CN203781934U - Sewage treatment equipment of ceramic production line - Google Patents
Sewage treatment equipment of ceramic production line Download PDFInfo
- Publication number
- CN203781934U CN203781934U CN201420086157.6U CN201420086157U CN203781934U CN 203781934 U CN203781934 U CN 203781934U CN 201420086157 U CN201420086157 U CN 201420086157U CN 203781934 U CN203781934 U CN 203781934U
- Authority
- CN
- China
- Prior art keywords
- tank
- sewage disposal
- disposal device
- blender
- treating pond
- 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
- 239000010865 sewage Substances 0.000 title claims abstract description 35
- 239000000919 ceramic Substances 0.000 title claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 230000001154 acute effect Effects 0.000 claims abstract description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 26
- 238000001035 drying Methods 0.000 claims description 15
- 229910052742 iron Inorganic materials 0.000 claims description 13
- 239000012528 membrane Substances 0.000 claims description 7
- 238000010409 ironing Methods 0.000 abstract 2
- 238000000034 method Methods 0.000 description 7
- 239000002002 slurry Substances 0.000 description 7
- 239000002994 raw material Substances 0.000 description 5
- 238000000498 ball milling Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004049 embossing Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010433 feldspar Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000002649 leather substitute Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses sewage treatment equipment of a ceramic production line. A blender is connected to a ball grinder, wherein the ball grinder is connected to a de-ironing separator; the de-ironing separator is connected with a pressing machine; the sewage treatment equipment also comprises a clarifier-tank and a water channel; the axis of the water channel and the horizontal plane form an acute angle; the water channel is arranged below the pressing machine; the lower end of the water channel is connected to the clarifier-tank; the clarifier-tank comprises at least one water pump; the water pump is connected to the blender and/or the ball grinder; the water squeezed by the pressing machine is collected by the water tank, and then conveyed to the blender and the ball grinder after being participated and purified by the clarifier-tank. The sewage treatment equipment is attached to ceramic production, and an extra site is not required.
Description
Technical field
The utility model relates to the auxiliary facility of ceramic production line, relates in particular to the sewage disposal device of ceramic production line.
Background technology
Ceramic raw material needs through ball milling, the deironing step of press filt again in mud process processed, and wherein ball milling needs water filling endlessly, by press filt, moisture is extruded again, and the water after extruding contains a large amount of slurries, and eliminating pollutes.
Prior art provides some to process the method for ceramic production line sewage.
201220436785.3 disclose a kind of ceramics factory waste disposal plant, the water-in of the sewage agitated pool of this device communicates with plant effuent pipeline, sewage agitated pool is connected with dosing coagulation basin by hydraulic control sludge pump, dosing coagulation basin bottom communicates with inclined-plate clarifying basin bottom by pipeline, inclined-plate clarifying basin top communicates with filtering basin by pipeline, bottom is connected with plate-and-frame filter press with concentration basin respectively through ram pump pipeline, filtering basin are connected with clean water basin by recycle pump, and clean water basin water up to standard turns back to workshop recycling through circulation line.
201220143815.1 relate to ceramics wastewater treatment equipment, comprise the acid-base neutralisation pond connecting by pipeline successively, some reaction tanks, settling tank and clean water basin, this treatment unit also comprise can catchment, the equalizing tank of regulating pondage, waste water passes through the processing of equalizing tank, acid-base neutralisation pond, this reaction tank and settling tank successively, finally enters above-mentioned clean water basin.
Above two cases provide the structure of disposing of sewage, and not yet solve the problem of centralized recovery sewage before processing.
Utility model content
The utility model proposes a kind of sewage disposal device of ceramic production line, can be according to the feature of ceramic production line, centralized recovery sewage, focuses on, then by sewage Returning utilization.
The technical solution of the utility model is achieved in that
A kind of sewage disposal device of ceramic production line, comprise: blender, ball mill, tramp iron separator, slip drying press, described blender is connected to described ball mill, described ball mill is connected to described tramp iron separator, described tramp iron separator is connected to described slip drying press, it is characterized in that, described sewage disposal device also comprises treating pond and tank, the axis of described tank is horizontal by acute angle, this tank is arranged on the below of described slip drying press, the low side of described tank is connected to described treating pond, described treating pond has the water pump of at least one, described water delivery side of pump is connected to described blender and/or ball mill.
In sewage disposal device of the present utility model, the level height of described water pump is less than described low side.
In sewage disposal device of the present utility model, described water pump is positioned at the middle part of described treating pond.
In sewage disposal device of the present utility model, the inclination angle of described tank is 5 to 20 °.
In sewage disposal device of the present utility model, described treating pond is comprised of a plurality of separate unit cells, between described unit cells, connects successively by transport pipe.
In sewage disposal device of the present utility model, in described treating pond, be provided with a semi-permeable membranes, described low side and water pump lay respectively at the both sides of described semi-permeable membranes.
Implement the sewage disposal device of this ceramic production line of the present utility model, there is following beneficial effect: the water that tank squeezes out slip drying press collects, through the precipitation for the treatment of pond, purify, then be delivered to blender and ball mill.This sewage disposal device is attached to Production of Ceramics, does not need extra place.
Accompanying drawing explanation
Fig. 1 is the part-structure schematic diagram of sewage disposal device of the present utility model;
Fig. 2 is another part structural representation of sewage disposal device of the present utility model;
Fig. 3 is another part structural representation of sewage disposal device of the present utility model;
Fig. 4 is the preferred structure schematic diagram for the treatment of pond of the present utility model.
Embodiment
Below in conjunction with accompanying drawing, dual-purpose synthetic leather embossing machine of the present utility model is described in further detail.
The sewage disposal device of this ceramic production line of the present utility model as shown in Figures 1 to 3, comprising: blender 10, ball mill 20, tramp iron separator 40, slip drying press 62, treating pond 80 and tank 70.
Described blender 10 is connected to described ball mill 20, and described ball mill 20 is connected to described tramp iron separator 40, and described tramp iron separator 40 is connected to described slip drying press 62.Blender 10, for the raw materials such as lithium feldspar and triphane are mixed, adds water according to ratio in mixing process.Mixed raw material enters ball mill 20, and ball mill 20 is powdered by raw material grinding mill, needs constantly to add water in process of lapping.Raw material after grinding is mud shape, is passed in tramp iron separator 40, and electromagnetic equipment 42 is removed the irony in tramp iron separator 40.Slurry after deironing passes into slip drying press 62, and slip drying press 62 is squeezed out water, forms the lower pug of water content.Structurally, blender 10 can be sent to ball mill 20 by powder by belt 11.Can be in calutron 21 after ball mill 20 has ground preliminary deironing, then enters slurry pool 30, and the pump housing 31 is delivered to slurry in the container 41 of higher tramp iron separator 40, and at slurry, gradually in descending process, electromagnetic equipment 42 is by irony sucking-off.After deironing, through suction pit 50 transfers, then by a pump housing 61, slurry is delivered to slip drying press 62.Obviously, suction pit 50 and slurry pool 30, as transfer, can cancel or adopt pipeline to replace.
In the course of processing of whole pug, at least need in blender 10 and ball mill 20, add water, sometimes in tramp iron separator 40, also need to add water, but these moisture have and need to squeeze out in press filt process, due to the restriction of slip drying press 62 structures, moisture is easily collecting not.In addition, it is more that this moisture contains shale, should not directly use again.And the sewage disposal device of ceramic production line of the present utility model has solved the problems referred to above.
The axis of described tank 70 is horizontal by acute angle, and this tank 70 is arranged on the below of described slip drying press 62, and the low side of described tank 70 is connected to described treating pond 80.The oblique layout of tank 70, it is high-end 72 that higher one end is called, and lower one end is called low side 71.Slip drying press 62 drops in tank 70 after moisture is squeezed out, and moisture is collected in treating pond 80 under action of gravity.Described treating pond 80 has the water pump 82 of at least one, and described water pump 82 is connected to described blender 10 and/or ball mill 20.And this water pump 82 can be delivered to moisture blender 10 and ball mill 20 endlessly.
The purification style for the treatment of pond 80 can be varied, for example, can adopt the mode of precipitation, and the low side 71 of tank 70 is positioned at the top of described treating pond 80, and water enters treating pond 80 under action of gravity.Shale is deposited in the bottom for the treatment of pond 80 gradually, and water floats over upper surface.Described water pump 82 is positioned at the middle part of described treating pond 80, and the level height of described water pump 82 is less than described low side 71.Water pump 82 can be extracted the moisture of upper surface out, and the mud of bottom only need to regularly clear out.The mud clearing out in addition can be back to again blender 10 and use.In order to improve decontamination effect improving, described treating pond 80 is comprised of a plurality of separate unit cells 81, between unit cells 81, connects successively by transport pipe.Pipeline zero position is installed water pump 82, and this water pump 82, by the moisture suction opposite side of a side upper surface, precipitates, again until surperficial clear water can be used.
The utility model does not limit the purification style for the treatment of pond 80, and described treating pond 80 is interior can be provided with a semi-permeable membranes, and described low side 71 and water pump 82 lay respectively at the both sides of described semi-permeable membranes.Moisture particle is little, can pass semi-permeable membranes, and mud particle is large, stays put, and then water is separated.In addition, for the ease of collecting moisture, reduce difficulty of construction, the inclination angle of described tank 70 is 5 to 20 ° simultaneously.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (6)
1. the sewage disposal device of a ceramic production line, comprise: blender, ball mill, tramp iron separator, slip drying press, described blender is connected to described ball mill, described ball mill is connected to described tramp iron separator, described tramp iron separator is connected to described slip drying press, it is characterized in that, described sewage disposal device also comprises treating pond and tank, the axis of described tank is horizontal by acute angle, this tank is arranged on the below of described slip drying press, the low side of described tank is connected to described treating pond, described treating pond has the water pump of at least one, described water delivery side of pump is connected to described blender and/or ball mill.
2. sewage disposal device according to claim 1, is characterized in that, the level height of described water pump is less than described low side.
3. sewage disposal device according to claim 1, is characterized in that, described water pump is positioned at the middle part of described treating pond.
4. sewage disposal device according to claim 1, is characterized in that, the inclination angle of described tank is 5 to 20 °.
5. according to the sewage disposal device described in claim 1 to 4 any one, it is characterized in that, described treating pond is comprised of a plurality of separate unit cells, between described unit cells, connects successively by transport pipe.
6. according to the sewage disposal device described in claim 1 to 4 any one, it is characterized in that, in described treating pond, be provided with a semi-permeable membranes, described low side and water pump lay respectively at the both sides of described semi-permeable membranes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420086157.6U CN203781934U (en) | 2014-02-28 | 2014-02-28 | Sewage treatment equipment of ceramic production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420086157.6U CN203781934U (en) | 2014-02-28 | 2014-02-28 | Sewage treatment equipment of ceramic production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203781934U true CN203781934U (en) | 2014-08-20 |
Family
ID=51318142
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420086157.6U Expired - Lifetime CN203781934U (en) | 2014-02-28 | 2014-02-28 | Sewage treatment equipment of ceramic production line |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203781934U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN115532352A (en) * | 2022-09-07 | 2022-12-30 | 万合(恩平)新型材料科技有限公司 | Device for preparing kaolin base stock by decomposing and removing impurities from kaolin raw ore |
-
2014
- 2014-02-28 CN CN201420086157.6U patent/CN203781934U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN115532352A (en) * | 2022-09-07 | 2022-12-30 | 万合(恩平)新型材料科技有限公司 | Device for preparing kaolin base stock by decomposing and removing impurities from kaolin raw ore |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102228762B (en) | Dehydration method and device of tailings | |
| CN103408207B (en) | Integrated test device and method for dredging, dewatering and drying sludge in river and lake | |
| CN103357212B (en) | A kind of mine tailing solid-liquid separating equipment and method | |
| CN202754866U (en) | Device for treating sewage in ceramic factory | |
| CN104478193B (en) | The dewatering system of a kind of Soil leaching mud and method thereof | |
| CN204079743U (en) | A kind of Technique of Coal Mine Drainage sludge treatment equipment | |
| CN109721191A (en) | A kind of sandstone building stones production wastewater treatment system | |
| CN205473043U (en) | Breed sewage and collect separator | |
| CN103553274A (en) | Treatment process of industrial wastewater of medium density fiber | |
| CN203781934U (en) | Sewage treatment equipment of ceramic production line | |
| CN102500472A (en) | Concentrating, filtering and dehydrating process for flotation clean coal | |
| CN101805075A (en) | Method for purification treatment of underground wastewater of coal mine | |
| CN203700858U (en) | System with zero emission of papermaking pulp dreg and sludge | |
| CN102992578A (en) | Sludge thickening and dehydration system | |
| Skolubovich et al. | Cleaning and reusing backwash water of water treatment plants | |
| CN203866134U (en) | Movable type wastewater treatment device | |
| CN106995718B (en) | Treatment method of oil field settling tank bottom sludge discharge online treatment device | |
| CN205840846U (en) | Drilling mud does not land processing means | |
| CN205295010U (en) | Lithium cell waste water's processing and recovery system | |
| CN202143801U (en) | Tailing dehydrating device | |
| CN204569618U (en) | Oilfield sewage treatment device | |
| CN210163225U (en) | Finished concrete waste water cyclic utilization environmental protection processing apparatus | |
| CN203781954U (en) | Comprehensive water recycling device of aluminum electrolysis waste treatment system | |
| CN105399248A (en) | Treating process and treating system for sewage of concentrating plant or sand producing plant | |
| CN106007062A (en) | System and method for treating waste water of glass production |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 344600 Yu Qingting, Lichuan County, Fuzhou, Jiangxi Patentee after: Jiangxi Kangshu Ceramics Co.,Ltd. Address before: 344600 Yu Qingting, Lichuan County, Fuzhou, Jiangxi Patentee before: JIANGXI KANGSHU PORCELAIN CO.,LTD. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140820 |