CN202358976U - Glass wastewater treatment equipment - Google Patents
Glass wastewater treatment equipment Download PDFInfo
- Publication number
- CN202358976U CN202358976U CN201120426018XU CN201120426018U CN202358976U CN 202358976 U CN202358976 U CN 202358976U CN 201120426018X U CN201120426018X U CN 201120426018XU CN 201120426018 U CN201120426018 U CN 201120426018U CN 202358976 U CN202358976 U CN 202358976U
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- treatment equipment
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Abstract
The utility model discloses glass wastewater treatment equipment, which relates to the field of environment protection projects and comprises a glass wastewater purifying system and a recycled water reusing system. In the glass wastewater purifying system, glass wastewater flows through a regulating tank, a reaction tank, a settling tank, a middle tank, a filter, an ultrafiltration device, an ultrafiltration water tank, a reverse osmosis device and a reverse osmosis water tank sequentially to be purified and enter a purified water tank. In the recycled water reusing system, the middle tank, the reverse osmosis water tank and the purified water tank are respectively provided with a recycled water reusing pump outside. The glass wastewater treatment equipment can be used for thoroughly purifying glass wastewater while reusing recycled water during glass wastewater treatment.
Description
Technical field
The utility model relates to field of environmental engineering, particularly a kind of glass sewage treatment equipment.
Background technology
Along with the aggravation of problem of environmental pollution and shortage of water resources problem, People more and more is recognized protection environment and water-saving importance.In the glass production process, can produce a large amount of waste water, if these waste water directly discharges, will cause the serious environmental pollution, the while is also caused a large amount of wastes of water resources, therefore, is enterprise's obligation one can't decline to the purification and the recycling of glass waste water.
Development along with technology; Glass industry has produced the glass sewage treatment equipment gradually; In the treating processes of existing glass sewage treatment equipment, on the one hand, glass waste water discharges behind equalizing tank, reaction tank and settling tank; On the other hand, the mud of settling tank is transported outward behind sludge thickener and pressure filter.Yet; In the treating processes of this kind glass sewage treatment equipment,, also contain suspended impurities such as suspended particulates, colloid, mikrobe owing to only do not contain mud in the glass waste water; And settling tank only can be handled the impurity that this type of mud sinks easily; Then do not have effect for impurity such as suspended particulates, colloid, mikrobes, therefore, the waste water that behind settling tank, discharges still can cause environmental pollution; Moreover, because the water after the existing glass sewage treatment equipment processing directly discharges, do not recycle, therefore cause a large amount of wastes of water resources, do not reach the aim of environmental requirement energy-saving and emission-reduction.
The utility model content
The technical problem that the utility model will solve is to above-mentioned deficiency of the prior art, and a kind of glass sewage treatment equipment is provided, and this glass sewage treatment equipment is not only thorough to the glass purification of waste water, and the water in handling glass waste water process can be adjusted back utilization.
The technical scheme of the utility model is: a kind of glass sewage treatment equipment, comprise glass waste water purification system and intermediate water reuse system, wherein:
The glass waste water purification system, in this glass waste water purification system, glass waste water is purified behind equalizing tank, reaction tank, settling tank, middle pond, strainer, ultra-filtration equipment, ultrafiltration pond, reverse osmosis unit, r-o-pond successively and arrives the pure water case;
Intermediate water reuse system, the water pump of water reuse in the middle of said, being respectively equipped with outside pond, r-o-pond and the pure water case.
Said settling tank connects sludge treating system; In sludge treating system, set gradually sludge sump, sludge pump and pressure filter, after this sludge sump receives the mud at the bottom of the said settling tank pond, extract the arrival pressure filter through sludge pump; In pressure filter, the solid of mud and liquid separation.Said settling tank has the tipping bucket structure at the bottom of the pond, and said sludge sump is communicated with the tipping bucket bottom of settling tank through sludge pipe.
Said pressure filter is equipped with outward to the recoil pump that carries out water slug in the pressure filter and to adding the chemicals dosing plant of spice in the pressure filter.
In the said equalizing tank aerating apparatus is installed.
Said reaction tank is equipped with the chemicals dosing plant that in reaction tank, adds spice outward, and whipping appts is installed in the reaction tank.
Said reaction tank is provided with three covers; Be respectively acid-alkali accommodation reaction tank, PAC inorganic salt coagulating agent reaction tank and PAM polymeric flocculant reaction tank, glass waste water gets into settling tank successively behind acid-alkali accommodation reaction tank, PAC inorganic salt coagulating agent reaction tank and PAM polymeric flocculant reaction tank.
Be provided with ultraviolet sterilization apparatus between said reverse osmosis unit and the r-o-pond.
Be provided with ultraviolet sterilization apparatus between said reverse osmosis unit and the pure water case.
Said reverse osmosis unit is provided with two covers, is respectively first-stage reverse osmosis device and two-pass reverse osmosis device.
The beneficial effect of the utility model is: because in the glass waste water purification system of the utility model; Glass waste water is purified behind equalizing tank, reaction tank, settling tank, middle pond, strainer, ultra-filtration equipment, ultrafiltration pond, reverse osmosis unit, r-o-pond successively and arrives the pure water case; Therefore; Glass waste water can be purified completely, and the water that emits from the pure water case can not cause environmental pollution; Because the utility model is provided with intermediate water reuse system; The water pump of water reuse in the middle of said, being respectively equipped with outside pond, r-o-pond and the pure water case; Therefore; The water of pond, r-o-pond and pure water case to be making production usefulness in the middle of can transferring according to production plant different production needs, thereby practices thrift great lot of water resources and production cost expense.
Description of drawings
Fig. 1 is the one-piece construction synoptic diagram of the utility model.
Among the figure: 1. equalizing tank; 2. reaction tank; 3. settling tank; 4. middle pond; 5. strainer; 6. ultra-filtration equipment; 7. ultrafiltration pond; 8. reverse osmosis unit; 9. r-o-pond; 10. pure water case; 11. water pump; 12. water pump; 13. water pump; 14. sludge sump; 15. sludge pump; 16. pressure filter; 17. aerating apparatus; 18. chemicals dosing plant; 19. whipping appts; 20. acid-alkali accommodation reaction tank; 21.PAC inorganic salt coagulating agent reaction tank; 22.PAM polymeric flocculant reaction tank; 23.PH value test rod; 24. tipping bucket; 25. ultraviolet sterilization apparatus; 26. ultraviolet sterilization apparatus; 27. recoil pump; 28. chemicals dosing plant; A. glass waste water; B. mud; C. plant area's tap water; D. plant area's pressurized air; E. filter mud cake; F. filtrate.
Embodiment
Below in conjunction with accompanying drawing the structural principle and the principle of work of the utility model are done further explain.
As shown in Figure 1, the utility model is a kind of glass sewage treatment equipment, comprises glass waste water purification system, intermediate water reuse system and sludge treating system, wherein:
The glass waste water purification system; In said glass waste water purification system, the glass waste water A is purified behind equalizing tank 1, reaction tank 2, settling tank 3, middle pond 4, strainer 5, ultra-filtration equipment 6, ultrafiltration pond 7, reverse osmosis unit 8, r-o-pond 9 successively and arrives pure water case 10.
Intermediate water reuse system, the water pump (11,12,13) of water reuse in the middle of said, being respectively equipped with outside pond 4, r-o-pond 8 and the pure water case 10;
Sludge treating system; This sludge treating system sets gradually sludge sump 14, sludge pump 15 and pressure filter 16, and this sludge sump 14 extracts arrival pressure filter 16 through sludge pump 15 after receiving the mud at the bottom of said settling tank 3 ponds; In pressure filter 16, the solid of mud and liquid separation.
The workflow of each part mentioned above is:
1. equalizing tank 1: equalizing tank 1 is regulated the glass waste water A and is collected homogeneous; Aerating apparatus 17 is installed in the equalizing tank 1; Prevent glass powder gathering caking; Aerating apparatus 17 can be designed to the structure that aerated conduit stretches into equalizing tank 1 bottom, in aerated conduit, imports pressurized gas through the pressurized air D of plant area and realizes aeration.
2. reaction tank 2: the reaction tank 2 outer chemicals dosing plants 18 that in reaction tank 2, add spice that are equipped with are equipped with whipping appts 19 in the reaction tank 2.Chemicals dosing plant 18 is sent in the reaction tank 2 after the tap water C of plant area is mixed with spice, and whipping appts 19 mixes and produce reaction with spice and glass waste water A again.Further, aerating apparatus (identical with the aerating apparatus structure in the equalizing tank) is installed in the chemicals dosing plant 18, the spice that is beneficial in the chemicals dosing plant 18 mixes with the tap water C of plant area, and whipping appts 19 can be designed to driven by step-down gear the structure of agitator arm rotation.
As optimal way to reaction tank 2; Reaction tank 2 is provided with three covers; Be respectively acid-alkali accommodation reaction tank 20, PAC inorganic salt coagulating agent reaction tank 21 and PAM polymeric flocculant reaction tank 22, the glass waste water A gets into settling tank 4 successively behind acid-alkali accommodation reaction tank 20, PAC inorganic salt coagulating agent reaction tank 21 and PAM polymeric flocculant reaction tank 22.For the potential of hydrogen of real time inspection acid-alkali accommodation reaction tank 20, pH value test rod 23 can be installed in acid-alkali accommodation reaction tank 20.Utilize the flocculation function of PAC, PAM; Organic outstanding absurd creature in the water and mud liquid are mixed into mud and precipitate; Thereby reach the purpose of removal; And the filter effect through sand removes solid particulate more tiny in the water outlet and is suspended in the minute impurities in the water with other, thereby its filtration, purification function to water inlet is strengthened greatly, improved the water quality condition of water outlet.
3. settling tank 3: settling tank 3 is for species precipitate provides the place, and material has enough STs in settling tank 3, makes solid particulate matter and part suspended substance to precipitate.Have tipping bucket 24 structures at the bottom of settling tank 3 ponds, make mud obtain enrichment in tipping bucket 24 bottoms.
4. middle pond 4: middle pond 4 is places that settling tank 3 water outlets store and place, and a part of water that stores in the middle pond 4 directly is delivered to the glass production workshop through water pump 11, can supply the glass edge-grinding machine (not shown) of production plant to use.
5. strainer 5: the water in middle pond 4 can filter out partial impurities behind strainer 5.
6. ultra-filtration equipment 6: the ultrafiltration membrane system of ultra-filtration equipment 6 can be used for removing suspended particulates in the water, colloid, mikrobe etc.Water molecules and small-molecule substance see through ultra-filtration membrane under the effect of hydraulic pressure, and the suspended particulates in the water, colloid, mikrobe etc. then are trapped within the internal surface of ultra-filtration membrane.Because the micropore on the ultra-filtration membrane is very little; Can remove suspended particle, colloid, bacterium and larger molecular organics etc. in the various water effectively; These are held back material and may gather at the internal surface of film, so need carry out regular back flushing and dosing is cleaned to hyperfiltration membrane assembly.
7. the ultrafiltration pond 7: ultrafiltration pond 7 is places that ultra-filtration equipment 6 ultrafiltration water outlets store and place.
8. reverse osmosis unit 8: reverse osmosis unit utilizes the pressurization of HPP, and holding back of membrane technique molecule can separate water in the solution, and liquid concentrator is discharged with solute.
Reverse osmosis process is to utilize semipermeability spiral wound membrane sepn to remove soluble solids, organism, colloidalmaterial and bacterium in the water.Former water is sent to certain pressure and through reverse osmosis membrane, water sees through the micro-holes on the film, obtains pure water after the collection.Impurity in the water concentrates in current-carrying liquid and is removed.Reverse osmosis unit can be removed the soluble solid more than 95% in the water into, organism more than 99% and colloid, almost 100% bacterium.Reverse osmosis unit is to produce one of state-of-the-art equipment of pure water in the water treating equipment in the world at present, and its working cost is low, economical, easy to operate, reliable, is the first-selected equipment of producing pure water of businessman.The throughput of reverse osmosis unit is in the value of former water under 25 ℃, standard production situation.The change of water temperature and working condition all will influence the throughput of equipment.
9. the r-o-pond 9: r-o-pond 9 is places that reverse osmosis unit 8 r-o-water outlets store and place.The a part of water that stores in the r-o-pond 9 directly is delivered to the glass production workshop through water pump 12, can supply the cleaning machine (not shown) of production plant to use.
10. the pure water case 10: the institute of the storage after the glass waste water A of pure water case 10 is purified, a part of water that store in the pure water case 10 directly are delivered to the glass production workshop through water pump 13, can supply the packing cleaning machine (not shown) of production plant to use.
Further preferred as between reverse osmosis unit 8, r-o-pond 9 and the pure water case 10, said reverse osmosis unit 8 is provided with two covers, is respectively first-stage reverse osmosis device and two-pass reverse osmosis device.After the glass waste water A gets into the first-stage reverse osmosis device, behind r-o-pond 9, two-pass reverse osmosis device, get into pure water case 10.Further again, be provided with ultraviolet sterilization apparatus between said reverse osmosis unit and the r-o-pond; Be provided with ultraviolet sterilization apparatus between said reverse osmosis unit and the pure water case.
11. sludge sump 14: sludge sump 14 is communicated with tipping bucket 24 bottoms of settling tank 3 through sludge pipe.
12. sludge pump 15: sludge pump 15 is sent to pressure filter 16 with the mud in the sludge sump 14.
13. pressure filter 16: pressure filter 16 is used for separating of solid and liquid.Sludge stream is through filtration medium (like filter cloth), and solid rests on the filter cloth, and on filter cloth, piles up gradually to form and filter mud cake E, and filtrating F part then penetrates filter cloth, becomes not contain solid filtrating F.Filtration mud cake E transports and gets final product, and filtrating F then sends equalizing tank 1 again back to.
Pressure filter 16 is equipped with outward to the recoil pump 27 that carries out water slug in the pressure filter 16 and to adding the chemicals dosing plants 28 of spices in the pressure filter 16.Like this, pressure filter 16 can in time be cleaned after work for some time, and rerun.Recoil pump 27 can draw water to impacting in the pressure filter 16 in middle pond, and the structure of chemicals dosing plant 28 is identical with the chemicals dosing plant structure of reaction tank 2.
The above only is the utility model preferred embodiments, and every any trickle modification, equivalent variations and modification of above embodiment being done according to the technical scheme of the utility model all belongs in the scope of the utility model technical scheme.
Claims (10)
1. glass sewage treatment equipment is characterized in that: comprise glass waste water purification system and intermediate water reuse system, wherein:
The glass waste water purification system, in this glass waste water purification system, glass waste water is purified behind equalizing tank, reaction tank, settling tank, middle pond, strainer, ultra-filtration equipment, ultrafiltration pond, reverse osmosis unit, r-o-pond successively and arrives the pure water case;
Intermediate water reuse system, the water pump of water reuse in the middle of said, being respectively equipped with outside pond, r-o-pond and the pure water case.
2. glass sewage treatment equipment according to claim 1; It is characterized in that: said settling tank connects sludge treating system; In sludge treating system, set gradually sludge sump, sludge pump and pressure filter, after this sludge sump receives the mud at the bottom of the said settling tank pond, extract the arrival pressure filter through sludge pump; In pressure filter, the solid of mud and liquid separation.
3. glass sewage treatment equipment according to claim 2 is characterized in that: said settling tank has the tipping bucket structure at the bottom of the pond, and said sludge sump is communicated with the tipping bucket bottom of settling tank through sludge pipe.
4. glass sewage treatment equipment according to claim 2 is characterized in that: said pressure filter is equipped with outward to the recoil pump that carries out water slug in the pressure filter and to adding the chemicals dosing plant of spice in the pressure filter.
5. glass sewage treatment equipment according to claim 1 is characterized in that: in the said equalizing tank aerating apparatus is installed.
6. glass sewage treatment equipment according to claim 1 is characterized in that: said reaction tank is equipped with the chemicals dosing plant that in reaction tank, adds spice outward, and whipping appts is installed in the reaction tank.
7. glass sewage treatment equipment according to claim 1; It is characterized in that: said reaction tank is provided with three covers; Be respectively acid-alkali accommodation reaction tank, PAC inorganic salt coagulating agent reaction tank and PAM polymeric flocculant reaction tank, glass waste water gets into settling tank successively behind acid-alkali accommodation reaction tank, PAC inorganic salt coagulating agent reaction tank and PAM polymeric flocculant reaction tank.
8. glass sewage treatment equipment according to claim 1 is characterized in that: be provided with ultraviolet sterilization apparatus between said reverse osmosis unit and the r-o-pond.
9. glass sewage treatment equipment according to claim 1 is characterized in that: be provided with ultraviolet sterilization apparatus between said reverse osmosis unit and the pure water case.
10. glass sewage treatment equipment according to claim 1 is characterized in that: said reverse osmosis unit is provided with two covers, is respectively first-stage reverse osmosis device and two-pass reverse osmosis device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120426018XU CN202358976U (en) | 2011-11-01 | 2011-11-01 | Glass wastewater treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120426018XU CN202358976U (en) | 2011-11-01 | 2011-11-01 | Glass wastewater treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202358976U true CN202358976U (en) | 2012-08-01 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201120426018XU Expired - Fee Related CN202358976U (en) | 2011-11-01 | 2011-11-01 | Glass wastewater treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202358976U (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102992519A (en) * | 2012-11-27 | 2013-03-27 | 常州大学 | Industrial sewage treatment device |
| CN103739110A (en) * | 2013-11-15 | 2014-04-23 | 安徽省绿巨人环境技术有限公司 | Glassware processing wastewater treatment technology |
| CN105621763A (en) * | 2014-11-26 | 2016-06-01 | 成都锦汇科技有限公司 | System for recovering acid and alkali from glass production sewage |
| CN105621773A (en) * | 2014-11-26 | 2016-06-01 | 成都锦汇科技有限公司 | System for recovering acid and alkali from glass production sewage |
| CN105692980A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | Recovery system for recovering acid and base from glass production wastewater |
| CN105692987A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | Recovery system for recovering acid and base from glass production wastewater |
| CN105692988A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | System for recovering acid and base from glass production wastewater |
| CN105712532A (en) * | 2016-02-02 | 2016-06-29 | 湖南景翌湘台环保高新技术开发有限公司 | Window glass processing wastewater treatment and reuse technology |
| CN105712528A (en) * | 2016-01-26 | 2016-06-29 | 中建材（合肥）新能源有限公司 | Photovoltaic glass deep processing cooling water recycling method |
| CN105899466A (en) * | 2013-12-02 | 2016-08-24 | 拉普兰塔理工大学 | A wastewater purification system |
| CN107473471A (en) * | 2017-09-18 | 2017-12-15 | 成都恒力达科技有限公司 | A kind of sewage purifying and treating device |
| CN109956601A (en) * | 2019-04-25 | 2019-07-02 | 浙江嘉福玻璃有限公司 | A kind of coated glass production wastewater recycling process and recyclable device |
| CN110950413A (en) * | 2019-12-17 | 2020-04-03 | 江门市豪睿环保节能科技有限公司 | Full-automatic intelligent sewage treatment system |
| CN115321711A (en) * | 2022-08-25 | 2022-11-11 | 河南能源化工集团鹤壁煤化工有限公司 | Chemical wastewater treatment and recycling device and using method thereof |
-
2011
- 2011-11-01 CN CN201120426018XU patent/CN202358976U/en not_active Expired - Fee Related
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102992519A (en) * | 2012-11-27 | 2013-03-27 | 常州大学 | Industrial sewage treatment device |
| CN103739110A (en) * | 2013-11-15 | 2014-04-23 | 安徽省绿巨人环境技术有限公司 | Glassware processing wastewater treatment technology |
| CN105899466A (en) * | 2013-12-02 | 2016-08-24 | 拉普兰塔理工大学 | A wastewater purification system |
| CN105621763A (en) * | 2014-11-26 | 2016-06-01 | 成都锦汇科技有限公司 | System for recovering acid and alkali from glass production sewage |
| CN105621773A (en) * | 2014-11-26 | 2016-06-01 | 成都锦汇科技有限公司 | System for recovering acid and alkali from glass production sewage |
| CN105692980A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | Recovery system for recovering acid and base from glass production wastewater |
| CN105692987A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | Recovery system for recovering acid and base from glass production wastewater |
| CN105692988A (en) * | 2014-11-26 | 2016-06-22 | 成都锦汇科技有限公司 | System for recovering acid and base from glass production wastewater |
| CN105712528A (en) * | 2016-01-26 | 2016-06-29 | 中建材（合肥）新能源有限公司 | Photovoltaic glass deep processing cooling water recycling method |
| CN105712532A (en) * | 2016-02-02 | 2016-06-29 | 湖南景翌湘台环保高新技术开发有限公司 | Window glass processing wastewater treatment and reuse technology |
| CN107473471A (en) * | 2017-09-18 | 2017-12-15 | 成都恒力达科技有限公司 | A kind of sewage purifying and treating device |
| CN107473471B (en) * | 2017-09-18 | 2021-01-15 | 福建省福清市诺华水务有限公司 | Sewage purification treatment device |
| CN109956601A (en) * | 2019-04-25 | 2019-07-02 | 浙江嘉福玻璃有限公司 | A kind of coated glass production wastewater recycling process and recyclable device |
| CN109956601B (en) * | 2019-04-25 | 2023-11-07 | 浙江嘉福玻璃有限公司 | Coated glass production wastewater recovery process and recovery device |
| CN110950413A (en) * | 2019-12-17 | 2020-04-03 | 江门市豪睿环保节能科技有限公司 | Full-automatic intelligent sewage treatment system |
| CN115321711A (en) * | 2022-08-25 | 2022-11-11 | 河南能源化工集团鹤壁煤化工有限公司 | Chemical wastewater treatment and recycling device and using method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120801 Termination date: 20121101 |