CN110156199A - A washing machine waste water recycling system and treatment method - Google Patents
A washing machine waste water recycling system and treatment method Download PDFInfo
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- CN110156199A CN110156199A CN201810144536.9A CN201810144536A CN110156199A CN 110156199 A CN110156199 A CN 110156199A CN 201810144536 A CN201810144536 A CN 201810144536A CN 110156199 A CN110156199 A CN 110156199A
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- 239000002351 wastewater Substances 0.000 title claims abstract description 163
- 238000005406 washing Methods 0.000 title claims abstract description 96
- 238000004064 recycling Methods 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 213
- 238000005189 flocculation Methods 0.000 claims abstract description 131
- 230000016615 flocculation Effects 0.000 claims abstract description 131
- 238000001914 filtration Methods 0.000 claims abstract description 66
- 238000011084 recovery Methods 0.000 claims abstract description 58
- 238000004519 manufacturing process Methods 0.000 claims abstract description 49
- 238000011001 backwashing Methods 0.000 claims abstract description 22
- 239000013049 sediment Substances 0.000 claims abstract description 18
- 239000004576 sand Substances 0.000 claims description 50
- 238000000108 ultra-filtration Methods 0.000 claims description 18
- 239000007788 liquid Substances 0.000 claims description 15
- 238000000746 purification Methods 0.000 claims description 7
- 239000006228 supernatant Substances 0.000 claims description 6
- 230000002457 bidirectional effect Effects 0.000 claims description 5
- 238000011010 flushing procedure Methods 0.000 claims description 4
- 239000002244 precipitate Substances 0.000 claims description 4
- 238000003672 processing method Methods 0.000 claims description 3
- 239000003814 drug Substances 0.000 claims description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 13
- 229910052760 oxygen Inorganic materials 0.000 description 13
- 239000001301 oxygen Substances 0.000 description 13
- 238000012544 monitoring process Methods 0.000 description 7
- 239000010865 sewage Substances 0.000 description 7
- 241000894006 Bacteria Species 0.000 description 5
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 230000002070 germicidal effect Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000004094 surface-active agent Substances 0.000 description 3
- 238000001514 detection method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
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- 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
-
- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- 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
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
-
- 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
- C02F2001/007—Processes including a sedimentation step
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/002—Grey water, e.g. from clothes washers, showers or dishwashers
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/08—Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/10—Energy recovery
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
本发明公开了一种洗衣机废水回收系统及处理方法,所述洗衣机废水回收系统包括通过废水回收管路依次连接导通的废水收集箱、絮凝装置、过滤系统与产水箱;废水收集箱收集洗衣机废水,洗衣机废水经絮凝装置进行絮凝净化、经过滤系统过滤处理后,被回收至产水箱;产水箱经反冲洗系统与过滤装置和絮凝装置依次连通,反冲洗系统利用产水箱中的水对过滤系统和/或絮凝装置进行反向冲洗。通过在废水回收系统中设置反冲洗系统,絮凝装置与过滤系统进行反向冲洗,以实现对絮凝装置和过滤系统中的污物进行及时清理,进而避免了在洗衣机废水回收过程中由于残留沉淀物太多导致回收系统阻塞,影响回收系统正常运行。
The invention discloses a washing machine waste water recovery system and a treatment method. The washing machine waste water recovery system comprises a waste water collection tank, a flocculation device, a filtration system and a water production tank which are connected and connected in sequence through a waste water recovery pipeline; the waste water collection box collects the washing machine waste water. , the washing machine waste water is flocculated and purified by the flocculation device, filtered by the filtration system, and then recycled to the water production tank; the water production tank is connected to the filter device and the flocculation device through the backwash system in turn, and the backwash system uses the water in the water production tank to filter the system. And/or the flocculation unit is back flushed. By setting a backwashing system in the waste water recovery system, the flocculation device and the filtration system are backwashed, so that the dirt in the flocculation device and the filtration system can be cleaned in time, thereby avoiding the residual sediment in the washing machine waste water recycling process. Too much will cause the recycling system to block and affect the normal operation of the recycling system.
Description
技术领域technical field
本发明涉及洗衣领域,具体地说涉及一种洗衣机废水回收系统,还涉及一种洗衣机废水回收系统处理方法。The invention relates to the field of laundry, in particular to a washing machine waste water recycling system, and also to a processing method for the washing machine waste water recycling system.
背景技术Background technique
目前洗衣机废水采用的传统工艺如絮凝沉淀,生化处理等方法去除废水中颗粒悬浮物如线屑,毛发等,但净化装置会残留部分沉淀物,若长期积聚可能出现净化装置堵塞的情况,且传统的净化工艺对色度和细菌的去除率较低,并很少回收废水中的热量;此外洗衣机废水处理设备占地面积较大,基建投资较高,自动化程度低。At present, traditional processes such as flocculation and precipitation, biochemical treatment and other methods are used in washing machine wastewater to remove suspended particles such as lint, hair, etc. in the wastewater, but the purification device will leave some sediment, and if it accumulates for a long time, the purification device may be blocked. The purification process of the washing machine has a low removal rate of chroma and bacteria, and seldom recovers the heat in the wastewater; in addition, the washing machine wastewater treatment equipment occupies a large area, the capital investment is high, and the degree of automation is low.
现有的技术方案公开了一种洗涤污水回用装置,旨在提供一种能有效净化水质且能高效回收利用的洗涤污水回用装置,其技术方案要点是,一种洗涤污水回用装置,包括污水池、第一水泵、过滤机构、清水池,污水池设置有滤网且污水池与第一水泵相连接,第一水泵连接有过滤机构,过滤机构连接清水池,所述的清水池连接有对过滤机构进行反冲洗的反冲洗机构,所述的反冲洗机构包括循环利用水箱、第二水泵、反冲洗废水箱,第二水泵连接过滤机构,循环利用水箱分别与清水池、第二水泵、工业洗衣机相连接,反冲洗废水箱与过滤机构、第一水泵相连接。但该申请污水回收装置未对洗涤污水的热量进行收集,且反冲洗结构复杂,在反冲洗时仅对超滤模块进行冲洗。The existing technical solution discloses a washing sewage reuse device, which aims to provide a washing sewage reuse device that can effectively purify water quality and can be efficiently recycled. It includes a sewage pool, a first water pump, a filtering mechanism, and a clean water pool. The sewage pool is provided with a filter screen and the sewage pool is connected with the first water pump. The first water pump is connected with a filtering mechanism, and the filtering mechanism is connected to the clean water pool. There is a backwashing mechanism for backwashing the filtering mechanism. The backwashing mechanism includes a circulating water tank, a second water pump, and a backwashing waste water tank. The second water pump is connected to the filtering mechanism, and the circulating water tank is respectively connected with the clean water tank and the second water pump. , the industrial washing machine is connected, and the backwash waste water tank is connected with the filtering mechanism and the first water pump. However, the sewage recovery device of this application does not collect the heat of the washing sewage, and the backwashing structure is complicated, and only the ultrafiltration module is washed during backwashing.
有鉴于此特提出本发明。The present invention has been made in view of this.
发明内容SUMMARY OF THE INVENTION
本发明要解决的技术问题在于克服现有技术的不足,提供一种洗衣机废水回收系统,以实现对絮凝装置与过滤系统进行反向冲洗,避免絮凝装置与过滤系统被残留沉淀物堵塞,影响回收系统正常运行的目的。The technical problem to be solved by the present invention is to overcome the deficiencies of the prior art and provide a washing machine waste water recycling system, so as to realize the reverse flushing of the flocculation device and the filtration system, so as to avoid the flocculation device and the filtration system being blocked by residual sediment, which affects the recovery. the purpose of the normal operation of the system.
为解决上述技术问题,本发明采用技术方案的基本构思是:In order to solve the above-mentioned technical problems, the basic conception of the technical scheme adopted in the present invention is:
一种洗衣机废水回收系统,包括通过废水回收管路依次连接导通的废水收集箱、絮凝装置、过滤系统与产水箱;废水收集箱收集洗衣机废水,洗衣机废水经絮凝装置与过滤系统絮凝、过滤后,被回收至产水箱;产水箱经反冲洗系统与过滤装置和絮凝装置依次连通,反冲洗系统利用产水箱中的水对过滤系统和/或絮凝装置进行反向冲洗。A washing machine waste water recovery system, comprising a waste water collection tank, a flocculation device, a filtration system and a water production tank connected in sequence through a waste water recovery pipeline; , is recovered to the water production tank; the production water tank is connected with the filter device and the flocculation device in turn through the backwash system, and the backwash system uses the water in the water production tank to backwash the filter system and/or the flocculation device.
进一步,反冲洗系统的水流方向与废水回收管路内水流方向相反设置,产水箱经反冲洗管路与过滤系统、絮凝装置依次连接导通,产水箱与过滤系统连接导通的管路上设有为反冲洗水流提供动力的第三水泵。Further, the water flow direction of the backwash system is opposite to the water flow direction in the waste water recovery pipeline, the water production tank is connected to the filtration system and the flocculation device in turn through the backwash pipeline, and the production water tank is connected to the filter system. A third water pump that powers the backwash flow.
进一步,过滤系统包括经废水回收管路依次导通的砂滤过滤器、多介质过滤器、超滤模块,砂滤过滤器与多介质过滤器还通过反冲洗管路沿与过滤水流相反的方向导通连接;Further, the filtration system includes a sand filter, a multi-media filter, and an ultrafiltration module that are sequentially connected through the waste water recovery pipeline. The sand filter and the multi-media filter also pass through the backwash pipeline in the opposite direction to the filtered water flow. Conductive connection;
优选的,砂滤过滤器、多介质过滤器、超滤模块依次通过废水回收管路与反冲洗管路双向导通连接。Preferably, the sand filter, the multi-media filter, and the ultrafiltration module are sequentially connected to the backwashing pipeline through the waste water recovery pipeline in a bidirectional manner.
进一步,砂滤过滤器与多介质过滤器上端部设置有过滤进口与过滤出口,下端部设置有反冲洗进口与反冲洗出口,砂滤过滤器的过滤出口与多介质过滤器的过滤进口经废水回收管路连接导通,以供过滤水通过;多介质过滤器的反冲洗出口与砂滤过滤器的反冲洗进口经反冲洗管路沿与过滤水流相反的方向导通连接,以供反冲洗水通过。Further, the upper ends of the sand filter and the multi-media filter are provided with a filtration inlet and a filtration outlet, and the lower end is provided with a backwash inlet and a backwash outlet, and the filtration outlet of the sand filter and the filtration inlet of the multi-media filter pass through waste water. The recovery pipeline is connected and connected to allow the filtered water to pass through; the backwash outlet of the multi-media filter and the backwash inlet of the sand filter are connected through the backwash pipeline in the opposite direction to the filtered water flow for backwashing water through.
优选的,砂滤过滤器与多介质过滤器的反冲洗进口与反冲洗出口均设置有截流装置,以防止反冲洗水回流。Preferably, both the backwash inlet and the backwash outlet of the sand filter and the multi-media filter are provided with intercepting devices to prevent backwash water from flowing back.
进一步,絮凝装置设置有排水出口、进水口与出水口,絮凝装置与砂滤过滤器经废水回收管路与反冲洗管路双向导通连接,絮凝装置的出水口与砂滤过滤器的过滤进口经废水回收管路连接导通,以供过滤水通过;砂滤过滤器的反冲洗出口与絮凝装置的进水口经反冲洗管路沿与过滤水流相反的方向连接导通,以供反冲洗水通过。Further, the flocculation device is provided with a drainage outlet, a water inlet and a water outlet, the flocculation device and the sand filter are connected in a bidirectional manner through the waste water recovery pipeline and the backwash pipeline, and the water outlet of the flocculation device is connected with the filter inlet of the sand filter. It is connected and conducted through the waste water recovery pipeline to allow the filtered water to pass through; the backwash outlet of the sand filter and the water inlet of the flocculation device are connected and conducted through the backwash pipeline in the opposite direction to the filtered water flow for the backwash water. pass.
进一步,产水箱通过反冲洗管路与多介质过滤器的反冲洗进口连接导通,在第三水泵的作用下,产水箱中的水从多介质过滤器的反冲洗进口流入多介质过滤器。Further, the water production tank is connected to the backwash inlet of the multi-media filter through the backwash pipeline, and under the action of the third water pump, the water in the water production tank flows into the multi-media filter from the backwash inlet of the multi-media filter.
进一步,加药箱与絮凝装置进水口经管路连接导通,絮凝装置与加药箱的连接管路上设置有加药泵,在加药泵作用下,加药箱中的絮凝剂被添加至絮凝装置中,絮凝装置中的水在絮凝作用下进行絮凝沉淀。Further, the dosing box and the water inlet of the flocculation device are connected through pipelines, and a dosing pump is arranged on the connecting pipeline between the flocculation device and the dosing box. Under the action of the dosing pump, the flocculant in the dosing box is added to the flocculation. In the device, the water in the flocculation device is flocculated and precipitated under the action of flocculation.
进一步,连接絮凝装置出水口与砂滤过滤器过滤进口的废水回收管路上设置有第二水泵,在第二水泵的作用下,絮凝装置中的洗衣机废水经废水回收管路进入砂滤过滤器进行过滤。Further, a second water pump is provided on the waste water recovery pipeline connecting the water outlet of the flocculation device and the filter inlet of the sand filter. Under the action of the second water pump, the washing machine waste water in the flocculation device enters the sand filter through the waste water recovery pipeline for processing. filter.
本发明另一目的在于提供一种上述所述洗衣机废水回收系统的处理方法,当洗衣机废水净化量达到预设水量时,对过滤系统与絮凝装置进行反冲洗,第三水泵启动,产水箱中的水在第三水泵的作用下依次经连接管路流入过滤系统与絮凝装置中,对过滤系统与絮凝装置进行冲洗。Another object of the present invention is to provide a treatment method for the above-mentioned washing machine waste water recycling system. When the purification volume of washing machine waste water reaches the preset water volume, the filter system and the flocculation device are backwashed, the third water pump is started, and the water in the water production tank is backwashed. Under the action of the third water pump, the water flows into the filter system and the flocculation device through the connecting pipeline in turn, and washes the filter system and the flocculation device.
进一步,反冲洗后的水流入絮凝装置,絮凝装置对反冲洗水进行回收处理,加药泵启动,加药箱中的絮凝剂在加药泵的作用下被添加至絮凝装置,反冲洗水与絮凝剂反应进行絮凝沉淀,絮凝装置中形成沉淀物与上层清液,絮凝装置打开排水出口对沉淀物直接排放,上层清液在第二水泵作用下从絮凝装置出水口流出经过滤系统过滤处理后,再次回收至产水箱。Further, the backwashed water flows into the flocculation device, the flocculation device recycles the backwash water, the dosing pump is started, and the flocculant in the dosing tank is added to the flocculation device under the action of the dosing pump, and the backwash water is mixed with the flocculation device. The flocculant reacts for flocculation and precipitation, and the flocculation device forms sediment and supernatant liquid. The flocculation device opens the drainage outlet to discharge the sediment directly. The supernatant liquid flows out from the water outlet of the flocculation device under the action of the second water pump and is filtered by the filtration system. , which is recycled to the production water tank again.
优选的,反冲洗水对絮凝装置进行反冲洗后,絮凝装置打开排水出口将反冲洗水直接排放。Preferably, after the backwash water backwashes the flocculation device, the flocculation device opens the drain outlet to discharge the backwash water directly.
采用上述技术方案后,本发明与现有技术相比具有以下有益效果:After adopting the above-mentioned technical scheme, the present invention has the following beneficial effects compared with the prior art:
1、在絮凝装置中,洗衣机废水在絮凝作用下产生沉淀,从而除去洗衣机废水中的较大颗粒悬浮物如线屑,毛发以及残留的表面活性剂等;再将絮凝处理后的水流经过滤处理后,令絮凝后洁净水和絮凝物相分离,并使絮凝后洁净水全部流入产水箱内被收集后再利用。1. In the flocculation device, the washing machine wastewater is precipitated under the action of flocculation, so as to remove the larger suspended solids such as lint, hair and residual surfactant in the washing machine wastewater; and then the water after flocculation is filtered. Then, the clean water after flocculation is separated from the floc, and all the clean water after flocculation flows into the water production tank to be collected and reused.
2、回收系统处理洗衣机废水量达到设定值时,对絮凝装置与过滤系统进行反向冲洗,以对絮凝装置和过滤系统中的污物进行及时清理,进而避免了在洗衣机废水回收过程中由于残留沉淀物太多导致回收系统阻塞,影响回收系统正常运行。2. When the waste water volume of the washing machine treated by the recycling system reaches the set value, the flocculation device and the filtration system are backwashed to clean up the dirt in the flocculation device and the filtration system in time, thereby avoiding the waste water recycling process due to the washing machine. Too much residual sediment will cause the recovery system to block and affect the normal operation of the recovery system.
3、洗衣机废水通过化学处理与物理沉淀后,再通过活氧发生器产生的活氧对废水中的COD和色度进行氧化处理,使得废水净化更加全面彻底。3. After the washing machine wastewater is chemically treated and physically precipitated, the COD and chromaticity in the wastewater are oxidized by the active oxygen generated by the active oxygen generator, so that the wastewater purification is more comprehensive and thorough.
4、通过智能水质监测模块对处理后的洗衣机废水水质进行实时检测,使得回收的洗衣机废水水质合格率较高。4. Through the intelligent water quality monitoring module, the water quality of the treated washing machine wastewater is detected in real time, so that the qualified rate of the recycled washing machine wastewater is high.
5、回收系统中设置的热交换装置对废水中热量进行回收,节约能源。5. The heat exchange device set in the recovery system recovers the heat in the waste water and saves energy.
下面结合附图对本发明的具体实施方式作进一步详细的描述。The specific embodiments of the present invention will be described in further detail below with reference to the accompanying drawings.
附图说明Description of drawings
图1是本发明实施例中一种洗衣机废水回收系统结构示意图;1 is a schematic structural diagram of a washing machine waste water recycling system in an embodiment of the present invention;
图2是本发明实施例中一种洗衣机废水回收系统流程示意图。FIG. 2 is a schematic flow diagram of a washing machine waste water recycling system according to an embodiment of the present invention.
图中:1、加药箱;2、加药泵;3、废水收集水箱;4、热交换装置;5、第一水泵;6、絮凝装置;7、第二水泵;8、砂滤过滤器;9、多介质过滤器;10、超滤模块;11、产水箱;12、活氧发生器;13、智能水质监测模块;14、第三水泵。In the figure: 1. Dosing tank; 2. Dosing pump; 3. Waste water collection tank; 4. Heat exchange device; 5. First water pump; 6. Flocculation device; 7. Second water pump; 8. Sand filter 9. Multi-media filter; 10. Ultrafiltration module; 11. Water production tank; 12. Oxygen generator; 13. Intelligent water quality monitoring module; 14. Third water pump.
具体实施方式Detailed ways
实施例一Example 1
如图1所示,本实施例中介绍一种洗衣机废水回收系统,包括通过废水回收管路依次连接导通的废水收集箱3、絮凝装置6、过滤系统与产水箱11;洗衣机排水管与废水收集箱3相连通,废水收集箱3收集洗衣机废水,洗衣机废水经絮凝装置6进行絮凝净化、经过滤系统过滤处理后,被回收至产水箱11;产水箱经反冲洗系统与过滤系统和絮凝装置6依次连通,反冲洗系统利用产水箱11中的水对过滤系统和/或絮凝装置6进行反向冲洗。As shown in FIG. 1 , a washing machine waste water recovery system is introduced in this embodiment, which includes a waste water collection tank 3, a flocculation device 6, a filtration system and a water production tank 11 that are connected in sequence through a waste water recovery pipeline; a washing machine drain pipe and waste water The collection box 3 is connected, and the waste water collection box 3 collects washing machine waste water. The washing machine waste water is flocculated and purified by the flocculation device 6, and after being filtered by the filtration system, it is recycled to the water production tank 11; 6 are connected in sequence, and the backwash system uses the water in the water production tank 11 to backwash the filtration system and/or the flocculation device 6 .
通过在废水回收系统中设置反冲洗系统,絮凝装置6与过滤系统进行反向冲洗,以实现对絮凝装置6和过滤系统中的污物进行及时清理,进而避免了在洗衣机废水回收过程中由于残留沉淀物太多导致回收系统阻塞,影响回收系统正常运行。By setting a backwashing system in the waste water recovery system, the flocculation device 6 and the filtration system are backwashed, so as to realize the timely cleaning of the dirt in the flocculation device 6 and the filtration system, thereby avoiding the residues in the washing machine waste water recycling process. Too much sediment leads to blockage of the recovery system and affects the normal operation of the recovery system.
本实施例中,反冲洗系统沿与废水回收水流相反的方向设置,产水箱11与过滤系统、絮凝装置6依次经反冲洗管路连接导通,产水箱11与过滤系统连接导通的反冲洗管路上设有第三水泵14,在第三水泵14的作用下,产水箱11中的水经过反冲洗管路依次流入过滤系统与絮凝装置6,并对过滤系统与絮凝装置6进行冲洗。In this embodiment, the backwashing system is arranged in the opposite direction to the water flow of the waste water recovery, the water production tank 11 is connected with the filtration system and the flocculation device 6 through the backwashing pipeline in turn, and the backwashing tank 11 is connected with the filtration system. A third water pump 14 is provided on the pipeline. Under the action of the third water pump 14, the water in the water production tank 11 flows into the filtration system and the flocculation device 6 in turn through the backwash pipeline, and flushes the filtration system and the flocculation device 6.
本实施例中,过滤系统包括经废水回收管路依次导通的砂滤过滤器8、多介质过滤器9、超滤模块10,砂滤过滤器8与多介质过滤器9还通过反冲洗管路沿与过滤水流相反的方向导通连接;In this embodiment, the filtration system includes a sand filter 8, a multi-media filter 9, and an ultrafiltration module 10 that are connected in sequence through the waste water recovery pipeline. The sand filter 8 and the multi-media filter 9 also pass through the backwash pipe. The road is connected in the opposite direction to the filtered water flow;
优选的,砂滤过滤器8、多介质过滤器9、超滤模块10依次通过废水回收管路与反冲洗管路双向导通连接。Preferably, the sand filter 8 , the multi-media filter 9 , and the ultrafiltration module 10 are sequentially connected to the backwashing pipeline through the waste water recovery pipeline in a bidirectional manner.
本实施例中,砂滤过滤器8、多介质过滤器9的过滤进出口与反冲洗水进出口设置位置不同。In this embodiment, the filtration inlet and outlet of the sand filter 8 and the multi-media filter 9 are set at different positions from the inlet and outlet of the backwash water.
本实施例中,砂滤过滤器8与多介质过滤器9上端部设置有过滤进口与过滤出口,下端部设置有反冲洗进口与反冲洗出口,砂滤过滤器8的过滤出口与多介质过滤器的过滤进口经废水回收管路连接导通,以供过滤水通过;多介质过滤器9的反冲洗出口与砂滤过滤器8的反冲洗进口经反冲洗管路沿与过滤水流相反的方向导通连接,以供反冲洗水通过。In this embodiment, the upper ends of the sand filter 8 and the multi-media filter 9 are provided with a filter inlet and a filter outlet, the lower ends are provided with a backwash inlet and a backwash outlet, and the filter outlet of the sand filter 8 and the multi-media filter The filter inlet of the filter is connected through the waste water recovery pipeline to allow the filtered water to pass through; the backwash outlet of the multi-media filter 9 and the backwash inlet of the sand filter 8 are in the opposite direction to the filtered water flow through the backwash pipeline. Conductive connection for the passage of backwash water.
本实施例中,砂滤过滤器8与多介质过滤器9的反冲洗进口与反冲洗出口均设置有截流装置,以防止反冲洗水回流。In this embodiment, the backwash inlet and the backwash outlet of the sand filter 8 and the multi-media filter 9 are provided with intercepting devices to prevent backwash water from flowing back.
本实施例中,絮凝装置6设置有排水出口、进水口与出水口,絮凝装置6与砂滤过滤器10经废水回收管路与反冲洗管路双向导通连接,絮凝装置6的出水口与砂滤过滤器的过滤进口经废水回收管路连接导通,以供过滤水通过;砂滤过滤器10的反冲洗出口与絮凝装置的进水口经反冲洗管路沿与过滤水流相反的方向连接导通,以供反冲洗水通过。In this embodiment, the flocculation device 6 is provided with a drainage outlet, a water inlet and a water outlet, the flocculation device 6 and the sand filter 10 are connected in a bidirectional manner through the waste water recovery pipeline and the backwash pipeline, and the water outlet of the flocculation device 6 is connected to the The filtration inlet of the sand filter is connected through the waste water recovery pipeline to allow the filtered water to pass through; the backwash outlet of the sand filter 10 and the water inlet of the flocculation device are connected in the opposite direction to the filtered water flow through the backwash pipeline Conduction for the passage of backwash water.
本实施例中,产水箱11通过管路与多介质过滤器9的反冲洗进口连接导通,在第三水泵的作用下,产水箱中的水从多介质过滤器9的反冲洗进口流入多介质过滤器9。In this embodiment, the water production tank 11 is connected to the backwash inlet of the multi-media filter 9 through a pipeline. Under the action of the third water pump, the water in the water production tank flows into the multi-media filter 9 from the backwash inlet of the multi-media filter 9. Media filter 9.
实时例二Real-time example 2
如图1,2所示,本实施例中介绍了一种上述实施例一所述的洗衣机废水回收系统的处理方法,当废水的处理量达到预设水量时,反冲洗系统利用产水箱中的水对过滤系统与絮凝装置进行冲洗。As shown in FIGS. 1 and 2 , this embodiment introduces a method for processing the waste water recycling system of the washing machine according to the above-mentioned Embodiment 1. When the treatment volume of waste water reaches the preset water volume, the backwash system uses the waste water in the water production tank. Water flushes the filtration system and flocculation unit.
本实施例中,在第三水泵的作用下,反冲洗水经反冲洗管路依次进入多介质过滤器9与砂滤过滤器8,对多介质过滤器9与砂滤过滤器8进行冲洗,多介质过滤器9与砂滤过滤器8中的残留沉淀物随反冲水进入絮凝装置,反冲洗水对砂滤过滤器8进行冲洗,反冲洗完成后,絮凝装置6将反冲洗水直接排放至外部。In this embodiment, under the action of the third water pump, the backwash water enters the multi-media filter 9 and the sand filter 8 in turn through the back-wash pipeline, and washes the multi-media filter 9 and the sand filter 8. The residual sediment in the multi-media filter 9 and the sand filter 8 enters the flocculation device with the backwash water, and the backwash water washes the sand filter 8. After the backwash is completed, the flocculation device 6 directly discharges the backwash water. to the outside.
本实施例中,絮凝装置6收集反冲洗系统中的反冲洗水,当絮凝装置6中的反冲洗水达到一定量后,絮凝装置6对反冲洗水进行絮凝处理,加药泵2同时启动,加药箱1中的絮凝剂在加药泵2的作用下进入絮凝装置6,反冲洗水与絮凝剂反应进行絮凝沉淀,絮凝装置6中形成沉淀物与上层清液,沉淀物直接排放,上层清液则经回收系统处理后,再次回收至产水箱。In this embodiment, the flocculation device 6 collects the backwash water in the backwash system. When the backwash water in the flocculation device 6 reaches a certain amount, the flocculation device 6 performs flocculation treatment on the backwash water, and the dosing pump 2 starts simultaneously. The flocculant in the dosing tank 1 enters the flocculation device 6 under the action of the dosing pump 2, and the backwash water reacts with the flocculant to flocculate and precipitate. The clear liquid is processed by the recycling system and recycled to the water production tank again.
本实施例中,在回收系统停止工作中后对过滤系统与絮凝装置6进行冲洗,以避免过滤机构与絮凝装置6中的残留沉淀物在系统长期闲置时滋生细菌。In this embodiment, the filter system and the flocculation device 6 are flushed after the recovery system stops working, so as to prevent the residual sediment in the filter mechanism and the flocculation device 6 from breeding bacteria when the system is idle for a long time.
本实施例中,回收系统可设置为每间隔T1时间对过滤系统与絮凝装置6进行冲洗。对过滤系统与絮凝装置6定时进行冲洗,以避免在洗衣机废水回收过程中由于残留沉淀物太多导致系统阻塞,影响回收系统正常运行。In this embodiment, the recovery system can be set to flush the filter system and the flocculation device 6 every time T1. The filtration system and the flocculation device 6 are regularly flushed to avoid system blockage due to too much residual sediment during the recycling process of washing machine wastewater, which affects the normal operation of the recycling system.
实施例三Embodiment 3
如图1所示,本发明实施例中介绍了一种洗衣机废水回收系统,包括通过管路依次连接导通的废水收集箱3、絮凝装置6、过滤系统、产水箱11;废水收集箱3收集洗衣机废水,洗衣机废水经絮凝装置6与过滤系统絮凝、过滤后,被回收至产水箱11;废水收集箱3与絮凝装置6连接管路上设置有热交换装置4,热交换装置4对洗衣机废水中的热量进行回收。As shown in FIG. 1 , a washing machine waste water recycling system is introduced in the embodiment of the present invention, which includes a waste water collection tank 3, a flocculation device 6, a filtration system, and a water production tank 11 that are connected and conducted in sequence through pipelines; the waste water collection box 3 collects Washing machine waste water, after being flocculated and filtered by the flocculation device 6 and the filtration system, is recycled to the water production tank 11; the waste water collection tank 3 and the flocculation device 6 are connected with a heat exchange device 4 on the pipeline. heat is recovered.
本实施例中,热交换装置4还设置有常温水通道,常温水流经热交换装置4时,吸收洗衣机废水中的热量,以将洗衣机废水中的热量进行回收利用。优选的,产水箱11与热交换装置4经管路连接导通,产水箱11中的水再利用时,流经热交换装置4,对热交换装置中洗衣机废水的热量进行吸收。通过热交换装置4对废水中的热量进行回收利用,节约了大量能源。In this embodiment, the heat exchange device 4 is also provided with a normal temperature water channel. When the normal temperature water flows through the heat exchange device 4, it absorbs the heat in the waste water of the washing machine to recycle the heat in the waste water of the washing machine. Preferably, the water production tank 11 and the heat exchange device 4 are connected through pipelines, and when the water in the water production tank 11 is reused, it flows through the heat exchange device 4 to absorb the heat of the washing machine waste water in the heat exchange device. The heat in the wastewater is recycled and utilized by the heat exchange device 4, which saves a lot of energy.
本实施例中,废水收集箱3中设置有液位检测装置,对废水收集箱中的液位进行检测,当废水收集箱中的液位达到设定值后,废水回收系统启动,当液位低于设定值,废水回收系统处于待机状态和/或关机状态。In this embodiment, the waste water collection tank 3 is provided with a liquid level detection device to detect the liquid level in the waste water collection tank. When the liquid level in the waste water collection tank reaches the set value, the waste water recovery system is started. Below the set value, the waste water recovery system is in standby and/or off state.
本实施例中,加药箱1与絮凝装置6的进水口经管路连接导通,絮凝装置6与加药箱1的连接管路上设置有加药泵2,在加药泵2作用下,加药箱1中的絮凝剂被添加至絮凝装置6中,并与洗衣机废水发生反应,对洗衣机废水中污染物进行絮凝沉淀。通过絮凝作用,除去洗衣机废水中的较大颗粒悬浮物如线屑、毛发、以及残留的表面活性剂等。In this embodiment, the water inlet of the dosing box 1 and the flocculation device 6 are connected through pipelines, and a dosing pump 2 is arranged on the connecting pipeline between the flocculation device 6 and the dosing box 1. The flocculant in the medicine box 1 is added to the flocculation device 6 and reacts with the waste water of the washing machine to flocculate and precipitate the pollutants in the waste water of the washing machine. Through flocculation, larger suspended particles such as lint, hair, and residual surfactants in washing machine wastewater are removed.
本实施例中,回收系统还包括有第一水泵5、第二水泵7,第一水泵5设置在废水收集箱3与絮凝装置6的进水口连接管路上,在第一水泵5的作用下,废水收集箱3中的洗衣机废水经管路被输送至絮凝装置6中进行絮凝处理;第二水泵7设置于絮凝装置6的出水口与过滤系统连接管路上,在第二水泵7的作用下,经过絮凝的洗衣机废水进入过滤系统进行过滤处理。In this embodiment, the recovery system further includes a first water pump 5 and a second water pump 7. The first water pump 5 is arranged on the connection pipeline between the waste water collection tank 3 and the water inlet of the flocculation device 6. Under the action of the first water pump 5, The washing machine waste water in the waste water collection tank 3 is transported to the flocculation device 6 through the pipeline for flocculation treatment; the second water pump 7 is arranged on the connection pipeline between the water outlet of the flocculation device 6 and the filtration system. The flocculated washing machine wastewater enters the filtration system for filtration treatment.
本实施例中,过滤系统与产水箱11的连接管路上设置有活氧发生器12。超滤后,洗衣机废水进入活氧发生器12,活氧发生器12产生活氧对洗衣机废水进行氧化处理,除去洗衣机废水中的COD以及色度,使得废水净化更加彻底。优选的,在过滤系统与产水箱11的连接管路上设置有紫外线杀菌灯。超滤后,紫外线杀菌灯打开对洗衣机废水进行照射杀菌。洗衣机废水经紫外线杀菌灯照射杀菌,可除去废水中的细菌,提升净化水的质量。In this embodiment, an active oxygen generator 12 is provided on the connecting pipeline between the filtration system and the water production tank 11 . After ultrafiltration, the washing machine wastewater enters the active oxygen generator 12, and the active oxygen generator 12 generates living oxygen to oxidize the washing machine wastewater, remove the COD and chromaticity in the washing machine wastewater, and make the wastewater purification more thorough. Preferably, an ultraviolet germicidal lamp is provided on the connecting pipeline between the filtering system and the water production tank 11 . After ultrafiltration, the ultraviolet germicidal lamp is turned on to irradiate and sterilize the waste water of the washing machine. Washing machine wastewater is sterilized by ultraviolet germicidal lamp irradiation, which can remove bacteria in wastewater and improve the quality of purified water.
本实施例中,过滤系统与产水箱11的连接管路上设有智能水质监测模块13,智能水质监测模块13可同时测试回收处理后的洗衣机废水的温度,浊度,TDS以及洗涤液有机物残留量,以判定回收处理后的洗衣机废水的水质是否符合标准,若水质符合回收标准,回收处理后的洗衣机废水进入产水箱11待用;若水质不符合回收标准时,回收处理后的洗衣机废水回流至絮凝装置6继续进行絮凝、过滤。In this embodiment, an intelligent water quality monitoring module 13 is provided on the connecting pipeline between the filtration system and the water production tank 11, and the intelligent water quality monitoring module 13 can simultaneously test the temperature, turbidity, TDS and residual amount of organic matter in the washing machine after recycling and processing. , to determine whether the water quality of the recycled washing machine wastewater meets the standards. If the water quality meets the recycling standards, the recycled washing machine wastewater will enter the water production tank 11 for use; if the water quality does not meet the recycling standards, the recycled washing machine wastewater will flow back to flocculation. The device 6 continues to perform flocculation and filtration.
本实施例中,产水箱11连接有反冲洗系统,反冲洗系统利用产水箱中的水对过滤系统与絮凝装置6进行冲洗。对过滤系统以及絮凝装置6进行反冲洗,能够及时的将残留在过滤机构与絮凝装置6中的沉淀物进行收集排放,避免了沉淀物积聚后阻塞回收系统通道,影响回收系统正常运行。In this embodiment, the water production tank 11 is connected with a backwashing system, and the backwashing system uses the water in the water production tank to flush the filtration system and the flocculation device 6 . Backwashing the filtration system and the flocculation device 6 can collect and discharge the sediment remaining in the filtration mechanism and the flocculation device 6 in time, so as to avoid blocking the recovery system channel after the sediment accumulates and affect the normal operation of the recovery system.
本实施例中,过滤系统包括通过管路依次导通的砂滤过滤器8、多介质过滤器9、超滤模块10,砂滤过滤器8、多介质过滤器9、超滤模块10依次对流经的洗衣机废水进行过滤处理。In this embodiment, the filtration system includes a sand filter 8, a multi-media filter 9, and an ultrafiltration module 10 that are connected in sequence through pipelines. The sand filter 8, the multi-media filter 9, and the ultrafiltration module 10 convection in sequence. The washing machine wastewater is filtered.
本实施例中,过滤系统还包括反渗透模块,反渗透模块可对超滤后的洗衣机废水进行深度过滤;优选的,洗衣机废水通过管路依次流经砂滤过滤器8、多介质过滤器9、超滤模块10、反渗透模块。In this embodiment, the filtration system further includes a reverse osmosis module, which can perform deep filtration on the ultra-filtered washing machine waste water; preferably, the washing machine waste water flows through the sand filter 8 and the multi-media filter 9 in sequence through pipelines , ultrafiltration module 10, reverse osmosis module.
本实施例中,絮凝装置6、砂滤过滤器8以及多介质过滤器9设置有反冲洗通道,在第三水泵14的作用下,产水箱中的水通过反冲洗管路依次流入多介质过滤器9、砂滤过滤器8、絮凝装置6中,对多介质过滤器9、砂滤过滤器8、絮凝装置6进行冲洗。In this embodiment, the flocculation device 6, the sand filter 8 and the multi-media filter 9 are provided with a backwash channel. Under the action of the third water pump 14, the water in the water production tank flows into the multi-media filter sequentially through the backwash pipeline. In the filter 9 , the sand filter 8 and the flocculation device 6 , the multi-media filter 9 , the sand filter 8 and the flocculation device 6 are washed.
优选的,超滤模块10设置有反冲洗通道,在第三水泵14的作用下,产水箱11中的水通过反冲洗管路依次流入超滤模块10、多介质过滤器9、砂滤过滤器8以及絮凝装置6中,并对超滤模块10、多介质过滤器9、砂滤过滤器8以及絮凝装置6进行冲洗。Preferably, the ultrafiltration module 10 is provided with a backwash channel. Under the action of the third water pump 14, the water in the water production tank 11 flows into the ultrafiltration module 10, the multi-media filter 9, and the sand filter sequentially through the backwash pipeline. 8 and the flocculation device 6 , and rinse the ultrafiltration module 10 , the multimedia filter 9 , the sand filter 8 and the flocculation device 6 .
实施例四Embodiment 4
如图2所示,本发明实施例中介绍了一种实施例一所述洗衣机回收系统的处理方法,系统执行废水回收程序时至少对洗衣机废水中的热量进行回收,洗衣机废水通过热交换装置时,将热量传递给常温水,以对废水中的热量进行回收利用。对洗衣机废水中的热量回收,使得洗衣机废水中的热能被充分利用,节约能源。As shown in FIG. 2 , an embodiment of the present invention introduces a processing method of the washing machine recycling system according to the first embodiment. When the system executes the waste water recycling program, at least the heat in the washing machine waste water is recovered. When the washing machine waste water passes through the heat exchange device , transfer the heat to normal temperature water to recycle the heat in the wastewater. The heat recovery in the washing machine waste water makes full use of the heat energy in the washing machine waste water and saves energy.
本实施例中,废水收集箱收集洗衣机洗衣后排放的废水,废水收集箱中设置的液位检测装置检测废水收集箱中的液位,当废水收集箱中的液位达到设定值,废水回收系统启动,对洗衣机废水进行絮凝、过滤回收;当废水收集箱中的液位低于设定值时,废水回收系统处于待机状态和/或关机状态。对洗衣机废水定量处理,能够使废水充分净化。In this embodiment, the waste water collection tank collects the waste water discharged by the washing machine after washing, and the liquid level detection device set in the waste water collection tank detects the liquid level in the waste water collection tank. When the liquid level in the waste water collection tank reaches the set value, the waste water is recovered The system starts to flocculate, filter and recycle the waste water from the washing machine; when the liquid level in the waste water collection tank is lower than the set value, the waste water recovery system is in a standby state and/or a shutdown state. Quantitative treatment of washing machine wastewater can fully purify the wastewater.
本实施例中,废水回收系统启动后,废水收集箱中的洗衣机废水与产水箱中的常温水流入热交换装置,在热交换装置中,洗衣机废水的热量通过热交换装置传动给常温水,从而对废水中的热量进行回收利用。In this embodiment, after the waste water recovery system is activated, the washing machine waste water in the waste water collection tank and the normal temperature water in the water production tank flow into the heat exchange device. In the heat exchange device, the heat of the washing machine waste water is transmitted to the normal temperature water through the heat exchange device, thereby Recycle heat from wastewater.
本实施例中,在第一水泵作用下,洗衣机废水流经热交换装置后进入絮凝装置,加药泵启动,加药箱中的絮凝剂在加药泵的作用下进入絮凝装置,絮凝剂与洗衣机废水发生反应,对洗衣机废水中的污染物进行絮凝沉淀;对洗衣机废水进行一定时间的絮凝沉淀后,絮凝装置中形成沉淀物与上层清液,上层清液在第二水泵的作用下进入砂滤过滤器;絮凝装置中的沉淀物直接进行排放。洗衣机废水在絮凝装置中经化学处理,洗衣机废水中的较大颗粒悬浮物如线屑,毛发以及残留的表面活性剂等被去除。In this embodiment, under the action of the first water pump, the waste water from the washing machine flows through the heat exchange device and then enters the flocculation device, the dosing pump is started, and the flocculant in the dosing tank enters the flocculation device under the action of the dosing pump, and the flocculant and the dosing pump enter the flocculation device. The washing machine wastewater reacts to flocculate and precipitate the pollutants in the washing machine wastewater; after the washing machine wastewater is flocculated and precipitated for a certain period of time, sediment and supernatant liquid are formed in the flocculation device, and the supernatant liquid enters the sand under the action of the second water pump. filter; the sediment in the flocculation device is directly discharged. Washing machine wastewater is chemically treated in a flocculation unit, and larger suspended solids such as lint, hair and residual surfactants in washing machine wastewater are removed.
本实施例中,砂滤过滤器、多介质过滤器以及超滤模块依次对流经的洗衣机废水中的污染物进行过滤处理。洗衣机废水经过多层过滤,将废水中的絮凝体、颗粒物、微生物、细菌等进行过滤截留。In this embodiment, the sand filter, the multi-media filter and the ultrafiltration module sequentially filter the pollutants in the washing machine waste water that flows through. Washing machine wastewater is filtered through multiple layers to filter and retain flocs, particulates, microorganisms, bacteria, etc. in the wastewater.
本实施例中,洗衣机废水经过超滤后,进入活氧发生器,活氧发生器产生的活氧对洗衣机进行氧化处理,除去废水中残留的污染物。利用活氧发生器产生的活氧对废水中的细菌、COD以及色度等进行氧化处理,使废水净化的更加彻底。In this embodiment, the waste water of the washing machine enters the active oxygen generator after ultrafiltration, and the active oxygen generated by the active oxygen generator oxidizes the washing machine to remove the residual pollutants in the waste water. The active oxygen generated by the active oxygen generator is used to oxidize bacteria, COD and chromaticity in the wastewater, so that the wastewater can be purified more thoroughly.
本实施例中,废水从活氧发生器中出来后进入智能水质监测模块,智能水质监测模块对废水的水质进行检测并判定净化后的洗衣机废水是否符合回收标准,若净化后的洗衣机废水水质符合回收标准,则净化后的洗衣机废水流入产水箱待用;若净化后的洗衣机废水水质不符合回收标准,则洗衣机废水回流至絮凝装置,继续对洗衣机废水进行絮凝、过滤等净化处理。In this embodiment, after the waste water comes out of the active oxygen generator, it enters the intelligent water quality monitoring module, and the intelligent water quality monitoring module detects the water quality of the waste water and determines whether the purified washing machine waste water meets the recycling standard. If the water quality of the purified washing machine wastewater does not meet the recycling standard, the washing machine wastewater will be returned to the flocculation device, and the washing machine wastewater will continue to be purified by flocculation and filtration.
本实施例中,智能水质监测模块可同时测试洗衣机废水的温度,浊度,TDS,洗涤液有机物残留量,并可将监测到的水质数据进行实时显示,操作人员可通过显示的水质信息调节工艺流程。In this embodiment, the intelligent water quality monitoring module can simultaneously test the temperature, turbidity, TDS, and residual amount of organic matter in the washing machine wastewater, and can display the monitored water quality data in real time, and the operator can adjust the process through the displayed water quality information. process.
本实施例中,对过滤系统和/或絮凝装置进行反冲洗时,产水箱中的水在第三水泵的作用下流入过滤系统,对过滤装置中的沉淀物进行冲洗,对过滤系统执行一定时间的反冲洗后,反冲洗水流入絮凝装置,对絮凝装置进行冲洗,冲洗完成后,将冲洗后的水直接排放。对过滤系统与絮凝装置进行定时冲洗以防止残留沉淀物堵塞系统。优选的,对过滤系统执行一定时间的反冲洗后,水进入絮凝装置,絮凝装置对冲洗水进行回收处理。In this embodiment, when backwashing the filtration system and/or the flocculation device, the water in the water production tank flows into the filtration system under the action of the third water pump, and the sediment in the filtration device is washed, and the filtration system is executed for a certain period of time. After the backwashing is completed, the backwashing water flows into the flocculation device to flush the flocculation device. After the flushing is completed, the flushed water is directly discharged. Periodically flush the filtration system and flocculation unit to prevent residual sediment from clogging the system. Preferably, after the filtration system is backwashed for a certain period of time, the water enters the flocculation device, and the flocculation device recycles the flushing water.
以上所述仅是本发明的较佳实施例而已,并非对本发明作任何形式上的限制,虽然本发明已以较佳实施例揭示如上,然而并非用以限定本发明,任何熟悉本专利的技术人员在不脱离本发明技术方案范围内,当可利用上述提示的技术内容做出些许更动或修饰为等同变化的等效实施例,但凡是未脱离本发明技术方案的内容,依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本发明方案的范围内。The above descriptions are only preferred embodiments of the present invention, and do not limit the present invention in any form. Although the present invention has been disclosed above with preferred embodiments, it is not intended to limit the present invention. Anyone familiar with the technology of this patent Within the scope of the technical solution of the present invention, personnel can make some changes or modifications to equivalent examples of equivalent changes by using the above-mentioned technical content, but any content that does not depart from the technical solution of the present invention, according to the present invention. Any simple modifications, equivalent changes and modifications made to the above embodiments in the technical essence still fall within the scope of the solution of the present invention.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110563227A (en) * | 2019-09-30 | 2019-12-13 | 杭州太赫环保科技有限公司 | Wastewater zero-discharge treatment device |
CN111467857A (en) * | 2020-03-27 | 2020-07-31 | 合肥云雀智能科技有限公司 | Water purifier |
CN112914464A (en) * | 2019-12-06 | 2021-06-08 | E.G.O.电气设备制造股份有限公司 | Water-conducting domestic appliance and method for operating such a water-conducting domestic appliance |
CN118029485A (en) * | 2024-02-04 | 2024-05-14 | 江苏铭星供水设备有限公司 | Aseptic direct-drinking intelligent water supply system |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1673123A (en) * | 2005-03-15 | 2005-09-28 | 北京交通大学 | Treating method and micro flocculation reactor for reusing washing sewage |
CN101412551A (en) * | 2008-11-13 | 2009-04-22 | 同济大学 | Enhanced flocculation-hyperfiltration combined process and apparatus for emergency handling of drinking water |
CN102115288A (en) * | 2011-01-28 | 2011-07-06 | 吴紫城 | Method and equipment for recycling and treating vehicle cleaning and laundry wastewater |
CN202186929U (en) * | 2011-08-31 | 2012-04-11 | 浙江维兰特流体科技有限公司 | Washing sewage recycling device |
CN203238140U (en) * | 2013-05-13 | 2013-10-16 | 天津中海汇通科技有限公司 | Multi-stage deep wastewater circulating treatment system |
CN103896455A (en) * | 2014-03-28 | 2014-07-02 | 北京北控海创科技有限公司 | Biological pretreatment technology for seawater reverse osmosis method |
CN105217892A (en) * | 2015-10-27 | 2016-01-06 | 中国环境科学研究院 | A kind of petrochemical industry comprehensive wastewater treatment unit and petrochemical industry integrated waste water treatment method |
CN105884089A (en) * | 2016-07-04 | 2016-08-24 | 山东中移能节能环保科技股份有限公司 | Advanced treatment and recycling process for coking wastewater |
CN107555647A (en) * | 2017-04-17 | 2018-01-09 | 贵州中大方正水务环保有限公司 | Intelligent integration formula purifier |
-
2018
- 2018-02-12 CN CN201810144536.9A patent/CN110156199A/en active Pending
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1673123A (en) * | 2005-03-15 | 2005-09-28 | 北京交通大学 | Treating method and micro flocculation reactor for reusing washing sewage |
CN101412551A (en) * | 2008-11-13 | 2009-04-22 | 同济大学 | Enhanced flocculation-hyperfiltration combined process and apparatus for emergency handling of drinking water |
CN102115288A (en) * | 2011-01-28 | 2011-07-06 | 吴紫城 | Method and equipment for recycling and treating vehicle cleaning and laundry wastewater |
CN202186929U (en) * | 2011-08-31 | 2012-04-11 | 浙江维兰特流体科技有限公司 | Washing sewage recycling device |
CN203238140U (en) * | 2013-05-13 | 2013-10-16 | 天津中海汇通科技有限公司 | Multi-stage deep wastewater circulating treatment system |
CN103896455A (en) * | 2014-03-28 | 2014-07-02 | 北京北控海创科技有限公司 | Biological pretreatment technology for seawater reverse osmosis method |
CN105217892A (en) * | 2015-10-27 | 2016-01-06 | 中国环境科学研究院 | A kind of petrochemical industry comprehensive wastewater treatment unit and petrochemical industry integrated waste water treatment method |
CN105884089A (en) * | 2016-07-04 | 2016-08-24 | 山东中移能节能环保科技股份有限公司 | Advanced treatment and recycling process for coking wastewater |
CN107555647A (en) * | 2017-04-17 | 2018-01-09 | 贵州中大方正水务环保有限公司 | Intelligent integration formula purifier |
Non-Patent Citations (1)
Title |
---|
(美)鲁本斯坦: "《建筑机械与电气设备》", 30 April 2003, 大连理工大学出版社 * |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110563227A (en) * | 2019-09-30 | 2019-12-13 | 杭州太赫环保科技有限公司 | Wastewater zero-discharge treatment device |
CN112914464A (en) * | 2019-12-06 | 2021-06-08 | E.G.O.电气设备制造股份有限公司 | Water-conducting domestic appliance and method for operating such a water-conducting domestic appliance |
CN111467857A (en) * | 2020-03-27 | 2020-07-31 | 合肥云雀智能科技有限公司 | Water purifier |
CN111467857B (en) * | 2020-03-27 | 2022-03-25 | 合肥云雀智能科技有限公司 | Water purifier |
CN118029485A (en) * | 2024-02-04 | 2024-05-14 | 江苏铭星供水设备有限公司 | Aseptic direct-drinking intelligent water supply system |
CN118029485B (en) * | 2024-02-04 | 2025-01-07 | 江苏铭星供水设备有限公司 | A sterile direct drinking intelligent water supply system |
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