CN2878375Y - Sludge dehydration and concentration device - Google Patents
Sludge dehydration and concentration device Download PDFInfo
- Publication number
- CN2878375Y CN2878375Y CN 200620095947 CN200620095947U CN2878375Y CN 2878375 Y CN2878375 Y CN 2878375Y CN 200620095947 CN200620095947 CN 200620095947 CN 200620095947 U CN200620095947 U CN 200620095947U CN 2878375 Y CN2878375 Y CN 2878375Y
- Authority
- CN
- China
- Prior art keywords
- sludge
- water
- outlet
- concentration tank
- pipe
- 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
- 239000010802 sludge Substances 0.000 title claims description 65
- 230000018044 dehydration Effects 0.000 title description 11
- 238000006297 dehydration reaction Methods 0.000 title description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 48
- 239000012141 concentrate Substances 0.000 claims abstract description 3
- 238000003756 stirring Methods 0.000 claims description 19
- 230000016615 flocculation Effects 0.000 claims description 12
- 238000005189 flocculation Methods 0.000 claims description 12
- 238000004140 cleaning Methods 0.000 claims description 7
- 230000008676 import Effects 0.000 claims description 7
- 238000012423 maintenance Methods 0.000 abstract description 3
- 239000010801 sewage sludge Substances 0.000 abstract 8
- 230000007423 decrease Effects 0.000 abstract 1
- 239000003795 chemical substances by application Substances 0.000 description 5
- 239000010865 sewage Substances 0.000 description 4
- 229920002401 polyacrylamide Polymers 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a device used to dehydrate and concentrate sewage sludge, which is composed an agitating and modulating tank (1), a concentration tank (2) and a pipe for sewage sludge(3). An inlet (1-1) and an outlet (1-2) for remaining sewage sludge are arranged on the agitating and modulating tank (1). An overflow tank (2-1) is arranged on upper part inside the concentration tank (2) and an outlet (2-2) for flocculated and concentrated remaining sewage sludge is positioned at the bottom of the concentration tank (2). An outlet for rinsing is arranged in the overflow tank (2-1) of the concentration tank (2), and the outlet (1-2) for remaining sewage sludge of the agitating and modulating tank (1) is connected with the inlet of the pipe for sewage sludge. The outlet of pipe for sewage sludge extends into inside the concentration tank (2). The utility model greatly decreases the cost for disposing sewage sludge and labor intensity of worker because of the advantages of low current drain, water consumption, consumption of devices, as well as low maintenance costs of devices.
Description
Technical field
The utility model relates to the waste disposal plant field.
Background technology
At present, sewage mostly adopts sludge dehydration device that mud in the excess sludge and clear water are separated in treating processes.Sludge dehydration device is mainly formed by stirring modulation jar and sludge dewatering equipment, the principle of work of sludge dehydration device is, the excess sludge (water ratio is about 99.6%) that sewage is produced after biochemical treatment, by adding the flocculation agent polyacrylamide in stirring modulation jar behind the mixing, enter the sludge dewatering equipment flocculation dewatering, sludge dewatering equipment separates water in the excess sludge and mud, and clear water can turn back to Sewage treatment systems, reaches the purpose of excess sludge reduction.Its weak point is, because sewage is after biochemical treatment, it is lower to enter the excess sludge silt content that sludge dewatering equipment handles, and is generally about 0.4%, excess sludge clear water amount after flocculating is big, and the speed that clear water is separated is slow thereby influence the working efficiency of sludge dewatering equipment.
Technology contents
The purpose of this utility model is exactly that to enter the excess sludge silt content that sludge dewatering equipment handles lower at existing, a kind of sludge dewatering concentrating unit that influences the deficiency of sludge dewatering equipment working efficiency and provide, it is by stirring modulation jar 1, concentration tank 2 and sludge pipe 3 are formed, stir modulation jar 1 and be provided with excess sludge import 1-1 and excess sludge outlet 1-2, be provided with spilling water weir notch 2-1 at concentration tank 2 internal upper parts, be provided with flocculation in concentration tank 2 bottoms and concentrate excess sludge outlet 2-2, in the spilling water weir notch 2-1 of concentration tank 2, be provided with clear water output 2-3, the excess sludge outlet 1-2 that stirs modulation jar 1 communicates with the water-in of sludge pipe, and the water outlet end of sludge pipe is inserted in the concentration tank 2.It cleans water pipe 4 in addition, and the water-in of cleaning water pipe 4 communicates with the clear water output 2-3 of spilling water weir notch 2-1, and the water outlet that cleans water pipe 4 communicates with the excess sludge import of stirring modulation jar 1, on cleaning water pipe 4 valve is installed.
The utility model has the advantages that: after it can add excess sludge earlier flocculation agent flocculation concentration, secondary added the flocculation agent flocculation and enters the sludge dewatering equipment dehydration again.Excess sludge is entered before the sludge dewatering equipment, wherein existing water over half is separated in concentration tank, make in the excess sludge silt content surpass more than 1%, the excess sludge silt content that enters like this in the sludge dewatering equipment is enhanced about more than once, clear water in the former excess sludge has over halfly need not pass through sludge dewatering equipment, is equivalent to make the sludge dewatering equipment working efficiency to be enhanced about more than once.Promptly improved mud handling capacity in the unit time more than one times, reduced the working time of sludge dewatering equipment, reduced power consumption, water consumption, equipment loss, maintenance of the equipment maintenance cost, thereby greatly reduce the sludge treatment cost.Also reduced simultaneously labor strength.Use this device also can save the traditional sludge concentration basin, saved the investment cost of sludge thickener.
Description of drawings
Accompanying drawing 1 is the utility model structural representation, and white arrow is that clear water flows in the accompanying drawing, and black arrow flows to for concentrating excess sludge; Accompanying drawing 2 is the utility model concentration tank sectional structure synoptic diagram.
Embodiment
Stir modulation jar and concentration tank all with steel plate processing, stirring modulation jar and the stirring in the existing sludge dehydration device, to modulate jar structure the same, and agitator is installed in jar, and the height of concentration tank can be 8 meters, 2 meters of diameters.The spilling water weir notch is the groove that is provided with along tank skin in concentration tank, the wide 150mmm of overfalling weir bottom land, and high 160mm, the overfalling weir trench bottom can be reinforced with angle steel, and the upper surface of spilling water weir notch is provided with the sawtooth mouth.At each import and export place valve can be installed.The water-in that cleaning is assured communicates with the clear water output of spilling water weir notch, and water outlet communicates with the excess sludge import of stirring the modulation jar, on the cleaning water pipe valve is installed.
Other by specification and the connection of Figure of description mode of connection get final product.
Using method: former adding sludge dehydration device is stirred excess sludge in the modulation jar, after adding the flocculation agent polyacrylamide, be evacuated in the stirring modulation jar of this device behind the mixing, enter (will close the rinse water pipe valve this moment) in the concentration tank.In concentration tank,, there is clear water over half to overflow into the spilling water weir notch on top approximately, discharges through clear water output through flocculation sediment.Flocculation mud sinks down into the bottom, after concentrated excess sludge outlet adds the flocculation agent polyacrylamide, from the stirring modulation jar 5 that flow in the sludge dehydration device, after stirring, sends into sludge dewatering equipment 6 again and carries out processed again.The effect of cleaning water pipe is before sludge dehydration device quits work, close earlier and enter the excess sludge import that this device stirs the modulation jar, open the rinse water pipe valve, make clear water flow into this device and stir the modulation jar, with clear water this device is cleaned, the muddy water of cleaning is delivered to sludge dewatering equipment, stops sludge dehydration device after this device cleans up substantially again, after avoiding stopping sludge dehydration device, mud is difficult to remove after accumulating and doing in this device.
Claims (2)
1, a kind of sludge dewatering concentrating unit, it is characterized in that it is by stirring modulation jar (1), concentration tank (2) and sludge pipe (3) are formed, stir modulation jar (1) and be provided with excess sludge import (1-1) and excess sludge outlet (1-2), be provided with spilling water weir notch (2-1) at concentration tank (2) internal upper part, be provided with flocculation in concentration tank (2) bottom and concentrate excess sludge outlet (2-2), in the spilling water weir notch (2-1) of concentration tank (2), be provided with clear water output (2-3), the excess sludge outlet (1-2) of stirring modulation jar (1) communicates with the water-in of sludge pipe, and the water outlet end of sludge pipe is inserted in the concentration tank (2).
2, sludge dewatering concentrating unit according to claim 1, it is characterized in that it cleans water pipe (4) in addition, the water-in that cleans water pipe (4) communicates with the clear water output (2-3) of spilling water weir notch (2-1), the water outlet that cleans water pipe (4) communicates with the excess sludge import of stirring modulation jar 1, on cleaning water pipe (4) valve is installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620095947 CN2878375Y (en) | 2006-03-30 | 2006-03-30 | Sludge dehydration and concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620095947 CN2878375Y (en) | 2006-03-30 | 2006-03-30 | Sludge dehydration and concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2878375Y true CN2878375Y (en) | 2007-03-14 |
Family
ID=37860791
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620095947 Expired - Lifetime CN2878375Y (en) | 2006-03-30 | 2006-03-30 | Sludge dehydration and concentration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2878375Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101823785A (en) * | 2010-05-07 | 2010-09-08 | 江苏思诺环保机械科技有限公司 | Sludge flocculation reactor |
| CN104961322A (en) * | 2015-05-19 | 2015-10-07 | 温州大学 | Mud-water separation device and slurry mud-water separation method |
| CN104961210A (en) * | 2015-05-19 | 2015-10-07 | 温州大学 | Mud-water separation device |
| CN111875211A (en) * | 2020-06-17 | 2020-11-03 | 上海仁创环境科技有限公司 | Muddy water concentration and separation device and separation method |
-
2006
- 2006-03-30 CN CN 200620095947 patent/CN2878375Y/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101823785A (en) * | 2010-05-07 | 2010-09-08 | 江苏思诺环保机械科技有限公司 | Sludge flocculation reactor |
| CN104961322A (en) * | 2015-05-19 | 2015-10-07 | 温州大学 | Mud-water separation device and slurry mud-water separation method |
| CN104961210A (en) * | 2015-05-19 | 2015-10-07 | 温州大学 | Mud-water separation device |
| CN111875211A (en) * | 2020-06-17 | 2020-11-03 | 上海仁创环境科技有限公司 | Muddy water concentration and separation device and separation method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN2878375Y (en) | Sludge dehydration and concentration device | |
| CN210237322U (en) | Mine water recycling treatment system | |
| CN203355383U (en) | Coagulative precipitation tank | |
| CN201154258Y (en) | Waste water treatment plant for producing feedstuff-level calcium phosphate salt by sulfuric acid method | |
| CN103420483B (en) | A kind of sequencing batch type waste disposal plant | |
| CN103693840B (en) | Sludge storage tank and sludge concentration process | |
| CN203545784U (en) | Combined type oxidation ditch with external sedimentation basin | |
| CN204434432U (en) | A kind of sludge conditioning broken wall reaction unit | |
| CN205420078U (en) | Printing and dyeing wastewater advanced treatment unit is concentrated to industry park | |
| CN204779220U (en) | Sewage treatment device based on activated sludge process | |
| CN202576132U (en) | System for closed cyclic utilization of cinder flushing water in sulfuric acid preparation | |
| CN205387512U (en) | Wastewater treatment device | |
| CN204779028U (en) | Two -stage and oxygen sewage treatment plant | |
| CN204779225U (en) | Be applied to sewage treatment's double oxygen device | |
| CN201354326Y (en) | Multi-flow direction reinforced clarifier | |
| CN202415272U (en) | Sewage scum and sludge treatment device | |
| CN202785858U (en) | Coal-containing waste water processing and recycling system | |
| CN206858414U (en) | Desliming system waste water surplus flocculant regenerates and recycling device | |
| CN213475747U (en) | Municipal sludge solidification greening storehouse | |
| CN217377418U (en) | A high-efficient phosphorus removal device for rich phosphorus supernatant of sludge concentration pond | |
| CN204058089U (en) | Seasonal high turbid original sub-block device | |
| CN210595603U (en) | Efficient phosphorus removal and turbidity reduction process device | |
| CN211664844U (en) | Front physicochemical treatment device system for printing and dyeing wastewater | |
| CN204281522U (en) | Wool yarn factory Sewage treatment systems | |
| CN107954586A (en) | Water cycle utilization device and method are rinsed in desliming |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: HEJIA ZIYUAN DEVELOPMENT STOCK CO., LTD. ADDRESS Free format text: FORMER OWNER: ZHAO DA ADDRESS Effective date: 20081121 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20081121 Address after: No. 3, Huanyu Road, Majuqiao Jinqiao technology industry base, Beijing, Tongzhou District, China: 101102 Patentee after: Hejia Resources Development Co., Ltd. Address before: Hubei city of Jingmen province Duodao district do Bai Miao Jie Jiang Shan Cun Xia Jia Wan Jingmen city Water Service Company, zip code: 448002 Patentee before: Zhao Da |
|
| ASS | Succession or assignment of patent right |
Owner name: HEJIA ZIYUAN DEVELOPMENT STOCK CO., LTD. Free format text: FORMER OWNER: ZHAO DA Effective date: 20081121 |
|
| C56 | Change in the name or address of the patentee |
Owner name: SOUND ENVIRONMENTAL RESOURCES CO., LTD. Free format text: FORMER NAME: HEJIA RESOURCES DEVELOPMENT CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 101102, No. 3, Huanyu Road, Majuqiao Jinqiao technology industry base, Beijing, Tongzhou District Patentee after: Sound Environmental Resources Co., Ltd. Address before: 101102, No. 3, Huanyu Road, Majuqiao Jinqiao technology industry base, Beijing, Tongzhou District Patentee before: Hejia Resources Development Co., Ltd. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20070314 |
|
| EXPY | Termination of patent right or utility model | ||
| DD01 | Delivery of document by public notice |
Addressee: Sound Environmental Resources Co., Ltd. Document name: Notification of Expiration of Patent Right Duration |