CN203694759U - Ceramic wastewater treatment device - Google Patents
Ceramic wastewater treatment device Download PDFInfo
- Publication number
- CN203694759U CN203694759U CN201320885936.8U CN201320885936U CN203694759U CN 203694759 U CN203694759 U CN 203694759U CN 201320885936 U CN201320885936 U CN 201320885936U CN 203694759 U CN203694759 U CN 203694759U
- Authority
- CN
- China
- Prior art keywords
- efficiency
- wastewater
- waste water
- precision
- valve
- 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
Links
- 239000000919 ceramic Substances 0.000 title claims abstract description 22
- 238000004065 wastewater treatment Methods 0.000 title abstract description 7
- 239000002351 wastewater Substances 0.000 claims abstract description 56
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 230000008676 import Effects 0.000 claims description 10
- 239000010802 sludge Substances 0.000 abstract 2
- 238000004069 wastewater sedimentation Methods 0.000 abstract 2
- 238000012856 packing Methods 0.000 description 7
- 238000001914 filtration Methods 0.000 description 6
- 239000012535 impurity Substances 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 239000000084 colloidal system Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000004062 sedimentation Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000013459 approach Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 235000001674 Agaricus brunnescens Nutrition 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 159000000013 aluminium salts Chemical class 0.000 description 1
- 229910000329 aluminium sulfate Inorganic materials 0.000 description 1
- 238000000498 ball milling Methods 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000007688 edging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 230000002262 irrigation Effects 0.000 description 1
- 238000003973 irrigation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Filtering Materials (AREA)
Abstract
The utility model discloses a ceramic wastewater treatment device. The ceramic wastewater treatment device is characterized by comprising a wastewater sedimentation tank, a wastewater pump, more than two sets of high-efficiency precise treaters, a sludge tank and a clean water tank, wherein the wastewater sedimentation tank is sequentially connected to the wastewater pump, a water pipe, one valve ports of wastewater three-way valves connected to wastewater inlets, of the more than two sets of high-efficiency precise treaters, and the wastewater inlets of the more than two sets of high-efficiency precise treaters, clear water outlets with three-way valves of the more than two sets of high-efficiency precise treaters are connected to the clean water tank through one valve ports of the three-way valves and a pipeline, another valve ports of the three-way valves of the clean water outlets of the more than two sets of high-efficiency precise treaters are connected through pipelines, and the another valve ports of the wastewater three-way valves of the more than two sets of high-efficiency precise treaters, which are connected to the wastewater inlets, are connected to the sludge tank. Compared with the prior art, the ceramic wastewater treatment device has the advantage of rapidly and reliably purifying ceramic wastewater at high efficiency.
Description
Technical field:
The utility model relates to a kind of wastewater treatment equipment.
Background technology:
Ceramic industry waste water mainly results from the operations such as ball milling (washing ball) in production process, canvas press cloth cleaning, glazing (cleaning), spraying are dry, edging polishing, when ground dust is by rain drop erosion in raw material transports unrestrained and factory in addition, also bring certain high turbidity, high suspended matter waste water, although this type of concentration of organic wastewater is lower, but in each operation production process, partial material enters in water, cause more than Treating Suspended Matters in Water Drained mass concentration reaches as high as 5000mg/L, belong to high turbidity factory effluent.In waste water, part suspended particle is very little, and the suspension in waste water is mainly that the solid particle ratio of particle diameter < 150 μ m is very large, approaches the diameter of colloid ion, sedimentation separation difficulty, need to be in medicine flocculation situation could rapid subsidence.Once and sedimentation, because suspended particulate mostly is inorganic particulate, deposit moisture content is low, poor fluidity, particularly in the structures generation sedimentation alluvial of wastewater treatment, brings many difficulties to cleaning.Because each ceramics factory managerial skills differ greatly, workshop layout and even drainage pipeline, the gradient of irrigation canals and ditches, length difference, causes the concentration of suspension of total discharge outlet ceramic wastewater of each factory to be commonly 1000～1 × 10
4mg/L left and right, silts pipeline up, and polluted-water must be administered.
Because ceramic Clay Colloids ion is because of SiO
2particle absorption SiO
3 2-and electronegative, their removal can only depend on and destroy its stability finely divided or colloid.Coagulation process is the necessary process of ceramic wastewater processing thus, by adding certain inorganic polyvalent metal salt (as aluminium salt), in and the current potential of colloid be the de-steady and collision mutually of colloidal solid, again by precipitation or mechanical filter, significantly cut down the demand of pollutant levels.
And at present a lot of Ceramics Enterprises are owing to founding the factory in early days to environmental protection attention not, add in addition the increase step by step of enterprises' production capacity, the enlarging of processing structures site space is limited etc., directly cause cannot reaching discharge and reuse requirement after wastewater treatment, for this present situation, be badly in need of a kind of purified treatment setting efficiently, realize fast purification function, reach discharge and reuse requirement.
Summary of the invention:
Goal of the invention of the present utility model is to provide a kind of ceramic wastewater processing method and device that efficiently, quickly and reliably purifies ceramic wastewater.
Ceramic wastewater processing method of the present invention is to realize like this, ceramic wastewater is first collected effluent settling chamber, bulky grain solids is deposited in effluent settling chamber, then by waste water pump, the waste water pump after preliminary sedimentation being delivered to high-efficiency and precision processor filters, filtering the clear water producing delivers in clear water reserviors in order to reuse, when the filtrate that high-efficiency and precision processor gathers reach a certain amount of after, pass into recoil clear water toward high-efficiency and precision processor, the mud developing imports in sludge-tank.
Here, high-efficiency and precision processor has more than two, and the high-efficiency and precision processor that is other toward the recoil clear water that wherein a high-efficiency and precision processor passes into filters the clear water producing.
High-efficiency and precision processor is that the model that the Ah Ka of Israel produces is: the ARKAL self-loopa filter of AKLF-12, when high-efficiency and precision processor is during in filtration condition, the water of filtered is by three layers of water-locator, coordinate spherical housing, arrive the packing layer in high-efficiency and precision processor with the state that approaches advection, in the time that water flows through packing layer, impurity is trapped within packing layer, 55 mushroom filtration water collectors are arranged at high-efficiency and precision processor bottom, water after filtering is collected equably and flowed out, advection filters, determine that high-efficiency and precision processor can filter under high flow velocity, still can reach good filter effect, along with the continuous accumulation of impurity in packing layer, loss in head will constantly increase, in the time that loss in head arrives certain setting limit, high-efficiency and precision processor is converted to backwash state automatically, to clean the impurity being accumulated, when system is during in backwash state, one or more high-efficiency and precision processors on the same group can be by clean, pour in down a chimney in this high-efficiency and precision processor by a threeway backwash valve through the water filtering simultaneously, pour in down a chimney in process at this, rushed under the impact of current by the packing layer of the high-efficiency and precision processor of backwash, impurity is discharged from by the backwash mouth of a threeway, in high-efficiency and precision processor, the water collector of particular design makes packing layer in the time of backwash state, form interior circulation, between filler, wash by rubbing with the hands mutually, improve to greatest extent backwash efficiency, reduce required backwash water, when backwash simultaneously, do not run the sand that forms packing layer, in the time that backwash finishes, valve is returned to again filtration condition, next high-efficiency and precision processor prepares to enter backwash state.
Ceramic wastewater treating apparatus of the present utility model is to realize like this, comprise effluent settling chamber, waste water pump, the above high-efficiency and precision processor of two covers, sludge-tank, clear water reserviors, effluent settling chamber passes through waste water pump, water pipe, a wherein valve port of the waste water three-way valve being connected with waste water import of high-efficiency and precision processors more than two covers, the waste water import of high-efficiency and precision processors more than two covers is connected, the clear water output with triple valve of high-efficiency and precision processors more than two covers is by a wherein valve port of triple valve, pipeline is connected with clear water reserviors, another valve port of the triple valve of the clear water output of high-efficiency and precision processors more than two covers is connected by pipeline, another valve port of the waste water three-way valve being connected with waste water import of high-efficiency and precision processors more than two covers is connected with sludge-tank.
When work, ceramic wastewater passes through waste water pump, a wherein valve port of waste water three-way valve enters high-efficiency and precision processor and filters, the clear water producing is by wherein valve port guiding clear water reserviors of the triple valve of clear water output, when impurity in a high-efficiency and precision processor wherein reaches a certain amount of, so that clear water pressure head reduces to after certain value, by control device control wherein a wherein valve port of the waste water three-way valve of a high-efficiency and precision processor close, another valve port conducting, simultaneously, controlling a wherein valve port of the three-way valve of another high-efficiency and precision processor closes, another valve port conducting, like this, the clear water of another high-efficiency and precision processor is from the wherein clear water output importing of a high-efficiency and precision processor, recoil, the mud that recoil produces passes through wherein another valve port of the waste water triple valve of a high-efficiency and precision processor and imports in sludge-tank, like this, rotation is to the cleaning that recoils of high-efficiency and precision processor, device can be processed ceramic wastewater continuously.
Compared with the prior art the utility model, has advantages of efficiently, quickly and reliably purifies ceramic wastewater.
Accompanying drawing explanation:
Fig. 1 is structural representation of the present utility model;
Fundamental diagram when Fig. 2 is high-efficiency and precision processor filtered wastewater;
Fundamental diagram when Fig. 3 is the backwash of high-efficiency and precision processor.
The specific embodiment:
Now in conjunction with the accompanying drawings and embodiments the present invention is described in further detail:
As shown in Figure 1, ceramic wastewater treating apparatus of the present invention is to realize like this, comprise effluent settling chamber 1, waste water pump 2, the above high-efficiency and precision processor 3 of two covers, sludge-tank 4, clear water reserviors 5, effluent settling chamber 1 is by waste water pump 2, water pipe 6, a wherein valve port of the waste water three-way valve 7 being connected with waste water import of high-efficiency and precision processors 3 more than two covers, the waste water import of high-efficiency and precision processors 3 more than two covers is connected, the clear water output with triple valve 8 of high-efficiency and precision processors 3 more than two covers is by a wherein valve port of triple valve 8, pipeline 9 is connected with clear water reserviors 5, another valve port of the triple valve 8 of the clear water output of high-efficiency and precision processors 3 more than two covers is connected by pipeline 9, another valve port of the waste water three-way valve 7 being connected with waste water import of high-efficiency and precision processors 3 more than two covers is connected with sludge-tank 4.
Claims (1)
1. a ceramic wastewater treating apparatus, it is characterized in that comprising effluent settling chamber, waste water pump, the above high-efficiency and precision processor of two covers, sludge-tank, clear water reserviors, effluent settling chamber is connected with the water inlet of waste water pump, the delivery port of waste water pump is connected with the water inlet of water pipe, the waste water import of every cover high-efficiency and precision processor is connected with waste water three-way valve, the delivery port of water pipe is connected with a wherein valve port of the waste water three-way valve on each high-efficiency and precision processor respectively, another valve port of waste water three-way valve is connected with sludge-tank, the 3rd valve port of waste water three-way valve is connected with the waste water import of high-efficiency and precision processor, the clear water output of each high-efficiency and precision processor is connected with triple valve, a wherein valve port of triple valve is connected with clear water reserviors by pipeline, another valve port of the triple valve being connected with clear water output of each high-efficiency and precision processor is connected by pipeline, the 3rd valve port of triple valve is connected with the clear water output of high-efficiency and precision processor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320885936.8U CN203694759U (en) | 2013-12-31 | 2013-12-31 | Ceramic wastewater treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320885936.8U CN203694759U (en) | 2013-12-31 | 2013-12-31 | Ceramic wastewater treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203694759U true CN203694759U (en) | 2014-07-09 |
Family
ID=51045260
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320885936.8U Expired - Lifetime CN203694759U (en) | 2013-12-31 | 2013-12-31 | Ceramic wastewater treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203694759U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103752080A (en) * | 2013-12-31 | 2014-04-30 | 李�杰 | Ceramic wastewater treatment method and device |
-
2013
- 2013-12-31 CN CN201320885936.8U patent/CN203694759U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103752080A (en) * | 2013-12-31 | 2014-04-30 | 李�杰 | Ceramic wastewater treatment method and device |
| CN103752080B (en) * | 2013-12-31 | 2016-05-04 | 李�杰 | A kind of ceramic wastewater processing method and device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103030237B (en) | Treatment device and treatment method for recycling coal slurry sewage | |
| CN105879464A (en) | Municipal sewage sand removing device and method | |
| CN105089144B (en) | A kind of spiral early-stage rainwater filtering and purifying | |
| CN205616682U (en) | Industrial waste water clean system | |
| CN205391831U (en) | Vertical flow type tube settler | |
| CN105251254B (en) | Variable type bidirectional flow high-speed fiber filter | |
| CN203999002U (en) | A kind of radial-flow multimedium waste disposal plant | |
| CN203694759U (en) | Ceramic wastewater treatment device | |
| CN203346197U (en) | Integrated water purification device | |
| CN102910754B (en) | Treatment process of boiler dusting water | |
| CN202390268U (en) | In-situ reuse treatment system for downhole directional drilling machine medium circulation water | |
| CN104973711A (en) | Sewage impurity separation method | |
| CN204898858U (en) | Spiral initial stage rainwater filtration purification device | |
| CN203530058U (en) | Municipal sewage treatment device | |
| CN208517093U (en) | A kind of high efficiency sewage treatment facility | |
| CN103752080B (en) | A kind of ceramic wastewater processing method and device | |
| CN204981379U (en) | Sewage treatment filter equipment based on metal film | |
| CN203264364U (en) | 360-degree water feeding rotary underwater filter bed device | |
| CN203954764U (en) | Quartz filter | |
| CN107417056A (en) | A kind of storage pond and its purification method with self-purging function | |
| CN103215985A (en) | Community rainwater utilization system based on secondary split-flow of rainwater and sewage | |
| CN202643468U (en) | Novel waste water cycle processor | |
| CN206334427U (en) | A kind of water inlet water-distributing device of solid-liquid point filter | |
| CN204017477U (en) | A kind of dual anti-blocking filtering pond | |
| CN204848509U (en) | Mud water processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20151216 Address after: 6, No. 301, building 528200, A zone, Han Tian Technology City, 17 deep sea road, Nanhai, Foshan, Guangdong, Guicheng Patentee after: FOSHAN YAJIEYUAN TECHNOLOGY CO.,LTD. Address before: 528000, room 12, 704 Nanpu village, Chancheng District, Guangdong, Foshan Patentee before: Li Jie Patentee before: Liang Xiong |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140709 |