CN201495141U - Glass wastewater treatment integral machine - Google Patents
Glass wastewater treatment integral machine Download PDFInfo
- Publication number
- CN201495141U CN201495141U CN2009203095455U CN200920309545U CN201495141U CN 201495141 U CN201495141 U CN 201495141U CN 2009203095455 U CN2009203095455 U CN 2009203095455U CN 200920309545 U CN200920309545 U CN 200920309545U CN 201495141 U CN201495141 U CN 201495141U
- Authority
- CN
- China
- Prior art keywords
- storehouse
- bin
- air supporting
- clear water
- water
- 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 - Lifetime
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Abstract
The utility model discloses a glass wastewater treatment integral machine which comprises a reaction bin, wherein a dosing device is arranged on the reaction bin; the machine further comprises an air flotation bin and a clean water bin, wherein the air flotation bin is positioned at the downstream of the reaction bin, the clean water bin is positioned at the downstream of the air flotation bin, and partition boards are arranged between two adjacent bins and communicated at the bottom; a water outlet valve is arranged on the clean water bin, and simultaneously, another pipeline is connected with the air flotation bin through a dissolved air vessel; and a releaser is arranged at the lower part of the air flotation bin and connected with the dissolved air vessel through a pipeline. The machine has the advantages of higher efficiency, stability and convenient control.
Description
Technical field
The utility model belongs to environmental technology field, particularly relates to a kind of glass sewage disposal all-in-one.
Background technology
Glass deep processing enterprise is the water resources consumption rich and influential family.Contain a large amount of suspended solids in the sewage that produces, be discharged into river, pond and reservoir after, can cause the water body severe contamination.
The water consumption of glass deep processing industry comprises edging, boring cooling water and bath water mainly at pretreatment process.The water consumption of edge polisher or drilling machine is generally 5m
3/ h is to 10m
3/ h.The water consumption of a washing machine requires different according to the glass cleaning quality, be generally 1.5m
3/ h is to 6m
3/ h.Contain a large amount of glass powder and a spot of grit carborundum, cutting kerosene, washing composition and citric acid in the waste water that pretreatment process produces.
The waste water of glass deep processing enterprise generation at present is not through handling or just adopt simple dosing post precipitation discharging or reuse.The dosing precipitation promptly is to be sprinkled into polymerize aluminum chloride or other flocculation agents by artificial waste water to settling tank, makes the suspended substance generation flco in the waste water sink at the bottom of the pond supernatant liquor discharging or reuse.And because the mud that produces sinks at the bottom of the pond, and cleaning mud needs to stop work, and wastes time and energy, influence is produced.
Summary of the invention
To be solved in the utility model is the technical problem that glass sewage disposal means lack, and a kind of stable performance, highly-efficient treatment is provided, controls the all-in-one of glass sewage disposal easily.
For this reason, the technical solution adopted in the utility model is as follows: glass sewage disposal all-in-one, comprise reaction warehouse, have chemicals dosing plant on the reaction warehouse, it is characterized in that, it also comprises air supporting storehouse, clear water storehouse, the air supporting storehouse is in the reaction warehouse downstream, the clear water storehouse is in downstream, air supporting storehouse, is provided with dividing plate between adjacent two storehouses, and is communicated with in the bottom; The clear water storehouse is provided with outlet valve, has pipeline to link to each other with the air supporting storehouse by dissolving in addition simultaneously; Reliever is arranged at bottom, air supporting storehouse, links to each other with dissolving by pipeline.
As further technical scheme, top, air supporting storehouse is provided with mud scraper, and the bottom is provided with mud drainage slot; Bottom, clear water storehouse also is provided with reverse flow valve.
Further, the outlet valve place in clear water storehouse is provided with turbidometer.
The utility model in use, each workshop Waste Water Centralized enters the equalizing tank that catchments regulate water quality and quantity after, squeeze into reaction warehouse of the present utility model by lift pump, and accurately add coagulating agent, coagulant aids with chemicals dosing plant and form flco, add alkali and regulate PH, fully the reaction back flows into the air supporting storehouse.Owing to adopted efficient reliever, make air under the effect of certain pressure, be dissolved in the water and reach oversaturated state, and then in the air supporting storehouse, reduce to normal pressure suddenly, at this moment be dissolved in the air in the water, just from water, overflow, remove to adhere to the impurity in the water with the form of micro-bubble, cause its overall proportion to float to the water surface, thereby realize solid-liquid separation less than water.The bubble that air-dissolving air-float forms, granularity is very little, and its granularity can adhere to the tiny impurity of particle in the water about about the 1-10 micron.Impurity climbs up on top of the water, and can scrape the outward transport landfill by mud scraper.The clear water of removing impurity can enter the clear water storehouse, and a part enters dissolving and is used to form supersaturated vapor solution, but another part effluent reuse; When turbidometer shows that water outlet can not be up to standard, also can make it get back to equalizing tank by reverse flow valve, handle once again.
Can find out that by above description the utility model is reasonable in design, control is convenient, can handle glass sewage efficiently, and floor space is very little.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Embodiment
Referring to accompanying drawing.Present embodiment comprises reaction warehouse 3, air supporting storehouse 5, and clear water storehouse 10 separates with dividing plate 4 between reaction warehouse 3 and the air supporting storehouse 5, separates with dividing plate 18 between air supporting storehouse 5 and the clear water storehouse 10, and the dividing plate bottom is equipped with groove can be for being communicated with; Have chemicals dosing plant 2 on the reaction warehouse 3; The bottom in air supporting storehouse 5 is provided with efficient reliever 6, and 5 tops, air supporting storehouse are provided with mud scraper 14, and the bottom is provided with mud drainage slot 8, and has valve 7, and air supporting storehouse 5 also is provided with ash pit 13 near dividing plate 18 places; 10 bottoms, clear water storehouse have reverse flow valve 9; Clear water storehouse 10 links to each other with air supporting storehouse 5 by pipeline simultaneously, and pipeline is provided with air dissolved pump 17, dissolving 16, and molten gas relief valve 15 is connected with efficient reliever 6 at last; Clear water storehouse 10 also is provided with outlet valve 12, and outlet valve 12 places have turbidometer 11.
The operational process of present embodiment is such, and sewage enters reaction warehouse 3 by pump 1, and reacts with NaOH, the PAC (polymerize aluminum chloride) that add by chemicals dosing plant 2 and PAM (polyacrylamide) etc.; Then enter air supporting storehouse 5, realize solid-liquid separation by the micro-bubble that efficient reliever 6 produces, the solid that is produced is removed with mud scraper 14 and ash pit 13 at the top on the one hand, removes with mud drainage slot 8 and valve 7 in the bottom on the one hand, and water then enters clear water storehouse 10; Qualified as detecting through turbidometer 11, then most of small portion enters dissolving 16 by outlet valve 12 effluent reuses, forms supersaturated vapor solution with pressurized air, gets back to air supporting storehouse 5 with the formation micro-bubble, thereby constitutes complete reuse technology.Water as the clear water storehouse is defective through turbidometer 11 detections, then can get back to initial point by reverse flow valve 9, handles once more.
As seen, present embodiment control is convenient, and highly-efficient treatment can realize the utility model purpose.
Claims (4)
1. glass sewage disposal all-in-one comprises reaction warehouse, has chemicals dosing plant on the reaction warehouse, it is characterized in that it also comprises air supporting storehouse, clear water storehouse, the air supporting storehouse is in the reaction warehouse downstream, the clear water storehouse is in downstream, air supporting storehouse, is provided with dividing plate between adjacent two storehouses, and is communicated with in the bottom; The clear water storehouse is provided with outlet valve, has pipeline to link to each other with the air supporting storehouse by dissolving in addition simultaneously; Reliever is arranged at bottom, air supporting storehouse, links to each other with dissolving by pipeline.
2. glass sewage disposal all-in-one as claimed in claim 1 is characterized in that: top, air supporting storehouse is provided with mud scraper, and the bottom is provided with mud drainage slot.
3. glass sewage disposal all-in-one as claimed in claim 2 is characterized in that: bottom, clear water storehouse also is provided with reverse flow valve.
4. as each described glass sewage disposal all-in-one of claim 1-3, it is characterized in that: the outlet valve place in clear water storehouse is provided with turbidometer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009203095455U CN201495141U (en) | 2009-09-03 | 2009-09-03 | Glass wastewater treatment integral machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009203095455U CN201495141U (en) | 2009-09-03 | 2009-09-03 | Glass wastewater treatment integral machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201495141U true CN201495141U (en) | 2010-06-02 |
Family
ID=42438349
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009203095455U Expired - Lifetime CN201495141U (en) | 2009-09-03 | 2009-09-03 | Glass wastewater treatment integral machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201495141U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102408144A (en) * | 2011-11-15 | 2012-04-11 | 吴江南玻华东工程玻璃有限公司 | Edge-grinding water treatment system |
| CN102659273A (en) * | 2012-04-11 | 2012-09-12 | 无锡海达安全玻璃有限公司 | Novel glass edging wastewater collection and reuse system |
| CN102910756A (en) * | 2011-07-31 | 2013-02-06 | 浦江儒意水晶环保设备开发有限公司 | Treatment device for glass wastewater |
| CN108946897A (en) * | 2018-08-15 | 2018-12-07 | 安徽科技学院 | A kind of processing method of glass-cutting waste water |
| CN109592872A (en) * | 2018-11-16 | 2019-04-09 | 福建省晋江市净圣环保设备有限责任公司 | A kind of Stacked sludge dewatering machine |
-
2009
- 2009-09-03 CN CN2009203095455U patent/CN201495141U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102910756A (en) * | 2011-07-31 | 2013-02-06 | 浦江儒意水晶环保设备开发有限公司 | Treatment device for glass wastewater |
| CN102910756B (en) * | 2011-07-31 | 2014-09-03 | 浦江儒意水晶环保设备开发有限公司 | Treatment device for glass wastewater |
| CN102408144A (en) * | 2011-11-15 | 2012-04-11 | 吴江南玻华东工程玻璃有限公司 | Edge-grinding water treatment system |
| CN102659273A (en) * | 2012-04-11 | 2012-09-12 | 无锡海达安全玻璃有限公司 | Novel glass edging wastewater collection and reuse system |
| CN108946897A (en) * | 2018-08-15 | 2018-12-07 | 安徽科技学院 | A kind of processing method of glass-cutting waste water |
| CN109592872A (en) * | 2018-11-16 | 2019-04-09 | 福建省晋江市净圣环保设备有限责任公司 | A kind of Stacked sludge dewatering machine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Hangzhou Huishui Technology Co., Ltd. Assignor: Wang Wanshou Contract record no.: 2010330001956 Denomination of utility model: Glass wastewater treatment integral machine Granted publication date: 20100602 License type: Exclusive License Record date: 20100926 |
|
| ASS | Succession or assignment of patent right |
Owner name: HANGZHOU HUISHUI TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: WANG WANSHOU Effective date: 20120203 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20120203 Address after: Hangzhou City, Zhejiang province Binjiang District 310052 shore road 1180 No. 2 building 106-110 Patentee after: Hangzhou Huishui Technology Co., Ltd. Address before: 310052 Yao Xing building, 518 Jiangnan Avenue, Hangzhou, Zhejiang, 13-4, Binjiang District Patentee before: Wang Wanshou |
|
| CX01 | Expiry of patent term |
Granted publication date: 20100602 |
|
| CX01 | Expiry of patent term |