泥处理系统依次设置污泥池14、污泥泵15和压滤机16,该污泥池14接收所述沉淀池3池底的污泥后,经污泥泵15抽取到达压滤机16,在压滤机16内,污泥的固体与液体分离。 A sludge treatment system, the sludge treatment system is provided with a sludge tank 14, a sludge pump 15 and a filter press 16 in sequence. The extraction reaches a filter press 16 where the solids of the sludge are separated from the liquid.
上述各部分的工作流程是: The workflow of the above parts is:
1.调节池1:调节池1将玻璃废水A调节收集均质,调节池1内安装曝气装置17,防止玻璃粉聚集结块,曝气装置17可设计成曝气管道伸入调节池1底部的结构,通过厂区压缩空气D向曝气管道内输入压缩气体实现曝气。 1. Regulating pool 1: Regulating pool 1 regulates and collects glass wastewater A to make it homogeneous. Aeration device 17 is installed in regulating pool 1 to prevent glass powder from gathering and agglomerating. Aeration device 17 can be designed as an aeration pipe extending into regulating pool 1 The structure at the bottom is aerated by inputting compressed air into the aeration pipeline through the compressed air D of the factory area.
2.反应池2:反应池2外安装有向反应池2内添加药料的加药装置18,反应池2内安装有搅拌装置19。加药装置18将厂区自来水C与药料混合之后送入到反应池2内,搅拌装置19再将药料与玻璃废水A搅拌混合均匀并产生反应。进一步,加药装置18内安装曝气装置(与调节池内的曝气装置结构相同),以利于加药装置18内的药料与厂区自来水C混合,而搅拌装置19可设计成由减速机带动搅拌杆旋转的结构。 2. Reaction tank 2: A dosing device 18 for adding medicine to the reaction tank 2 is installed outside the reaction tank 2, and a stirring device 19 is installed inside the reaction tank 2. The dosing device 18 mixes the tap water C in the factory area with the medicinal materials and sends them into the reaction tank 2, and the stirring device 19 stirs and mixes the medicinal materials and the glass waste water A evenly to generate a reaction. Further, an aeration device is installed in the dosing device 18 (the same structure as the aeration device in the regulating tank), so as to facilitate the mixing of the medicinal materials in the dosing device 18 with the tap water C in the factory area, and the stirring device 19 can be designed to be driven by a reducer A structure in which the stirring rod rotates. the
作为对反应池2的优选方式,反应池2设置有三套,分别为酸碱调节反应池20、PAC无机盐混凝剂反应池21和PAM高分子絮凝剂反应池22,玻璃废水A依次经酸碱调节反应池20、PAC无机盐混凝剂反应池21和PAM高分子絮凝剂反应池22后进入沉淀池4。为了实时查看酸碱调节反应池20的酸碱度,可在酸碱调节反应池20中安装PH值测试棒23。利用PAC、PAM的絮凝功能,将水中的有机悬浊物与泥液混合成为污泥并沉淀下来,从而达到去除的目的,并通过砂子的过滤效果去除出水中较细小的固体颗粒和其它悬浮在水中的微小杂质,从而使其对进水的过滤净化功能大大增强,提高了出水的水质状况。 As a preferred mode of the reaction pool 2, the reaction pool 2 is provided with three sets, which are the acid-base adjustment reaction pool 20, the PAC inorganic salt coagulant reaction pool 21 and the PAM polymer flocculant reaction pool 22, and the glass wastewater A is passed through the acid Alkali adjustment reaction tank 20, PAC inorganic salt coagulant reaction tank 21 and PAM macromolecule flocculant reaction tank 22 enter the sedimentation tank 4. In order to check the pH of the acid-base adjustment reaction tank 20 in real time, a pH value test stick 23 can be installed in the acid-base adjustment reaction tank 20 . Using the flocculation function of PAC and PAM, the organic suspended matter in the water is mixed with the mud liquid to form sludge and precipitated, so as to achieve the purpose of removal, and the finer solid particles and other suspended in the water are removed through the filtering effect of sand. The small impurities in the water greatly enhance the filtration and purification function of the influent water and improve the water quality of the effluent. the
3.沉淀池3:沉淀池3为物质沉淀提供场所,在沉淀池3中物质有足够的沉淀时间,使得固体颗粒物质和部分悬浮物能够沉淀下来。沉淀池3池底具有斜斗24结构,使得污泥在斜斗24底部得到富集。 3. Sedimentation tank 3: Sedimentation tank 3 provides a place for material sedimentation, and the material in the sedimentation tank 3 has sufficient settling time, so that solid particulate matter and part of suspended matter can settle down. The bottom of the sedimentation tank 3 has an inclined bucket 24 structure, so that the sludge is enriched at the bottom of the inclined bucket 24 . the
4.中间池4:中间池4是沉淀池3出水储存和放置的场所,中间池4内储存的一部分水通过水泵11直接送达到玻璃生产车间,可供生产车间的玻璃磨边机(图中未示出)使用。 4. Intermediate pool 4: The intermediate pool 4 is the place where the effluent of the sedimentation tank 3 is stored and placed. A part of the water stored in the intermediate pool 4 is directly sent to the glass production workshop through the water pump 11, which can be used for the glass edger in the production workshop (in the figure not shown) use. the
5.过滤器5:中间池4的水经过滤器5后可过滤掉部分杂质。 5. Filter 5: After the water in the middle pool 4 passes through the filter 5, some impurities can be filtered out. the
6.超滤装置6:超滤装置6的超滤膜系统可用于去除水中的悬浮微粒、胶体、微生物等。在水压的作用下水分子及小分子物质透过超滤膜,而水中的悬浮微粒、胶体、微生物等则被截留在超滤膜的内表面。由于超滤膜上的微孔很小,可以有效地去除各种水中悬浮颗粒、胶体、细菌和大分子有机物等,这些截留物质可能会在膜的内表面集聚,所以需要对超滤膜组件进行定期的反冲洗和加药清洗。 6. Ultrafiltration device 6: The ultrafiltration membrane system of the ultrafiltration device 6 can be used to remove suspended particles, colloids, microorganisms, etc. in water. Under the action of water pressure, water molecules and small molecular substances pass through the ultrafiltration membrane, while suspended particles, colloids, microorganisms, etc. in the water are trapped on the inner surface of the ultrafiltration membrane. Since the micropores on the ultrafiltration membrane are very small, it can effectively remove various suspended particles, colloids, bacteria and macromolecular organic substances in water. These intercepted substances may accumulate on the inner surface of the membrane, so it is necessary to carry out ultrafiltration membrane components Regular backwash and dosing cleaning. the
7.超滤水池7:超滤水池7是超滤装置6超滤出水储存和放置的场所。 7. Ultrafiltration pool 7: The ultrafiltration pool 7 is the place where the ultrafiltration water from the ultrafiltration device 6 is stored and placed. the
8.反渗透装置8:反渗透装置利用高压泵的加压,膜技术分子的截留,可将溶液中水与溶质分离,并将浓缩液排放。 8. Reverse osmosis device 8: The reverse osmosis device uses the pressurization of the high-pressure pump and the interception of membrane technology molecules to separate the water and solute in the solution and discharge the concentrated solution. the
反渗透过程是利用半透性螺旋卷式膜分离去除水中的可溶性固体、有机物、胶体物质及细菌。原水以一定的压力被送至并通过逆渗透膜,水透过膜上的微小孔,收集后得到纯水。水中的杂质在载流液中浓缩并被去除。反渗透装置可除去进水中95%以上的溶解性固体,99%以上的有机物及胶体,几乎100%的细菌。反渗透装置是目前世界上水处理设备中制取纯水的最先进的设备之一,其运行费用低、经济、操作方便、运行可靠,是商家首选的制取纯水的设备。反渗透装置的生产能力是在原水在25℃、标准生产状况下的值。水温及生产条件的改变都将影响设备的生产能力。 The reverse osmosis process uses a semi-permeable spiral-wound membrane to separate and remove soluble solids, organic matter, colloidal substances and bacteria in water. Raw water is sent to and passes through the reverse osmosis membrane at a certain pressure, and the water passes through the tiny holes on the membrane, and pure water is obtained after collection. Impurities in the water are concentrated and removed in the carrier fluid. The reverse osmosis device can remove more than 95% of dissolved solids, more than 99% of organic matter and colloids, and almost 100% of bacteria in the influent. The reverse osmosis device is currently one of the most advanced equipment for producing pure water in the world's water treatment equipment. It is low in operating costs, economical, easy to operate, and reliable in operation. It is the preferred equipment for producing pure water by merchants. The production capacity of the reverse osmosis device is the value under the raw water at 25°C and standard production conditions. Changes in water temperature and production conditions will affect the production capacity of the equipment. the
9.反渗透水池9:反渗透水池9是反渗透装置8反渗透出水储存和放置的场所。反渗透水池9内储存的一部分水通过水泵12直接送达到玻璃生产车间,可供生产车间的清洗机(图中未示出)使用。 9. Reverse osmosis pool 9: The reverse osmosis pool 9 is the place where the reverse osmosis effluent from the reverse osmosis device 8 is stored and placed. A part of the water stored in the reverse osmosis pool 9 is directly sent to the glass production workshop through the water pump 12, and can be used by the cleaning machine (not shown in the figure) in the production workshop. the
10.纯水箱10:纯水箱10最玻璃废水A得到净化之后的储存之所,纯水箱10内储存的一部分水通过水泵13直接送达到玻璃生产车间,可供生产车间的包装清洗机(图中未示出)使用。 10. Pure water tank 10: The pure water tank 10 is the place where the purified glass wastewater A is stored. A part of the water stored in the pure water tank 10 is directly sent to the glass production workshop through the water pump 13, and can be used for the packaging cleaning machine in the production workshop (not shown) use. the
作为对反渗透装置8、反渗透水池9和纯水箱10之间的进一步优选,所述反渗透装置8设置二套,分别为一级反渗透装置和二级反渗透装置。玻璃废水A进入一级反渗透装置后,经反渗透水池9、二级反渗透装置后进入纯水箱10。再进一步,所述反渗透装置和反渗透水池之间设置有紫外线杀菌装置;所述反渗透装置和纯水箱之间设置有紫外线杀菌装置。 As a further preference between the reverse osmosis device 8 , the reverse osmosis pool 9 and the pure water tank 10 , two sets of the reverse osmosis device 8 are provided, namely a primary reverse osmosis device and a secondary reverse osmosis device. After the glass wastewater A enters the primary reverse osmosis device, it enters the pure water tank 10 after passing through the reverse osmosis pool 9 and the secondary reverse osmosis device. Still further, an ultraviolet sterilizing device is arranged between the reverse osmosis device and the reverse osmosis pool; an ultraviolet sterilizing device is arranged between the reverse osmosis device and the pure water tank. the
11.污泥池14:污泥池14通过污泥管道与沉淀池3的斜斗24底部连通。 11. Sludge tank 14: The sludge tank 14 communicates with the bottom of the inclined bucket 24 of the sedimentation tank 3 through a sludge pipeline. the
12.污泥泵15:污泥泵15将污泥池14中的污泥送达压滤机16。 12. Sludge pump 15: The sludge pump 15 sends the sludge in the sludge pool 14 to the filter press 16. the
13.压滤机16:压滤机16用于固体和液体的分离。污泥流经过滤介质(如滤布),固体停留在滤布上,并逐渐在滤布上堆积形成过滤泥饼E,而滤液F部分则渗透过滤布,成为不含固体的滤液F。过滤泥饼E运走即可,滤液F则重新送回调节池1。 13. Filter press 16: The filter press 16 is used for the separation of solids and liquids. The sludge flows through the filter medium (such as filter cloth), and the solid stays on the filter cloth, and gradually accumulates on the filter cloth to form a filter cake E, while the filtrate F part penetrates the filter cloth and becomes the filtrate F without solids. The filter mud cake E can be transported away, and the filtrate F is sent back to the regulating tank 1 again. the
压滤机16外安装有对压滤机16内进行水冲击的反冲泵27以及对压滤机16内添加药料的加药装置28。这样,使压滤机16在工作一段时间之后能得到及时清洗,并重新运行。反冲泵27可从中间池内抽水对压滤机16内冲击,加药装置28的结构与反应池2的加药装置结构相同。 The filter press 16 is equipped with a recoil pump 27 for impacting water in the filter press 16 and a dosing device 28 for adding medicinal materials in the filter press 16 . In this way, filter press 16 can be cleaned in time after working for a period of time, and run again. The recoil pump 27 can pump water from the intermediate tank to impact the filter press 16, and the structure of the dosing device 28 is the same as that of the reaction tank 2. the
以上所述,仅是本实用新型较佳实施方式,凡是依据本实用新型的技术方案对以上的实施方式所作的任何细微修改、等同变化与修饰,均属于本实用新型技术方案的范围内。 The above is only a preferred embodiment of the utility model, and any minor modifications, equivalent changes and modifications made to the above embodiments according to the technical solution of the utility model all belong to the scope of the technical solution of the utility model. the
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| CN102992519A (en) * | 2012-11-27 | 2013-03-27 | 常州大学 | Industrial sewage treatment device |
| CN103739110A (en) * | 2013-11-15 | 2014-04-23 | 安徽省绿巨人环境技术有限公司 | Glassware processing wastewater treatment technology |
| CN105621763A (en) * | 2014-11-26 | 2016-06-01 | 成都锦汇科技有限公司 | System for recovering acid and alkali from glass production sewage |
| CN105621773A (en) * | 2014-11-26 | 2016-06-01 | 成都锦汇科技有限公司 | System for recovering acid and alkali from glass production sewage |
| CN105692988A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | System for recovering acid and base from glass production wastewater |
| CN105692980A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | Recovery system for recovering acid and base from glass production wastewater |
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| CN105712528A (en) * | 2016-01-26 | 2016-06-29 | 中建材(合肥)新能源有限公司 | Photovoltaic glass deep processing cooling water recycling method |
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| CN103739110A (en) * | 2013-11-15 | 2014-04-23 | 安徽省绿巨人环境技术有限公司 | Glassware processing wastewater treatment technology |
| CN105899466A (en) * | 2013-12-02 | 2016-08-24 | 拉普兰塔理工大学 | Wastewater purification system |
| CN105621763A (en) * | 2014-11-26 | 2016-06-01 | 成都锦汇科技有限公司 | System for recovering acid and alkali from glass production sewage |
| CN105621773A (en) * | 2014-11-26 | 2016-06-01 | 成都锦汇科技有限公司 | System for recovering acid and alkali from glass production sewage |
| CN105692988A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | System for recovering acid and base from glass production wastewater |
| CN105692980A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | Recovery system for recovering acid and base from glass production wastewater |
| CN105692987A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | Recovery system for recovering acid and base from glass production wastewater |
| CN105712528A (en) * | 2016-01-26 | 2016-06-29 | 中建材(合肥)新能源有限公司 | Photovoltaic glass deep processing cooling water recycling method |
| CN105712532A (en) * | 2016-02-02 | 2016-06-29 | 湖南景翌湘台环保高新技术开发有限公司 | Window glass processing wastewater treatment and reuse technology |
| CN107473471A (en) * | 2017-09-18 | 2017-12-15 | 成都恒力达科技有限公司 | A kind of sewage purifying and treating device |
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| CN109956601B (en) * | 2019-04-25 | 2023-11-07 | 浙江嘉福玻璃有限公司 | Coated glass production wastewater recovery process and recovery device |
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