CN202705147U - Flotation workshop waste water treatment system - Google Patents
Flotation workshop waste water treatment system Download PDFInfo
- Publication number
- CN202705147U CN202705147U CN 201220388410 CN201220388410U CN202705147U CN 202705147 U CN202705147 U CN 202705147U CN 201220388410 CN201220388410 CN 201220388410 CN 201220388410 U CN201220388410 U CN 201220388410U CN 202705147 U CN202705147 U CN 202705147U
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- pond
- waste water
- water treatment
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- workshop waste
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Abstract
The utility model provides a flotation workshop waste water treatment system which is little in investment and good in processing effect. The flotation workshop waste water treatment system comprises a primary setting pond, a concrete flocculation pond, a sediment pond, a sand leaching water pond, a resin attaching system, a bentonite attaching system and a recycling water pond, and the primary setting pond, the concrete flocculation pond, the sediment pond, the sand leaching water pond, the resin attaching system, the bentonite attaching system and the recycling water pond are connected in sequence. Analytical solution outlets of the resin attaching system and the bentonite attaching system are connected with a regulating pond, the regulating pond is connected with an oxidation system, and the oxidation system is connected with a transition pond. The flotation workshop waste water treatment system has the advantages of being little in investment, simple, stable, economic and practical, and the like. Not only is processing effect ensured, but also investment and operating management cost are saved.
Description
Technical field
The utility model relates to a kind of Waste Water Treatment, especially a kind of flotation workshop Waste Water Treatment.
Background technology
The principal pollutant matter of flotation workshop waste discharge comprises suspended substance, organism etc., and existing Waste Water Treatment treatment effect is bad, can not reach the discharge water standard; And there are high, the shortcomings such as working cost is high, inconvenient operation of investment.
The utility model content
The purpose of this utility model provides a kind of less investment, flotation workshop Waste Water Treatment that treatment effect is good.
Realize the flotation workshop Waste Water Treatment of the utility model purpose, comprise the preliminary sedimentation tank, coagulation-flocculation pond, settling tank, Sand Filtration System, intermediate pool, resin absorption system, wilkinite adsorption system and the reuse pool that link to each other successively; Described resin absorption system is connected the desorbed solution outlet and connects equalizing tank with the wilkinite adsorption system, described equalizing tank connects oxidation system, and described oxidation system connects the transition pond.
The sludge outlet of described settling tank connects sludge sump, and the liquid outlet of described sludge sump connects preliminary sedimentation tank.
The beneficial effects of the utility model are as follows: flotation of the present utility model workshop Waste Water Treatment, less investment, simple, ripe, stable, practical, economical and practical had both guaranteed treatment effect, reduced investment outlay again and operational and administrative expenses.
Description of drawings
Fig. 1 is the functional block diagram of flotation of the present utility model workshop Waste Water Treatment.
Embodiment
Embodiment of the present utility model is as follows: as shown in Figure 1, flotation of the present utility model workshop Waste Water Treatment comprises the preliminary sedimentation tank, coagulation-flocculation pond, settling tank, Sand Filtration System, intermediate pool, resin absorption system, wilkinite adsorption system and the reuse pool that link to each other successively; Described resin absorption system is connected the desorbed solution outlet and connects equalizing tank with the wilkinite adsorption system, described equalizing tank connects oxidation system, and described oxidation system connects the transition pond.
The sludge outlet of described settling tank connects sludge sump, and the liquid outlet of described sludge sump connects preliminary sedimentation tank.
The principle of work of flotation of the present utility model workshop Waste Water Treatment is as follows: waste water is flowed through first on the preliminary sedimentation tank, precipitation is removed the macrobead suspended substance in the waste water under action of gravitation, utilize original water pump quantitatively to promote and flow to coagulation basin, through the quantitative dosing coagulant of dosing pump, make the neutral charge of pollutent colloid destroyed, thereby make it to be aggregated into larger small-particle.Quantitatively add flocculation agent by pump again, make that flocculation agent and waste particles thing are built bridge, the net effect of catching makes fine particle become the macrobead of easy precipitation.Form oarse-grained waste water and enter into settling tank, waste water flow to settling tank carry out mud, moisture from, clear liquor in the settling tank flows in the Sand Filtration System, filter by Sand Filtration System, further remove the suspended particulate in the waste water, to satisfy the subsequent disposal system requirements, the Sand Filtration System backwash water is discharged to preliminary sedimentation tank through pump and again processes.
Waste water flows to intermediate pool after filtering, pass through respectively the organism in resin absorption system and the wilkinite adsorption system two-stage Adsorption waste water under the lifting of pump, makes waste water can reach the reuse requirement.
Mud in the settling tank is discharged to sludge sump be deposited to the pond under action of gravitation at the bottom of under the effect of sludge pump, the mud in the sludge sump is discharged in the preliminary sedimentation tank under the effect of sludge pump after concentrated.
The stripping liquid that produces in resin absorption and the wilkinite adsorption-desorption process flows to equalizing tank, quantitatively adds medicament by dosing pump, generates the material of strong oxidizing property, generates organic free radical with hardly degraded organic substance and make it structure deteriorate in waste water, final oxygenolysis.Waste water after the oxygenolysis flows to the transition pond through overregulating pH, is discharged to Tailings Dam under the effect of pump.
Embodiment recited above is described preferred implementation of the present utility model; be not that scope of the present utility model is limited; design under the spiritual prerequisite not breaking away from the utility model; various distortion and improvement that the common engineering technical personnel in this area make technical solutions of the utility model all should fall in the definite protection domain of claims of the present utility model.
Claims (2)
1. a flotation workshop Waste Water Treatment is characterized in that: comprise the preliminary sedimentation tank, coagulation-flocculation pond, settling tank, Sand Filtration System, intermediate pool, resin absorption system, wilkinite adsorption system and the reuse pool that link to each other successively; Described resin absorption system is connected the desorbed solution outlet and connects equalizing tank with the wilkinite adsorption system, described equalizing tank connects oxidation system, and described oxidation system connects the transition pond.
2. flotation according to claim 1 workshop Waste Water Treatment, it is characterized in that: the sludge outlet of described settling tank connects sludge sump, and the liquid outlet of described sludge sump connects preliminary sedimentation tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220388410 CN202705147U (en) | 2012-08-07 | 2012-08-07 | Flotation workshop waste water treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220388410 CN202705147U (en) | 2012-08-07 | 2012-08-07 | Flotation workshop waste water treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202705147U true CN202705147U (en) | 2013-01-30 |
Family
ID=47585470
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220388410 Expired - Fee Related CN202705147U (en) | 2012-08-07 | 2012-08-07 | Flotation workshop waste water treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202705147U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103553243A (en) * | 2013-11-14 | 2014-02-05 | 安徽省绿巨人环境技术有限公司 | Boiler exhaust gas and wastewater treatment technology |
| CN104176854A (en) * | 2014-08-21 | 2014-12-03 | 营口东吉科技（集团）有限公司 | Method for utilizing mineral separation backwater in magnesite reverse flotation desilicification |
-
2012
- 2012-08-07 CN CN 201220388410 patent/CN202705147U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103553243A (en) * | 2013-11-14 | 2014-02-05 | 安徽省绿巨人环境技术有限公司 | Boiler exhaust gas and wastewater treatment technology |
| CN104176854A (en) * | 2014-08-21 | 2014-12-03 | 营口东吉科技（集团）有限公司 | Method for utilizing mineral separation backwater in magnesite reverse flotation desilicification |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130130 Termination date: 20140807 |
|
| EXPY | Termination of patent right or utility model |