CN204897574U - Oily waste water contact filtration combination formula advanced treatment unit that flocculates a little - Google Patents
Oily waste water contact filtration combination formula advanced treatment unit that flocculates a little Download PDFInfo
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- CN204897574U CN204897574U CN201520515800.7U CN201520515800U CN204897574U CN 204897574 U CN204897574 U CN 204897574U CN 201520515800 U CN201520515800 U CN 201520515800U CN 204897574 U CN204897574 U CN 204897574U
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- 238000011282 treatment Methods 0.000 title claims abstract description 39
- 239000002351 wastewater Substances 0.000 title claims abstract description 35
- 238000001914 filtration Methods 0.000 title claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 124
- 239000004519 grease Substances 0.000 claims abstract description 18
- 238000005189 flocculation Methods 0.000 claims abstract description 17
- 238000011001 backwashing Methods 0.000 claims abstract description 10
- 239000000463 material Substances 0.000 claims description 11
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- 238000001179 sorption measurement Methods 0.000 description 9
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- 238000005516 engineering process Methods 0.000 description 4
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- 238000000926 separation method Methods 0.000 description 4
- 238000004065 wastewater treatment Methods 0.000 description 4
- 229920002873 Polyethylenimine Polymers 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
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- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Water Treatment By Sorption (AREA)
Abstract
本实用新型公开了一种操作简单、投资省、运行可靠、合理有效的含油废水微絮凝接触过滤组合式深度处理装置。它包括隔油池出水渠、集水池、进水泵、过滤器,隔油池出水渠一侧设有第一进水管,隔油池出水渠内设有潜污泵,潜污泵通过第一出水管与集水池的一侧相接,集水池的另一侧通过第二进水管与进水泵相连;它还包括反冲洗水泵,所述过滤器还分别连接清水池和空气压缩机,所述过滤器下部设有第三出水管,第三出水管末端通入清水池;反冲洗水泵的一端连接第四出水管、反冲洗进水管、第二连接管,并与过滤器的底部相通,反冲洗水泵的另一端通过第四进水管与清水池相接。本装置简单,运行投资费用低,操作管理方便。
The utility model discloses a micro-flocculation contact filtration combined advanced treatment device for oily waste water with simple operation, low investment, reliable operation, reasonable and effective. It includes the outlet channel of the grease trap, the sump, the water inlet pump, and the filter. There is a first water inlet pipe on one side of the outlet channel of the grease trap, and a submersible pump is installed in the outlet channel of the grease trap. The water pipe is connected to one side of the water collection tank, and the other side of the water collection tank is connected to the water inlet pump through the second water inlet pipe; it also includes a backwash water pump, and the filter is also connected to the clear water tank and the air compressor respectively. The lower part of the device is provided with a third water outlet pipe, and the end of the third water outlet pipe leads into the clear water tank; one end of the backwash water pump is connected to the fourth water outlet pipe, the backwash water inlet pipe, and the second connecting pipe, and communicates with the bottom of the filter for backwashing. The other end of the water pump is connected with the clear water pool through the fourth water inlet pipe. The device is simple, low in operation investment cost, and convenient in operation and management.
Description
技术领域 technical field
本实用新型属于废水处理领域,特别是涉及一种含油废水微絮凝接触过滤组合式深度处理装置。 The utility model belongs to the field of wastewater treatment, in particular to a micro-flocculation contact filtration combined advanced treatment device for oily wastewater.
背景技术 Background technique
含油废水是一种常见的量大面广的工业废水,石油的开采及加工运输、机电及机械加工、石油化工等行业每天排出大量的含油废水,严重危害着水环境的安全,而经隔油池处理后,油的含量、COD、悬浮物和其他指标仍较高,不能满足回用的要求而被排出,既污染了环境,又造成了水资源的浪费。 Oily wastewater is a common industrial wastewater with a large volume and wide range. Petroleum mining, processing and transportation, electromechanical and mechanical processing, petrochemical and other industries discharge a large amount of oily wastewater every day, which seriously endangers the safety of the water environment. After the pool is treated, the oil content, COD, suspended matter and other indicators are still high, which cannot meet the requirements of reuse and are discharged, which not only pollutes the environment, but also causes a waste of water resources.
含油废水中浮油、固体附着油的粒径较大,易从废水中分离,经隔油池(或沉淀池)处理后可基本被除去;分散油和乳化油分散度和稳定性较高,常用的隔油、气浮等工艺很难将它们去除,因而还需深度处理;溶解态油一般含量较低,但不易被去除,须将其先转化为不溶物后再行处理。 The particle size of slick oil and solid attached oil in oily wastewater is relatively large, so it is easy to separate from wastewater and can be basically removed after treatment in a grease trap (or sedimentation tank); dispersed oil and emulsified oil have high dispersion and stability, Commonly used techniques such as oil separation and air flotation are difficult to remove them, so advanced treatment is required; the content of dissolved oil is generally low, but it is not easy to be removed, and it must be converted into insoluble matter before treatment.
在含油废水的初级处理中是把浮油与水分离,再采用二级处理技术或后处理技术改变并分离乳化油。乳化油的处理比较复杂,经初级重力分离后需进行二级处理或后处理,常用的处理方法有化学破乳法、气浮法、电解法、生物处理技术、膜分离法、粗粒化法、过滤法、吸附法。 In the primary treatment of oily wastewater, floating oil is separated from water, and then the emulsified oil is changed and separated by secondary treatment technology or post-treatment technology. The treatment of emulsified oil is relatively complicated. After primary gravity separation, secondary treatment or post-treatment is required. Commonly used treatment methods include chemical demulsification, air flotation, electrolysis, biological treatment technology, membrane separation, and coarse graining. , filtration, adsorption.
目前,含油废水的处理一般采用“老三套”的设备场池处理,即隔油池,然后气浮(沉淀)池,再到生化曝气池,其中所用的药剂几乎全是聚合氯化铝,由于该药剂水解形成的絮体结构松散,浮渣量大而密度小,含水率高,沉降性和脱水性均差,往往给后续的污泥处理带来很大的困难,并且不可避免地造成二次污染。由于在含油废水中常含有缓蚀剂、杀菌剂等,所以使该流程中的生化单元处理的效果并不好。含油废水中的乳化油在表面活性剂的作用下,十分稳定,不易被破坏,很难处理。传统的处理方法之一是在含乳化油的废水中加入表面活性较高但分子链较短或分子有支链的另一种表面活性剂来破乳,但表面活性剂的加入又会引起新的污染。另一种传统方法是在高压静电场的作用下使油珠向电极运动并放电,在电极处凝并而达到分离,但该法不适宜于大规模应用。 At present, the treatment of oily wastewater generally adopts the "old three sets" of equipment and field ponds, that is, grease traps, then air flotation (sedimentation) ponds, and then to biochemical aeration ponds. The chemicals used are almost all polyaluminum chloride , because the floc structure formed by the hydrolysis of the agent is loose, the amount of scum is large and the density is small, the water content is high, and the sedimentation and dehydration are poor, which often brings great difficulties to the subsequent sludge treatment, and inevitably cause secondary pollution. Because oily wastewater often contains corrosion inhibitors, bactericides, etc., the effect of the biochemical unit treatment in this process is not good. Under the action of surfactant, the emulsified oil in oily wastewater is very stable, not easy to be destroyed, and difficult to handle. One of the traditional treatment methods is to add another surfactant with high surface activity but short molecular chain or branched chain to the wastewater containing emulsified oil to break the emulsion, but the addition of surfactant will cause new pollution. Another traditional method is to make the oil droplets move to the electrode and discharge under the action of a high-voltage electrostatic field, and then condense at the electrode to achieve separation, but this method is not suitable for large-scale applications.
实用新型内容 Utility model content
本实用新型的目的是提供一种操作简单、投资省、运行可靠、合理有效的含油废水微絮凝接触过滤组合式深度处理装置。 The purpose of the utility model is to provide a micro-flocculation contact filtration combined advanced treatment device for oily wastewater with simple operation, low investment, reliable operation, reasonable and effective.
为解决上述问题,本实用新型技术方案如下:一种含油废水微絮凝接触过滤组合式深度处理装置,包括隔油池出水渠、集水池、进水泵、过滤器,隔油池出水渠一侧设有第一进水管,隔油池出水渠内设有潜污泵,潜污泵通过第一出水管与集水池的一侧相接,集水池的另一侧通过第二进水管与进水泵相连;它还包括反冲洗水泵,所述过滤器还分别连接清水池和空气压缩机,所述过滤器下部设有第三出水管,第三出水管末端通入清水池;反冲洗水泵(43)的一端连接第四出水管、反冲洗进水管、第二连接管,并与过滤器的底部相通,反冲洗水泵的另一端通过第四进水管与清水池相接;空气压缩机通过压缩空气管与过滤器底部相连。 In order to solve the above problems, the technical solution of the utility model is as follows: a micro-flocculation contact filtration combined advanced treatment device for oily wastewater, including a grease trap outlet channel, a sump, an inlet pump, a filter, and a grease trap outlet channel on one side. There is a first water inlet pipe, and a submersible sewage pump is installed in the outlet channel of the grease trap. The submersible sewage pump is connected to one side of the sump through the first outlet pipe, and the other side of the sump is connected to the water inlet pump through the second water inlet pipe. It also includes a backwashing water pump, the filter is also connected to the clear water tank and the air compressor, the lower part of the filter is provided with a third water outlet pipe, and the end of the third water outlet pipe leads into the clear water pool; the backwash water pump (43) One end of the backwashing water pump is connected to the fourth water outlet pipe, the backwashing water inlet pipe, and the second connecting pipe, and communicates with the bottom of the filter. The other end of the backwashing water pump is connected to the clear water pool through the fourth water inlet pipe; Attaches to the bottom of the filter.
针对含油废水水量大,难降解,污染性强等特性,需研究开发一种新型高效的含油废水处理方法,作为隔油池或混合沉淀池之后的单元操作,从而提高含油废水处理的水平和效果,以达到深度处理及回用的目的。本装置主要针对含油废水中的分散油和乳化油,基于微絮凝过滤和接触过滤对含油废水深度处理的良好效果,创造性地将二者相结合,一方面适度增大了污染物分散相的尺度,有利于污染物被滤床截留;另一方面可有效降低了滤料表面的电性,有利于滤料对污染物的吸附及滤床深层滤料吸附容量的充分利用,充分发挥了两者的各自优势。可有效破乳絮凝和吸附共沉淀去除乳化油和分散油,且絮凝剂对水体无毒害作用。 In view of the large amount of oily wastewater, difficult to degrade, and strong pollution, it is necessary to research and develop a new and efficient oily wastewater treatment method, which can be used as a unit operation after the grease trap or mixed sedimentation tank, so as to improve the level and effect of oily wastewater treatment , in order to achieve the purpose of in-depth treatment and reuse. This device is mainly aimed at the dispersed oil and emulsified oil in oily wastewater. Based on the good effect of micro-flocculation filtration and contact filtration on the advanced treatment of oily wastewater, the two are creatively combined. On the one hand, the scale of the dispersed phase of pollutants is moderately increased. , which is conducive to the pollutants being intercepted by the filter bed; on the other hand, it can effectively reduce the electrical properties of the filter material surface, which is conducive to the adsorption of pollutants by the filter material and the full use of the adsorption capacity of the filter material in the deep layer of the filter bed, giving full play to both their respective advantages. It can effectively demulsify flocculation and adsorption co-precipitation to remove emulsified oil and dispersed oil, and the flocculant has no toxic effect on water body.
本实用新型采用Zeta电位较低的均质陶粒砂滤料,运行稳定周期长,产水量高,工作吸附容量大,有效地提高了含油废水接触过滤深度处理的效果。 The utility model adopts the homogeneous ceramsite sand filter material with low Zeta potential, which has long stable operation period, high water yield and large working adsorption capacity, and effectively improves the effect of advanced treatment of oily wastewater contact filtration.
本实用新型采用气水联合反冲-水反冲先进性和可靠性技术,并辅以长柄滤头,可使滤床不分层,冲洗均匀,不宜积泥球,滤料损失率低,洗耗水率小,节省气量,操作简单,导致滤床完全再生,恢复其吸附容量。 The utility model adopts the advanced and reliable technology of air-water combined recoil-water recoil, and is supplemented with a long handle filter head, which can make the filter bed not stratified, flush evenly, not suitable for mud balls, and the loss rate of filter material is low. The washing water consumption rate is small, the air volume is saved, and the operation is simple, resulting in complete regeneration of the filter bed and restoring its adsorption capacity.
本实用新型集水池无搅拌混合装置,所发生的微絮凝是由布朗运动引起的是异向絮凝,即省去动力消耗,加上所用絮凝剂配方成本低廉,导致本工艺的水处理成本为0.58元/吨,远低于现行工业用水价格。 The water collecting tank of the utility model has no stirring and mixing device, and the micro-flocculation that occurs is anisotropic flocculation caused by Brownian motion, which saves power consumption, and the cost of the flocculant formula used is low, resulting in a water treatment cost of 0.58 in this process. Yuan/ton, far lower than the current price of industrial water.
综上,本实用新型的含油废水微絮凝接触过滤组合式深度处理装置简单,运行投资费用低,操作管理方便,出水水质达到国家一级排放标准,出水残余油浓度达12mg/L以下,COD去除率达49%以上,浊度去除率达93%以上,明显提高含油废水处理的水平和效果,达到深度处理及回用的目的。 In summary, the oily wastewater micro-flocculation contact filtration combined advanced treatment device of the utility model is simple, with low operating investment costs, convenient operation and management, effluent water quality meets the national first-class discharge standard, effluent residual oil concentration is below 12mg/L, and COD is removed The removal rate of turbidity is over 49%, and the removal rate of turbidity is over 93%, which significantly improves the level and effect of oily wastewater treatment, and achieves the purpose of advanced treatment and reuse.
附图说明 Description of drawings
图1为含油废水微絮凝接触过滤组合式深度处理装置的结构示意图。 Fig. 1 is a schematic structural diagram of a micro-flocculation contact filtration combined advanced treatment device for oily wastewater.
附图标记含义如下:1—隔油池出水渠;2—集水池;3—过滤器;4—清水池;5—空气压缩机;6—第一进水管;7—潜污泵;8—第一出水管;9—第一止回阀;10—第一阀门;11—第二阀门;12—第一放空管;13—第三阀门;14—第二进水管;15—进水泵;16—第二出水管;17—第五阀门;18—进水流量计;19—第六阀门;20—回流管;21—加药管;22—加药流量计;23—第四阀门;24—配药箱;25—第三进水管;26—第七阀门;27—第一压力表;28—第一连接管;29—第二连接管;30—第二压力表;31—第八阀门;32—第三出水管;33—反冲洗进水管;34—第十阀门;35—第十一阀门;36—排水管;37—冲洗流量计;38—第十二阀门;39—排气管;40—第九阀门;41—第四进水管;42—第十四阀门;43—反冲洗水泵;44—第十五阀门;45—第四出水管;46—冲洗流量计;47—溢流管;48—第二放空管;49—第十三阀门;50—压缩空气管;51—空气流量计;52—第三压力表;53—第二止回阀;54—第十六阀门。 The meanings of the reference signs are as follows: 1—the outlet channel of the grease trap; 2—the sump; 3—the filter; 4—the clear water pool; The first outlet pipe; 9—the first check valve; 10—the first valve; 11—the second valve; 12—the first vent pipe; 13—the third valve; 14—the second water inlet pipe; 15—the water inlet pump ; 16—the second outlet pipe; 17—the fifth valve; 18—the water inlet flowmeter; 19—the sixth valve; 20—the return pipe; 21—the dosing pipe; 22—the dosing flow meter; ; 24—dispensing box; 25—the third water inlet pipe; 26—the seventh valve; Eight valves; 32—third outlet pipe; 33—backwashing water inlet pipe; 34—tenth valve; 35—eleventh valve; 36—drainage pipe; 37—flush flow meter; 38—twelfth valve; Exhaust pipe; 40—ninth valve; 41—fourth water inlet pipe; 42—fourteenth valve; 43—backwash water pump; 44—fifteenth valve; 45—fourth outlet pipe; 46—flush flow meter; 47—overflow pipe; 48—second vent pipe; 49—thirteenth valve; 50—compressed air pipe; 51—air flow meter; 52—third pressure gauge; 53—second check valve; 54— Sixteenth valve.
具体实施方式 Detailed ways
下面结合附图对本实用新型作进一步详细的说明。 Below in conjunction with accompanying drawing, the utility model is described in further detail.
如图所示,一种含油废水微絮凝接触过滤组合式深度处理装置,包括隔油池出水渠1、集水池2、进水泵15、过滤器3,隔油池出水渠1一侧设有第一进水管6,隔油池出水渠1内设有潜污泵7,潜污泵7通过第一出水管8与集水池2的一侧相接,集水池2的另一侧通过第二进水管14与进水泵15相连;其特征在于:它还包括反冲洗水泵43,过滤器3还分别连接清水池4和空气压缩机5,进水泵15连接的出口端连接第二出水管16、第三进水管25、第一连接管28,且与过滤器3顶部相通;过滤器3下部设有第三出水管32,第三出水管32末端通入清水池4;反冲洗水泵43的一端连接第四出水管45、反冲洗进水管33、第二连接管29,并与过滤器3的底部相通,反冲洗水泵43的另一端通过第四进水管41与清水池4相接;空气压缩机5通过压缩空气管50与过滤器3底部相连。 As shown in the figure, a micro-flocculation contact filtration combined advanced treatment device for oily wastewater includes a grease trap outlet channel 1, a sump 2, an inlet pump 15, and a filter 3, and a first oil trap outlet channel is installed on one side of the grease trap outlet channel 1. A water inlet pipe 6 and a submersible sewage pump 7 are arranged in the outlet channel 1 of the grease trap. The water pipe 14 is connected with the water inlet pump 15; it is characterized in that: it also includes a backwash water pump 43, and the filter 3 is also connected with the clear water tank 4 and the air compressor 5 respectively, and the outlet end connected to the water inlet pump 15 is connected with the second water outlet pipe 16, the second Three inlet pipes 25, the first connecting pipe 28, and communicate with the top of the filter 3; the bottom of the filter 3 is provided with a third outlet pipe 32, and the end of the third outlet pipe 32 leads into the clear water pool 4; one end of the backwash water pump 43 is connected The fourth water outlet pipe 45, the backwash water inlet pipe 33, the second connecting pipe 29, and communicate with the bottom of the filter 3, the other end of the backwash water pump 43 is connected with the clear water pool 4 through the fourth water inlet pipe 41; the air compressor 5 is connected to the bottom of filter 3 through compressed air pipe 50.
第一出水管8上设有第一止回阀9与第一阀门10。集水池2底部设有第一放空管12,第一放空管12上设有第二阀门11。 The first water outlet pipe 8 is provided with a first check valve 9 and a first valve 10 . A first venting pipe 12 is provided at the bottom of the sump 2 , and a second valve 11 is provided on the first venting pipe 12 .
第二进水管14通过加药管21与配药箱24相连,第二进水管14上设有第三阀门13;加药管21上设有流量计22和第四阀门23。 The second water inlet pipe 14 is connected with the dispensing box 24 through the medicine feeding pipe 21 , the second water inlet pipe 14 is provided with a third valve 13 ; the medicine feeding pipe 21 is provided with a flow meter 22 and a fourth valve 23 .
第二出水管16上设有第五阀门17和进水流量计18,第二出水管16接有回流管20,回流管20的另一端与集水池2相连,回流管20上设有第六阀门19。第三进水管25上设有第七阀门26;第一连接管28上设有第一压力表27;第二连接管29上设有第二压力表30;第三出水管32上设有第八阀门31。 The second outlet pipe 16 is provided with a fifth valve 17 and a water inlet flowmeter 18, the second outlet pipe 16 is connected with a return pipe 20, the other end of the return pipe 20 is connected with the sump 2, and the return pipe 20 is provided with a sixth valve. Valve 19. The third inlet pipe 25 is provided with a seventh valve 26; the first connecting pipe 28 is provided with a first pressure gauge 27; the second connecting pipe 29 is provided with a second pressure gauge 30; the third outlet pipe 32 is provided with a first pressure gauge 27; Eight valves31.
过滤器3内自上而下设有滤料层、垫料层及长柄滤头;配药箱24絮凝剂为聚乙烯亚胺PEI复配絮凝剂。过滤器的滤料层由粒径0.9~1.3mm、厚度为1200mm的均质陶粒砂构成;垫料层由粒径4~8mm、厚度为200mm的石英砂构成;长柄滤头数量可以为6只,通过该长柄滤头实现过滤器的气水反冲洗。 The filter 3 is provided with a filter material layer, a cushion material layer and a long-handle filter head from top to bottom; the flocculant in the dispensing box 24 is polyethyleneimine PEI compound flocculant. The filter material layer of the filter is composed of homogeneous ceramsite sand with a particle size of 0.9~1.3mm and a thickness of 1200mm; the cushion layer is composed of quartz sand with a particle size of 4~8mm and a thickness of 200mm; the number of long handle filter heads can be 6 pieces, the air-water backwashing of the filter can be realized through the long handle filter head.
过滤器3的顶部设有排气管39,过滤器3的底部设有排水管36和第二放空管37;排气管39上设有第九阀门40,反冲洗进水管33上设有第十阀门34;排水管36上设有第十一阀门35,放空管37上设有第十二阀门38。 The top of the filter 3 is provided with an exhaust pipe 39, and the bottom of the filter 3 is provided with a drain pipe 36 and a second vent pipe 37; the exhaust pipe 39 is provided with a ninth valve 40, and the backwash water inlet pipe 33 is provided with The tenth valve 34 ; the eleventh valve 35 is arranged on the drain pipe 36 , and the twelfth valve 38 is arranged on the vent pipe 37 .
清水池4设有溢流管47、第二放空管48,第二放空管48上设有第十三阀门49。第四进水管41上设有第十四阀门42;第四出水管45上设有第十五阀门44和冲洗流量计46。压缩空气管50上设有空气流量计51、第三压力表52、第二止回阀53、第十六阀门54。 The clean water pool 4 is provided with an overflow pipe 47 and a second vent pipe 48, and the second vent pipe 48 is provided with a thirteenth valve 49. The fourth water inlet pipe 41 is provided with a fourteenth valve 42 ; the fourth water outlet pipe 45 is provided with a fifteenth valve 44 and a flushing flow meter 46 . The compressed air pipe 50 is provided with an air flow meter 51 , a third pressure gauge 52 , a second check valve 53 and a sixteenth valve 54 .
本实用新型的进水水处理流程如下:隔油池来水由第一进水管6流入隔油池出水渠1,出水经潜污泵7提升至集水池2。集水池2中含油废水经进水泵15发生部分水回流(回流比为3:1),在第二进水管14上进行管式PEI复配絮凝剂投加,废水中乳化油和分散油经破乳絮凝和吸附架桥形成微小絮体,形成含油废水与微絮凝混合水,并被进水泵15依次经过第二出水管16、第三进水管25、第一连接管28抽送至过滤器3。开启第七阀门26、第八阀门31,关闭第十阀门34、第十一阀门35,过滤器3中混合水从上往下,流经滤料并发生微絮凝和接触过滤,通过均质陶粒砂滤料的截留、表面吸附、惯性碰撞、筛分等作用,混合水中乳化油和分散油的微小絮体、COD、浊度物质得到去除,过滤器3出水经第二连接管29、第三出水管32进入清水池4。清水池4贮水水质达到国家一级排放标准,含油废水达到深度处理及回用的目的。 The inlet water treatment process of the utility model is as follows: the incoming water of the grease trap flows into the outlet channel 1 of the grease trap through the first water inlet pipe 6, and the outlet water is lifted to the sump 2 by the submersible sewage pump 7. The oily wastewater in the sump 2 passes through the water inlet pump 15 and part of the water backflows (the reflux ratio is 3:1), and the tubular PEI compound flocculant is added to the second water inlet pipe 14, and the emulsified oil and dispersed oil in the wastewater are broken. Milk flocculation and adsorption bridging form tiny flocs, forming oily wastewater and micro-flocculation mixed water, which is pumped by the inlet pump 15 to the filter 3 through the second outlet pipe 16, the third inlet pipe 25, and the first connecting pipe 28 in sequence. Open the seventh valve 26 and the eighth valve 31, close the tenth valve 34 and the eleventh valve 35, the mixed water in the filter 3 flows through the filter material from top to bottom, micro-flocculation and contact filtration occur, and passes through the homogeneous ceramic Interception, surface adsorption, inertial collision, sieving, etc. of the granular sand filter material, the micro flocs, COD, and turbidity substances of the emulsified oil and dispersed oil in the mixed water are removed, and the water outlet of the filter 3 passes through the second connecting pipe 29, the second Three outlet pipes 32 enter the clear water pool 4. The water quality of the clean water pool 4 meets the national first-class discharge standard, and the oily wastewater reaches the purpose of advanced treatment and reuse.
在过滤器3出水超标时,需对滤床经行气水联合反冲-水反冲洗再生,具体发生方式为:开启第十阀门34、第十一阀门35,关闭第七阀门26、第八阀门31,清水池4贮水通过反冲洗水泵14依次经第四出水管45、反冲洗进水管32、第二连接管29在过滤器3底部形成水层;开启空气压缩机5,压缩空气经压缩空气管路50在过滤器3底部形成气层;过滤器3底部形成的、气层同时从下往上冲洗滤床5min,关闭空气压缩机5、第十六阀门54,单独水层冲洗滤床5min,滤床再生完成,并恢复其吸附容量。 When the outlet water of filter 3 exceeds the standard, the filter bed needs to be regenerated by air-water combined backwash-water backwash. The specific occurrence method is: open the tenth valve 34 and the eleventh valve 35, close the seventh valve Valve 31, clean water pool 4 store water through backwashing water pump 14 successively through the 4th water outlet pipe 45, backwashing water inlet pipe 32, the second connecting pipe 29 to form a water layer at the bottom of filter 3; Turn on air compressor 5, compressed air passes through The compressed air pipeline 50 forms an air layer at the bottom of the filter 3; the air layer formed at the bottom of the filter 3 flushes the filter bed from bottom to top for 5 minutes at the same time, closes the air compressor 5 and the sixteenth valve 54, and the separate water layer flushes the filter bed. After 5 minutes, the regeneration of the filter bed is completed and its adsorption capacity is restored.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107129111A (en) * | 2017-06-23 | 2017-09-05 | 山东海吉雅环保设备有限公司 | A kind of Physical oil field water process device up to standard and handling process |
| CN107285522A (en) * | 2017-08-02 | 2017-10-24 | 金剑环保有限公司 | Air-water back-flushing pressure type constant-speed contact filter and back-flushing method thereof |
| CN107285521A (en) * | 2017-08-02 | 2017-10-24 | 金剑环保有限公司 | Full-automatic pressure type water purification station |
| CN108483753A (en) * | 2018-06-15 | 2018-09-04 | 中铁第六勘察设计院集团有限公司 | A kind of mobile integrated mining method construction wastewater treatment equipment |
| CN118929806A (en) * | 2024-08-29 | 2024-11-12 | 金剑环保集团有限公司 | A fully automatic pressure contact filter |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107129111A (en) * | 2017-06-23 | 2017-09-05 | 山东海吉雅环保设备有限公司 | A kind of Physical oil field water process device up to standard and handling process |
| CN107129111B (en) * | 2017-06-23 | 2020-04-24 | 山东海吉雅环保设备有限公司 | Physical method oil field water treatment standard-reaching device and treatment process |
| CN107285522A (en) * | 2017-08-02 | 2017-10-24 | 金剑环保有限公司 | Air-water back-flushing pressure type constant-speed contact filter and back-flushing method thereof |
| CN107285521A (en) * | 2017-08-02 | 2017-10-24 | 金剑环保有限公司 | Full-automatic pressure type water purification station |
| CN108483753A (en) * | 2018-06-15 | 2018-09-04 | 中铁第六勘察设计院集团有限公司 | A kind of mobile integrated mining method construction wastewater treatment equipment |
| CN108483753B (en) * | 2018-06-15 | 2023-10-31 | 中铁第六勘察设计院集团有限公司 | Mobile integrated mine construction wastewater treatment device |
| CN118929806A (en) * | 2024-08-29 | 2024-11-12 | 金剑环保集团有限公司 | A fully automatic pressure contact filter |
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