CN202754866U - Device for treating sewage in ceramic factory - Google Patents
Device for treating sewage in ceramic factory Download PDFInfo
- Publication number
- CN202754866U CN202754866U CN 201220436785 CN201220436785U CN202754866U CN 202754866 U CN202754866 U CN 202754866U CN 201220436785 CN201220436785 CN 201220436785 CN 201220436785 U CN201220436785 U CN 201220436785U CN 202754866 U CN202754866 U CN 202754866U
- Authority
- CN
- China
- Prior art keywords
- basin
- sewage
- water
- filtering
- waste disposal
- 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
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- 239000010865 sewage Substances 0.000 title claims abstract description 47
- 239000000919 ceramic Substances 0.000 title claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 51
- 238000005345 coagulation Methods 0.000 claims abstract description 32
- 230000015271 coagulation Effects 0.000 claims abstract description 32
- 238000001914 filtration Methods 0.000 claims abstract description 22
- 238000004140 cleaning Methods 0.000 claims abstract description 14
- 238000004062 sedimentation Methods 0.000 claims abstract description 10
- 239000010802 sludge Substances 0.000 claims abstract description 9
- 239000002699 waste material Substances 0.000 claims description 17
- 239000006228 supernatant Substances 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 239000003245 coal Substances 0.000 claims description 4
- 239000002893 slag Substances 0.000 claims description 4
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 238000005755 formation reaction Methods 0.000 claims description 2
- 238000003756 stirring Methods 0.000 abstract description 5
- 239000002351 wastewater Substances 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 230000001131 transforming Effects 0.000 abstract 1
- 238000001556 precipitation Methods 0.000 description 3
- 235000012970 cakes Nutrition 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000002706 hydrostatic Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000001376 precipitating Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Abstract
The utility model relates to a device for treating sewage in a ceramic factory and belongs to the technical field of sewage treatment equipment. The technical scheme includes that the device comprises a sewage stirring basin, a solution-adding coagulation basin, a sloping plate sedimentation basin, a concentration basin, a filtering basin and a clean water basin, wherein a water inlet of the sewage stirring basin is communicated with a sewage conduit of the factory, the sewage stirring basin is connected with the solution-adding coagulation basin through a hydraulic control sludge pump, the bottom of the solution-adding coagulation basin is communicated with the bottom of the sloping plate sedimentation basin through a pipe, the upper portion of the sloping plate sedimentation basin is communicated with the filtering basin through a pipe, the bottom of the sloping plate sedimentation basin is connected with the concentration basin and a plate-and-frame filter press respectively through plunger pump pipelines, the filtering basin is connected with the clean water basin through a circulating pump, and standard water in the filtering basin returns to a workshop through a circulating pipeline for recycling. The device has the advantages of being simple, small in occupied area, low in investment, convenient to operate, capable of achieving solid-liquid separation for mud-containing wastewater, enabling the sewage to reach the environmental protection standard and achieving recycle of sewage in the ceramic factory, and suitable for transformation of the existing sewage systems of ceramic factories.
Description
Technical field
The utility model relates to the device that a kind of ceramics factory disposes of sewage, and belongs to technical field of sewage treatment equipment.
Background technology
Ceramics factory can produce a large amount of waste water in process of production, need carry out the trade effluent recycling, otherwise contaminate environment not only, what water loss also can be large is surprising.The Sewage treatment systems investment of most ceramics factory is large, floor space is large, it is artificial many to need to use, the effluent cycle utilization ratio is low, and the mud that produces after the sewage disposal needs the labor cleaning, labour intensity is very large, also trouble, time-consuming, effort, inefficiency.
The utility model content
Technical problem to be solved in the utility model provides a kind of ceramics factory waste disposal plant, and this waste disposal plant is simple to operate, investment is little, the solid, liquid that contains mud waste water can be separated, and makes sewage reach environmental protection standard, realizes the recycle of sewage.
The technical scheme that solves the problems of the technologies described above is:
A kind of ceramics factory waste disposal plant, comprise the sewage agitated pool in its formation, the dosing coagulation basin, inclined-plate clarifying basin, concentration basin, filtering basin, clean water basin, the water-in of sewage agitated pool is connected with the plant effuent discharge tube, be connected with hydraulic control sludge pump and transfer line between sewage agitated pool and the dosing coagulation basin, dosing coagulation basin bottom is connected with the inclined-plate clarifying basin bottom by the coagulation water transfer line, the bottom of inclined-plate clarifying basin is connected with concentration basin by concentrated mud siphon pipeline, the water outlet on inclined-plate clarifying basin top has the supernatant water transfer line to be connected with filtering basin, inclined-plate clarifying basin top also has mixed water vacuum primingpump pipeline to be connected with the dosing coagulation basin, filtering basin are connected with clean water basin by recycle pump, and the water outlet of clean water basin connects water circulation pipe up to standard.
Above-mentioned ceramics factory waste disposal plant is equipped with the sewage agitator in the described sewage agitated pool.
Above-mentioned ceramics factory waste disposal plant, the level attitude of described dosing coagulation basin is higher than the sewage agitated pool, and the dosing coagulation basin also has the multifunctional pump pipeline to be connected with concentration basin.
Above-mentioned ceramics factory waste disposal plant is equipped with inclined plate sedimentation device in the described inclined-plate clarifying basin.
Above-mentioned ceramics factory waste disposal plant, described concentration basin links to each other with plate-and-frame filter press by the ram pump pipeline.
Above-mentioned ceramics factory waste disposal plant, described filtering basin inside add the quartzy slag of ￠ 2-3mm and yellow coal.
Usefulness of the present utility model is:
The utility model can carry out sewage pure and impure separation by technological processs such as stirring, dosing, precipitation, concentrated, filtrations, and clear water can recycle, becomes mud cake behind the sludge press filtration, has realized harmless processing and the recycle of sewage.The utility model has remedied the deficiency of common sewage disposal device.The links of sewage disposal is scientific and reasonable, and the sewage recovery utilization rate is high, and floor space is little, need staff number few.Investment of the present utility model is compared with the common Sewage treatment systems of identical scale, but reduce cost 50 ~ 60% has positive promoter action for middle-size and small-size ceramics factory sewage disposal science modernization development.
Description of drawings
Fig. 1 structural representation of the present utility model;
Fig. 2 is the vertical view of Fig. 1;
Fig. 3 piping arrangement schematic diagram of the present utility model;
Fig. 4 is the vertical view of Fig. 3.
Mark is as follows among the figure: plant effuent discharge tube 1, sewage agitated pool 2, sewage agitator 3, hydraulic control sludge pump 4, dosing coagulation basin 5, coagulation water transfer line 6, inclined-plate clarifying basin 7, concentrated mud siphon pipeline 8, plate-and-frame filter press 9, ram pump 10, multifunctional pump 11, supernatant water transfer line 12, water circulation pipe 13 up to standard, inclined plate sedimentation device 14, mixed water vacuum primingpump pipeline 15, concentration basin 16, filtering basin 17, clean water basin 18, recycle pump 19, ram pump pipeline 20, multifunctional pump pipeline 21.
Embodiment
The utility model comprises sewage agitated pool 2, dosing coagulation basin 5, inclined-plate clarifying basin 7, concentration basin 16, filtering basin 17, clean water basin 18.
Show among the figure, structure and the connecting pipeline in above-mentioned each pond are as follows:
The water-in of sewage agitated pool 2 is connected with plant effuent discharge tube 1, and sewage agitator 3 is installed in sewage agitated pool 2.
Be connected with hydraulic control sludge pump 4 and transfer line between sewage agitated pool 2 and the dosing coagulation basin 5, the level attitude of dosing coagulation basin 5 is higher than sewage agitated pool 2.
Dosing coagulation basin 5 bottoms are connected with inclined-plate clarifying basin 7 bottoms by coagulation water transfer line 6, and dosing coagulation basin 5 also has multifunctional pump pipeline 21 to be connected with concentration basin 16.
Inclined plate sedimentation device 14 is installed in the inclined-plate clarifying basin 7, the bottom of inclined-plate clarifying basin 7 is connected with concentration basin 16 by concentrated mud siphon pipeline 8, the water outlet on inclined-plate clarifying basin 7 tops has supernatant water transfer line 12 to be connected with filtering basin 17, and inclined-plate clarifying basin 7 tops also have mixed water vacuum primingpump pipeline 15 to communicate with dosing coagulation basin 5.
Concentration basin 16 links to each other with plate-and-frame filter press 9 by ram pump pipeline 20.
Filtering basin 17 inside add the quartzy slag of ￠ 2-3mm and yellow coal, and filtering basin 17 are connected with clean water basin 18 by recycle pump 19, and the water outlet of clean water basin 18 connects water circulation pipe 13 up to standard.
Show among the figure, workflow of the present utility model is as follows:
The production waste of ceramics factory enters in the sewage agitated pool 2 of waste disposal plant by plant effuent discharge tube 1.Sewage is through the even water quality of abundant stirring and adjusting of sewage agitator 3, and the sewage after the adjusting is lifted in the dosing coagulation basin 5 through hydraulic control sludge pump 4.Waste water adds flocculation agent in coagulation basin, enter inclined-plate clarifying basin 7 bottoms by coagulation water transfer line 6 behind the coagulation, and at the action of gravity middle suspended substance that goes down to dewater, sludge settling is at the bottom of the pond.Inclined-plate clarifying basin 7 is according to the shallow layer precipitating principle, increases the turbulent fluctuation of inclined plate sedimentation device 14 rear minimizing water in the pond, promotes precipitation to make the solids precipitation Distance Shortened, reduces sedimentation time, raises the efficiency.The pool inner water flow velocity V=5mm/s of inclined-plate clarifying basin 7, hydraulic detention time t=0.5h.Inclined-plate clarifying basin 7 bottom mud are discharged into (hydrostatic pressure valve control in the concentration basin 16 through concentrated mud siphon pipeline 8, there is not energy consumption), the top clear water is discharged in the filtering basin 17 by supernatant water transfer line 12, and mixed water promotes back in the dosing coagulation basin 5 by mixed water vacuum primingpump pipeline 15.Concentration basin 16 interior sludge settlings advanced ram pump 10 by the pond bottom tube and are pressed into plate-and-frame filter press 9 after 30 minutes, mud cake outward transport after the press filtration, and the mixed water that concentration basin 16 interior mixed water and pressure filter 9 extrude is in multifunctional pump 11 is got back to dosing coagulation basin 5.Clear water in the filtering basin 17 reaches environmental protection standard through the filtration of quartzy slag and yellow coal, collects in the clean water basin 18 by recycle pump 19, is transported to each workshop of factory through water circulation pipe 13 up to standard and re-uses.
Claims (6)
1. ceramics factory's waste disposal plant, it is characterized in that: comprise sewage agitated pool (2) in its formation, dosing coagulation basin (5), inclined-plate clarifying basin (7), concentration basin (16), filtering basin (17), clean water basin (18), the water-in of sewage agitated pool (2) is connected with plant effuent discharge tube (1), be connected with hydraulic control sludge pump (4) and transfer line between sewage agitated pool (2) and the dosing coagulation basin (5), dosing coagulation basin (5) bottom is connected with inclined-plate clarifying basin (7) bottom by coagulation water transfer line (6), the bottom of inclined-plate clarifying basin (7) is connected with concentration basin (16) by concentrated mud siphon pipeline (8), the water outlet on inclined-plate clarifying basin (7) top has supernatant water transfer line (12) to be connected with filtering basin (17), inclined-plate clarifying basin (7) top also has mixed water vacuum primingpump pipeline (15) to be connected with dosing coagulation basin (5), filtering basin (17) are connected with clean water basin (18) by recycle pump (19), and the water outlet of clean water basin (18) connects water circulation pipe up to standard (13).
2. ceramics factory according to claim 1 waste disposal plant is characterized in that: sewage agitator (3) is installed in the described sewage agitated pool (2).
3. ceramics factory according to claim 2 waste disposal plant, it is characterized in that: the level attitude of described dosing coagulation basin (5) is higher than sewage agitated pool (2), and dosing coagulation basin (5) also has multifunctional pump pipeline (21) to be connected with concentration basin (16).
4. ceramics factory according to claim 3 waste disposal plant is characterized in that: inclined plate sedimentation device (14) is installed in the described inclined-plate clarifying basin (7).
5. ceramics factory according to claim 4 waste disposal plant, it is characterized in that: described concentration basin (16) links to each other with plate-and-frame filter press (9) by ram pump pipeline (20).
6. ceramics factory according to claim 5 waste disposal plant, it is characterized in that: described filtering basin (17) inside adds the quartzy slag of ￠ 2-3mm and yellow coal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220436785 CN202754866U (en) | 2012-08-30 | 2012-08-30 | Device for treating sewage in ceramic factory |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220436785 CN202754866U (en) | 2012-08-30 | 2012-08-30 | Device for treating sewage in ceramic factory |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202754866U true CN202754866U (en) | 2013-02-27 |
Family
ID=47734059
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220436785 Expired - Fee Related CN202754866U (en) | 2012-08-30 | 2012-08-30 | Device for treating sewage in ceramic factory |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202754866U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104384138A (en) * | 2014-11-14 | 2015-03-04 | 重庆海山橡塑化工有限公司 | Waste plastic regeneration cleaning machine |
| CN104384137A (en) * | 2014-11-14 | 2015-03-04 | 重庆海山橡塑化工有限公司 | Waste plastic regeneration cleaning and drying device |
| CN104623932A (en) * | 2014-12-30 | 2015-05-20 | 广东新明珠陶瓷集团有限公司 | Raw material residue wastewater recycling system and recovering method |
| CN104710095A (en) * | 2015-02-04 | 2015-06-17 | 浙江辰鑫机械设备有限公司 | Building mud treatment apparatus |
| CN106396064A (en) * | 2016-11-30 | 2017-02-15 | 恩平市华昌陶瓷有限公司 | Ceramic sewage treating method |
-
2012
- 2012-08-30 CN CN 201220436785 patent/CN202754866U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104384138A (en) * | 2014-11-14 | 2015-03-04 | 重庆海山橡塑化工有限公司 | Waste plastic regeneration cleaning machine |
| CN104384137A (en) * | 2014-11-14 | 2015-03-04 | 重庆海山橡塑化工有限公司 | Waste plastic regeneration cleaning and drying device |
| CN104623932A (en) * | 2014-12-30 | 2015-05-20 | 广东新明珠陶瓷集团有限公司 | Raw material residue wastewater recycling system and recovering method |
| CN104710095A (en) * | 2015-02-04 | 2015-06-17 | 浙江辰鑫机械设备有限公司 | Building mud treatment apparatus |
| CN106396064A (en) * | 2016-11-30 | 2017-02-15 | 恩平市华昌陶瓷有限公司 | Ceramic sewage treating method |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130227 Termination date: 20160830 |