CN2858629Y - Processing reuse device for used vehicle and clothes washing water - Google Patents

Processing reuse device for used vehicle and clothes washing water Download PDF

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Publication number
CN2858629Y
CN2858629Y CN 200520036165 CN200520036165U CN2858629Y CN 2858629 Y CN2858629 Y CN 2858629Y CN 200520036165 CN200520036165 CN 200520036165 CN 200520036165 U CN200520036165 U CN 200520036165U CN 2858629 Y CN2858629 Y CN 2858629Y
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CN
China
Prior art keywords
electrolyzer
shell
water
aeration tube
colloid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 200520036165
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Chinese (zh)
Inventor
陈国东
杨莉
陈丽曼
黄素华
朱贻凤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHENGDU DONGHUI QINGYUAN ENVIRONMENTAL ENGINEERING EQUIPMENT Co Ltd
Original Assignee
CHENGDU DONGHUI QINGYUAN ENVIRONMENTAL ENGINEERING EQUIPMENT Co Ltd
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Filing date
Publication date
Application filed by CHENGDU DONGHUI QINGYUAN ENVIRONMENTAL ENGINEERING EQUIPMENT Co Ltd filed Critical CHENGDU DONGHUI QINGYUAN ENVIRONMENTAL ENGINEERING EQUIPMENT Co Ltd
Priority to CN 200520036165 priority Critical patent/CN2858629Y/en
Application granted granted Critical
Publication of CN2858629Y publication Critical patent/CN2858629Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a wash vehicle and apparatus for recycling waste water of washing clothing. The apparatus includes an outer shell (18), a floatation apparatus, an electroanalysis apparatus (7), a filter apparatus (8), a defoaming apparatus (6), a bubble collecting tube (5), a circuit controlling case (12) and a dynamic pipe system, the floatation apparatus is compose of blower (3), wind can (14), aeration pipe (4) and gum membrane (2). Waste gas is cleaned with the floatation apparatus, electroanalysis apparatus (7) and filter apparatus (8) in turn after the gas inter the outer shell, and the floatation apparatus is capable of eliminating most of soil colloid particles, cation surface active agent and suspended substances. The utility model has stronger ability of long time processing, stable effect and higher efficiency and lower cost of processing when compared with existing technique.

Description

Carwash and laundrywastes are handled equipment for reclaiming
Technical field
The utility model relates to a kind of wastewater treatment and renovation equipment, and particularly a kind of carwash and laundrywastes are handled equipment for reclaiming.
Background technology
At present Small Washing parking lot and small-sized laundry spread all over the country, and the waste water after carwash and the laundry mostly is disposable use and just discharges, and this is the serious waste water resources not only, and arbitrarily discharging also can cause the pollution of water surrounding.
Pollution factor in carwash and the laundrywastes mainly contains anion surfactant (LAS), microorganism oxygen-consumption (COD), suspended substance (SS) and soil colloid particulate.The technological treatment that existing carwash and laundrywastes processing reclamation set mainly adopt has: (1). and use desilting, oil removal means purifying treatment, this method can only be removed particle in the water, can not remove colloidalmaterial; (2). on the technology basis of (1), add flocculation treatment and remove pollutent, though this method can be removed oils, suspended substance, COD and LAS to a certain extent, but big because of dosage, sludge quantity is big, the processing cost height, therefore less economical, and water quality is also unstable; (3). adopt methods such as biological method and membrane filtration nanofiltration to carry out purifying treatment, use the device of these methods because the soil colloid particle diameter is less, even its filtration unit is having under the situation of back flushing, still stop up easily, therefore processing power descends in the course of time, effect is difficult to guarantee that the one-time investment cost of adding the nanofiltration membrane filtration is higher, also allows the user be difficult to accept; (4). adopt single electrochemical method to handle, though this method can be removed colloidal solids a large amount of in the sewage and anionic part tensio-active agent, make water quality look comparatively limpid, but the clearance for anion surfactant is still lower, is difficult to make sewage reach the reuse effect in a large number apace.From on can find out that existing carwash is handled reclamation set with laundrywastes and all had certain defective separately, therefore need a kind of more perfect wastewater treatment and renovation equipment and replace existing carwash and laundrywastes processing reclamation set.
Summary of the invention
The purpose of this utility model be to overcome the deficiencies in the prior art and provide that a kind of long-time continuous processing power is strong, the treatment effect stabilization energy reaches the quality of reused water standard, processing efficiency height and low carwash and the laundrywastes of processing cost handled equipment for reclaiming.
For achieving the above object, the solution that the utility model adopts is: this equipment comprises shell, electrolyzer, filtration unit, circuit control box and power piping system, electrolyzer comprises battery lead plate, pilot circuit and electrolyzer, circuit control box is installed in the enclosure, the utility model also includes air-floating apparatus, defoaming device, bubble collecting tube and plate, described air-floating apparatus is by blower fan, air duct, aeration tube and colloid adsorption unit are formed, aeration tube is installed in the bottom of the upper cavity of shell, the colloid adsorption unit is installed in aeration tube top in the upper cavity, the two ends of air duct link to each other with aeration tube with blower fan respectively, the collection mouth of bubble collecting tube upper end is positioned at the intravital foam habitat of shell epicoele, the lower end is connected on the foam defoaming device, two plates tilt to be fixed on the top of shell upper cavity, and formation makes foam stream collect the passage of mouth to foam, the bottom of shell upper cavity is provided with throw out row mouth, water-in is positioned on the shell upper cavity, described electrolyzer is installed in the cavity at shell middle part, the upper end of road pipe is positioned at the below of the shell upper cavity water surface, the lower end places in the electrolyzer, the bottom surface of electrolyzer is processed with the hole that throw out is discharged, and be provided with and make throw out from the dope row mouthful passage of discharging, filtration unit is installed in the cavity of outer casing underpart, the top of rising pipe places the underwater of electrolyzer, the lower end places filtration unit, the cavity of outer casing underpart is that water purification holds case, and water purification row mouth is located on this cavity.
Colloid adsorption unit in the such scheme is the colloid biofilm, and this biofilm hangs on the aeration tube.
Filtration unit in the such scheme can adopt the drawer type filter screen, places the chlorine tablet in the filter screen.
The pole plate of the electrolyzer in the such scheme is the aluminium plate.
During work, open the buoyancy switch in wastewater collection pond, waste water enters efficient air-floating apparatus case (shell upper cavity) through pump by water-in, blower fan running this moment, gas enters efficient air-floating apparatus by aeration tube, impact along with air-flow, anion surfactant in the waste water is foamed by air supporting, the collection mouth of crossing the bubble collecting tube upper end with air communication enters defoaming device, the soil colloid material is hung on the biofilm absorption on the aeration tube in aeration, it is big that gathering becomes, and the particulate matter post precipitation that final formation is bigger is regularly arranged mouth by throw out and discharged back wastewater collection pond precipitation.Enter electrolyzer by the water of cleaning after the efficient air-floating apparatus processing by pipeline, in electrolyzer, the soil colloid material is attracted to around the pole plate, the micro-positively charged ion of plate stripping has formed the colloid aggregation core simultaneously, colloidal solid is grown up become precipitation, from the hole of electrolyzer base plate, flow out by dope row mouth and discharge back wastewater collection pond precipitation.The micro-bubble that electrolysis produces in the electrolyzer continues to make the anion surfactant foaming to be trapped in the surface to treat regular removal in addition, and simultaneously because the anode dissolution phenomenon, the pollutants in waste water flocculation is agglomerating, flows with water and removes through filtration unit.Water after device filters after filtration enters the water purification casing, by preparing against reuse in the regular suction water tank of pump.The water quality of water can reach the quality of reused water standard in the clear water tanks.
The utility model compared with prior art has following effect: (1) the long time treatment ability is strong continuously, and treatment effect is stable, and its water quality of purifying waste water can reach the requirement of " urban sewage reutilization city miscellaneous water water quality " GB/T18920-2002 after tested; (2) processing efficiency height can be stablized and reaches day output 2-4 ton; (3) processing cost is low; (4) simple in structure, volume is little; (5) easy to operate.
Description of drawings
Fig. 1 is a sectional view of the present utility model.
Fig. 2 is the vertical view of electrolyzer.
Among the figure: 1-water-in 2-biofilm 3-blower fan 4-aeration tube 5-bubble collecting tube 501-foam is collected a mouthful 6-defoaming device 7-electrolyzer 701-battery lead plate 8-filtration unit 9-clear water tanks 10-dope row mouthful 11-water purification row mouthful 12-circuit control box 13-throw out row mouthful 14-air duct 15-plate 16-pipeline 17-rising pipe 18-shell
Embodiment
As shown in Figure 1, the utility model is made of shell 18, electrolyzer 7, circuit control box 12, air-floating apparatus, defoaming device 6, bubble collecting tube 5, plate 15, filtration unit 8, shell 18 comprises upper chamber, middle part cavity and lower cavity, air-floating apparatus is installed in the upper chamber, it comprises blower fan 3, air duct 14, aeration tube 4 and colloid biofilm 2, aeration tube 4 places the bottom of upper cavity, colloid biofilm 2 hangs on the aeration tube 4, when aeration tube 4 aerations, biofilm 2 is floated in upper cavity, absorption soil colloidalmaterial.Blower fan 3 places the bottom of shell 18, and an end of air duct 14 links to each other with blower fan 3, and the other end is connected with aeration tube 4, and the vertex of air duct 14 is positioned at upper cavity top, and doing like this is to avoid air duct 14 water inlets.Defoaming device 6 is installed in the bottom of shell 18, the lower end of bubble collecting tube 5 links to each other with defoaming device 6, the upper end is positioned at upper cavity top, two plates 15 tilt to be installed in upper cavity top, its foam of anion surfactant air supporting foaming back floats on the liquid level with air-flow, and be subjected to being pressed through the passage between two plates 15 and flowing into the collection mouth 501 of bubble collecting tube 5 upper ends of plate 15 with the scarp of plate 15, flow in the defoaming devices 6 by collection tube 5 again, the foam that defoaming device 6 is collected regularly incline to.The throw out row of the particulate matter throw out that soil colloid forms bottom upper cavity mouthful 13 discharges, throw out is easier discharges from row's mouth 13 in order to make, and the upper cavity bottom surface is designed to tilt, and throw out row mouth 13 is positioned at lower end.Water-in 1 is positioned on the upper cavity of shell 18.
Electrolyzer 7 is installed in the middle part cavity of shell 18, water is entered in the electrolyzer 7 by pipeline 16 after air-floating apparatus purifies, applied the 20-50V direct current between the positive and negative electrode of electrolyzer 7, cathode-anode plate 701 is made of the aluminium plate, the bottom surface of electrolyzer is processed with the hole 702 (as shown in Figure 2) that precipitation is discharged, and form between the bottom surface of electrolyzer and the end face of lower cavity and make throw out from dope row mouthful 10 passages of discharging, equally, easier for throw out is discharged, the end face of upper cavity also is designed to tilt.Water after electrolyzer 7 purifies enters water purification water tank 9 by rising pipe 17 after by filtration unit 8, the cotton-shaped pollutent that produces in electrolyzer 7 is removed through filtration unit 7, filtration unit 8 adopts the drawer type filter screen, every day is by the drawer type filter screen 8 artificial chlorine tablets of throwing in, to reach the purpose of sterilization.It is standby that water purification is regularly put into storage tank from row's mouthful 11 extractions by pump.

Claims (4)

1. carwash and laundrywastes are handled equipment for reclaiming, comprise shell (18), electrolyzer (7), filtration unit (8), circuit control box (12) and power piping system, described electrolyzer (7) comprises battery lead plate (701), pilot circuit and electrolyzer, circuit control box (12) is installed in the shell (18), it is characterized in that:
A. it also comprises air-floating apparatus, defoaming device (6), bubble collecting tube (5) and plate (15), described air-floating apparatus is by blower fan (3), air duct (14), aeration tube (4) and colloid adsorption unit (2) are formed, aeration tube (4) is installed in the bottom of the upper cavity of shell (18), colloid adsorption unit (2) is installed in the top of the intravital aeration tube of epicoele (4), the two ends of air duct (14) link to each other with aeration tube (4) with blower fan (3) respectively, the collection mouth (501) of bubble collecting tube (5) upper end is positioned at the intravital foam habitat of epicoele, the lower end is connected on the foam defoaming device (6), two plates (15) tilt to be fixed on the intravital top of epicoele, and formation makes foam stream collect the passage of mouthful (501) to foam, the bottom of upper cavity is provided with throw out row mouthful (13), and water-in (1) is positioned on the upper cavity;
B. electrolyzer (7) is installed in the middle part cavity of shell (18), water in the air-floating apparatus (16) by the road enters in the electrolyzer (7), the bottom surface of electrolyzer is processed with the hole (702) that throw out is discharged, and be provided with the passage that throw out is discharged from dope row mouthful (10), filtration unit (8) is installed in the lower cavity of shell (18), the top of rising pipe (17) places the underwater in the electrolyzer (7), the lower end places filtration unit (8), and water purification row mouthful (11) is located on the lower cavity of shell (18).
2. a kind of carwash according to claim 1 and laundrywastes are handled equipment for reclaiming, it is characterized in that: colloid adsorption unit (2) is the colloid biofilm, and this colloid biofilm (2) hangs on the aeration tube (4).
3. a kind of carwash according to claim 1 and laundrywastes are handled equipment for reclaiming, and it is characterized in that: filtration unit (8) is the drawer type filter screen.
4. a kind of carwash according to claim 1 and laundrywastes are handled equipment for reclaiming, and it is characterized in that: battery lead plate (701) is the aluminium plate.
CN 200520036165 2005-11-18 2005-11-18 Processing reuse device for used vehicle and clothes washing water Expired - Fee Related CN2858629Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200520036165 CN2858629Y (en) 2005-11-18 2005-11-18 Processing reuse device for used vehicle and clothes washing water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200520036165 CN2858629Y (en) 2005-11-18 2005-11-18 Processing reuse device for used vehicle and clothes washing water

Publications (1)

Publication Number Publication Date
CN2858629Y true CN2858629Y (en) 2007-01-17

Family

ID=37611488

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200520036165 Expired - Fee Related CN2858629Y (en) 2005-11-18 2005-11-18 Processing reuse device for used vehicle and clothes washing water

Country Status (1)

Country Link
CN (1) CN2858629Y (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103645291A (en) * 2013-12-19 2014-03-19 重庆市渝西水务有限公司 Method for detecting water discharging index of contact tank
CN109205868A (en) * 2018-09-30 2019-01-15 宁波中车时代传感技术有限公司 A kind of vehicle-mounted suspension type device for treatment of high-concentration dirt water
CN110615567A (en) * 2019-10-12 2019-12-27 李德峰 Be used for abluent sewage treatment system of car
CN110872146A (en) * 2018-08-30 2020-03-10 无锡小天鹅电器有限公司 Sewage treatment device and clothes treatment system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103645291A (en) * 2013-12-19 2014-03-19 重庆市渝西水务有限公司 Method for detecting water discharging index of contact tank
CN103645291B (en) * 2013-12-19 2015-05-13 重庆市渝西水务有限公司 Method for detecting water discharging index of contact tank
CN110872146A (en) * 2018-08-30 2020-03-10 无锡小天鹅电器有限公司 Sewage treatment device and clothes treatment system
CN109205868A (en) * 2018-09-30 2019-01-15 宁波中车时代传感技术有限公司 A kind of vehicle-mounted suspension type device for treatment of high-concentration dirt water
CN110615567A (en) * 2019-10-12 2019-12-27 李德峰 Be used for abluent sewage treatment system of car

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