CN106915893A - The method and its device of a kind of efficient process sludge dewatering - Google Patents
The method and its device of a kind of efficient process sludge dewatering Download PDFInfo
- Publication number
- CN106915893A CN106915893A CN201710290953.XA CN201710290953A CN106915893A CN 106915893 A CN106915893 A CN 106915893A CN 201710290953 A CN201710290953 A CN 201710290953A CN 106915893 A CN106915893 A CN 106915893A
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- sludge
- dictyosome
- pam
- stirring pool
- stirring
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Filtration Of Liquid (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention provides the method and its device of a kind of efficient process sludge dewatering.Methods described is carried out as follows：1st, the installation of equipment be connected；2nd, flocculating agent formulation；3rd, material conveying；4th, stirring flocculation；5th, drying and other treatment.Described device pipeline respectively connects sludge concentration tank, PAM dissolving tanks, stirring pool and dry net body phase, sewage sludge feed pump, solution stirrer and agitator are respectively provided with sludge concentration tank, PAM dissolving tanks and stirring pool, water leg drainpipe is connected with cesspool.Filter screen drying sludge groove process is simple used in the method and device, it is easy to operate, it is not necessary to which that the ratio debugging and start operation debugging of complicated sludge and PAM solution, and small investment, low cost, using effect are good, and mud handling capacity is big.
Description
Technical field
The present invention relates to process sludge and environmental technology field, a kind of side of efficient process sludge dewatering is related specifically to
Method and its device.
Background technology
Treatment of Sludge is the important component of sewage disposal, it is necessary to carry out solid, liquid to sludge in sludge handling process
Separate, the sewage after separation is further carried out treatment, outward transport treatment is then carried out to dewatered sludge.Sludge dehydration device mostly by
Sludge carrier pipe, sludge pump and dewatering device are into defeated from sludge-tank by sludge by sludge material delivery pipe and sludge pump
Delivering to dewaterer carries out separation of solid and liquid.But the methods such as current mechanism filter-pressing, vacuum filter, investment is high, power drain is big, operation
Complexity, pipeline is easily blocked, thus most of multiple enterprises are reluctant or the powerless treatment for carrying out sludge in sewage, cause sludge to be arranged everywhere
Put, cause secondary pollution, it is impossible to reach elimination pollution, the purpose of environmental protection.
The content of the invention
Object of the present invention is to provide a kind of small investment, low cost is rational in infrastructure, and mud handling capacity is big, solid-liquid point
From the method and its device of the good efficient process sludge dewatering of effect.
To achieve the above object, the technical scheme is that：
A kind of method of efficient process sludge dewatering, it is characterised in that：Methods described is carried out as follows：
1st, the installation of equipment be connected：Dictyosome will be dried and be placed on position beneficial to draining, with connector by the filter of 50-200 mesh
Net is arranged on surrounding and the bottom for drying dictyosome, and the remaining seam of 45-50cm is left on filter screen periphery, with pipeline respectively by sludge condensation
The connection of pond, PAM dissolving tanks, stirring pool and dry net body phase；
2nd, flocculating agent formulation：Water and polyacrylamide are pressed 1000：The ratio of 0.8-1.2 is injected into PAM dissolving tanks, is started molten
Liquid agitator is stirred under being 63-85 revs/min in rotating speed, after stirring, is made mass percent concentration for 0.08-
0.12% flocculant solution；
3rd, material conveying：It is the sludge water of 95-99% by water content in sludge concentration tank, flow is pressed for 10- by sewage sludge feed pump
15m3/h is delivered in stirring pool, while the flocculant solution in PAM dissolving tanks is by PAM measuring pumps, it is 200- by flow
The speed of 500L/h is delivered in stirring pool；
4th, stirring flocculation：Start the agitator of stirring pool, control the rotating speed of agitator for 63-85 revs/min is stirred, work as discovery
When there are a large amount of flocculates to occur in stirring pool, start sludge pump, will be during flocculation material be delivered to and dries dictyosome；
5th, drying and other treatment：Flocculation material in feeding dry net body, its moisture is respectively from drying dictyosome surrounding and bottom 50-200
Flowed out in purpose filter screen, entered in cesspool through water leg, natural air drying took solid sludges after 3-7 days from dictyosome is dried
Go out, pack is transported.
A kind of device of efficient process sludge dewatering, including sludge concentration tank, PAM dissolving tanks, stirring pool, dry dictyosome,
Water leg, cesspool, sewage sludge feed pump, solution stirrer, PAM measuring pumps, agitator, sludge pump, filter screen and connector, it is described
The sludge concentration tank of device is connected built with sewage sludge feed pump, sludge concentration tank material delivery pipe with stirring pool, and material is defeated
Send equipped with sludge pump valve on pipe, PAM dissolving tanks are built with solution stirrer, PAM dissolving tanks solution conveyor tube and stirring pool phase
Connection, is respectively provided with PAM measuring pumps and solution control valve on solution conveyor tube, and stirring pool uses pipeline built with agitator
Connected with dry net body phase, sludge pump is housed on pipeline, dried and water leg is provided with below dictyosome, water leg drainpipe
It is connected with cesspool.
The surrounding for drying dictyosome and bottom with filter screen of the connector equipped with 50-200 mesh, dry the filter of dictyosome bottom respectively
The mud discharging mouth that can be switched is provided with net.
The positive effect of the present invention is：
1st, the filter screen drying sludge groove process is simple used in the method and device, easy to operate, it is not necessary to complicated sludge
Ratio debugging and start operation debugging with PAM solution；
2nd, the method and plant investment are few, low cost.Engineering such as the filter screen drying sludge groove of 400 cubic metres of sewage of day treatment is made
20 yuan of valency, expense 80% can be typically saved than methods such as mechanism filter-pressing, vacuum filters；
3rd, the device using effect is good, and mud handling capacity is big, effectively prevent the secondary pollution of sludge.Such as factory day treatment sewage
400 tons, kilogram/day of the sludge amount of actually occurring 800, sludge need to take up an area 200 square metres without drying and other treatment, after drying and other treatment only
Take up an area 30 square metres, the sludge after desiccation can transport outward utilization.
Brief description of the drawings
The connection diagram of Fig. 1, efficient process sludge dehydration device.
Specific embodiment
Clear, complete description further is carried out to technical scheme with reference to the accompanying drawings and examples.
Embodiment one
Referring to Fig. 1
1st, the installation of equipment be connected：Dictyosome 4 will be dried and be placed on the top position of water leg 5, with connector 19 by the filter of 50 mesh
Net 17 is arranged on surrounding and the bottom for drying dictyosome 4, and the remaining seam of 45-50cm is left on the periphery of filter screen 17, in case the stress of filter screen 17 is broken
Split, sludge concentration tank 1 is connected with stirring pool 3 respectively with material delivery pipe 14, PAM dissolving tanks 2 are measured with pipeline with PAM
Pump 10 is connected, and PAM measuring pumps 10 are connected with dissolving delivery pipe 15 with stirring pool 3, stirring pool 3 pipeline and the phase of sludge pump 13
Connection, the pipeline of sludge pump 13 is connected with dictyosome 4 is dried, and water leg 5 is connected with drainpipe 16 with cesspool 6；
2nd, flocculating agent formulation：By water and polyacrylamide（PAM）By 1000：0.8 ratio is injected into PAM dissolving tanks 2, is started
Solution stirrer 9 is stirred under being 63 revs/min in rotating speed, after stirring, is made the wadding that mass percent concentration is 0.08%
Solidifying agent solution；
3rd, material conveying：It is the sludge water of 95-99% by water content in sludge concentration tank 1, is by flow by sewage sludge feed pump 7
10m3/h is delivered in stirring pool 3, while the flocculant solution in PAM dissolving tanks 2 is by flow by PAM measuring pumps 10
The speed of 200L/h is delivered in stirring pool 3；
4th, stirring flocculation：Start the agitator 12 of stirring pool 3, control the rotating speed of agitator 12 for 63 revs/min are stirred, work as hair
When there are a large amount of flocculates to occur in existing stirring pool 3, start sludge pump 13, will be during flocculation material be delivered to and dries dictyosome 4；
5 drying and other treatments：Feeding dries flocculation material in dictyosome 4, and its moisture is respectively from drying the surrounding of dictyosome 4 and the purpose of bottom 50
Flowed out in filter screen 17, entered in cesspool 6 through water leg 5, after 3-7 days, opening dries the mud discharging mouth of the bottom of dictyosome 4 to natural air drying
18, solid sludges to be taken out from dictyosome 4 is dried, pack is transported.
Embodiment two
Referring to Fig. 1
1st, the installation of equipment be connected：Dictyosome 4 will be dried and be placed on the top position of water leg 5, with connector 19 by the filter of 100 mesh
Net 17 is arranged on surrounding and the bottom for drying dictyosome 4, and the remaining seam of 45-50cm is left on the periphery of filter screen 17, in case the stress of filter screen 17 is broken
Split, sludge concentration tank 1 is connected with stirring pool 3 respectively with material delivery pipe 14, PAM dissolving tanks 2 are measured with pipeline with PAM
Pump 10 is connected, and PAM measuring pumps 10 are connected with dissolving delivery pipe 15 with stirring pool 3, stirring pool 3 pipeline and the phase of sludge pump 13
Connection, the pipeline of sludge pump 13 is connected with dictyosome 4 is dried, and water leg 5 is connected with drainpipe 16 with cesspool 6；
2nd, flocculating agent formulation：By water and polyacrylamide（PAM）By 1000：0.9 ratio is injected into PAM dissolving tanks 2, is started
Solution stirrer 9 is stirred under being 63 revs/min in rotating speed, after stirring, is made the wadding that mass percent concentration is 0.09%
Solidifying agent solution；
3rd, material conveying：It is the sludge water of 95-99% by water content in sludge concentration tank 1, is by flow by sewage sludge feed pump 7
12m3/h is delivered in stirring pool 3, while the flocculant solution in PAM dissolving tanks 2 is by flow by PAM measuring pumps 10
The speed of 300L/h is delivered in stirring pool 3；
4th, stirring flocculation：Start the agitator 12 of stirring pool 3, control the rotating speed of agitator 12 for 63 revs/min are stirred, work as hair
When there are a large amount of flocculates to occur in existing stirring pool 3, start sludge pump 13, will be during flocculation material be delivered to and dries dictyosome 4；
5 drying and other treatments：Feeding dries flocculation material in dictyosome 4, and its moisture is respectively from drying the surrounding of dictyosome 4 and the mesh of bottom 100
Filter screen 17 in flow out, entered in cesspool 6 through water leg 5, natural air drying is after 3-7 days, opens the spoil disposal for drying the bottom of dictyosome 4
Mouth 18, solid sludges are taken out from dictyosome 4 is dried, and pack is transported.
Embodiment three
Referring to Fig. 1
1st, the installation of equipment be connected：Dictyosome 4 will be dried and be placed on the top position of water leg 5, with connector 19 by the filter of 150 mesh
Net 17 is arranged on surrounding and the bottom for drying dictyosome 4, and the remaining seam of 45-50cm is left on the periphery of filter screen 17, in case the stress of filter screen 17 is broken
Split, sludge concentration tank 1 is connected with stirring pool 3 respectively with material delivery pipe 14, PAM dissolving tanks 2 are measured with pipeline with PAM
Pump 10 is connected, and PAM measuring pumps 10 are connected with dissolving delivery pipe 15 with stirring pool 3, stirring pool 3 pipeline and the phase of sludge pump 13
Connection, the pipeline of sludge pump 13 is connected with dictyosome 4 is dried, and water leg 5 is connected with drainpipe 16 with cesspool 6；
2nd, flocculating agent formulation：By water and polyacrylamide（PAM）By 1000：1.1 ratio is injected into PAM dissolving tanks 2, is started
Solution stirrer 9 is stirred under being 85 revs/min in rotating speed, after stirring, is made the wadding that mass percent concentration is 0.11%
Solidifying agent solution；
3rd, material conveying：It is the sludge water of 95-99% by water content in sludge concentration tank 1, is by flow by sewage sludge feed pump 7
14m3/h is delivered in stirring pool 3, while the flocculant solution in PAM dissolving tanks 2 is by flow by PAM measuring pumps 10
The speed of 400L/h is delivered in stirring pool 3；
4th, stirring flocculation：Start the agitator 12 of stirring pool 3, control the rotating speed of agitator 12 for 85 revs/min are stirred, work as hair
When there are a large amount of flocculates to occur in existing stirring pool 3, start sludge pump 13, will be during flocculation material be delivered to and dries dictyosome 4；
5 drying and other treatments：Feeding dries flocculation material in dictyosome 4, and its moisture is respectively from drying the surrounding of dictyosome 4 and the mesh of bottom 150
Filter screen 17 in flow out, entered in cesspool 6 through water leg 5, natural air drying is after 3-7 days, opens the spoil disposal for drying the bottom of dictyosome 4
Mouth 18, solid sludges are taken out from dictyosome 4 is dried, and pack is transported.
Example IV
Referring to Fig. 1
1st, the installation of equipment be connected：Dictyosome 4 will be dried and be placed on the top position of water leg 5, with connector 19 by the filter of 200 mesh
Net 17 is arranged on surrounding and the bottom for drying dictyosome 4, and the remaining seam of 45-50cm is left on the periphery of filter screen 17, in case the stress of filter screen 17 is broken
Split, sludge concentration tank 1 is connected with stirring pool 3 respectively with material delivery pipe 14, PAM dissolving tanks 2 are measured with pipeline with PAM
Pump 10 is connected, and PAM measuring pumps 10 are connected with dissolving delivery pipe 15 with stirring pool 3, stirring pool 3 pipeline and the phase of sludge pump 13
Connection, the pipeline of sludge pump 13 is connected with dictyosome 4 is dried, and water leg 5 is connected with drainpipe 16 with cesspool 6；
2nd, flocculating agent formulation：By water and polyacrylamide（PAM）By 1000：1.2 ratio is injected into PAM dissolving tanks 2, is started
Solution stirrer 9 is stirred under being 85 revs/min in rotating speed, after stirring, is made the wadding that mass percent concentration is 0.12%
Solidifying agent solution；
3rd, material conveying：It is the sludge water of 95-99% by water content in sludge concentration tank 1, is by flow by sewage sludge feed pump 7
15m3/h is delivered in stirring pool 3, while the flocculant solution in PAM dissolving tanks 2 is by flow by PAM measuring pumps 10
The speed of 500L/h is delivered in stirring pool 3；
4th, stirring flocculation：Start the agitator 12 of stirring pool 3, control the rotating speed of agitator 12 for 85 revs/min are stirred, work as hair
When there are a large amount of flocculates to occur in existing stirring pool 3, start sludge pump 13, will be during flocculation material be delivered to and dries dictyosome 4；
5 drying and other treatments：Feeding dries flocculation material in dictyosome 4, and its moisture is respectively from drying the surrounding of dictyosome 4 and the mesh of bottom 200
Filter screen 17 in flow out, entered in cesspool 6 through water leg 5, natural air drying is after 3-7 days, opens the spoil disposal for drying the bottom of dictyosome 4
Mouth 18, solid sludges are taken out from dictyosome 4 is dried, and pack is transported.
All features disclosed in this specification, or it is disclosed it is all during the step of, except mutually exclusive feature
And/or beyond step, can combine by any way.This specification（Including claim, summary）Disclosed in any spy
Levy, unless specifically stated otherwise, can alternative features equivalent by other or with similar purpose replaced.I.e. except non-specifically is chatted
State, each feature is an example in a series of equivalent or similar characteristics.
The above is only non-limiting implementation method of the invention, substantial amounts of embodiment can also be derived, for ability
For the those of ordinary skill in domain, not departing from the invention design and on the premise of not making creative work, can be with
Some deformations and improved embodiment are made, these belong to protection scope of the present invention.
Claims (3)
1. a kind of method of efficient process sludge dewatering, it is characterised in that：Methods described is carried out as follows：
（1）The installation of equipment be connected：Dictyosome will be dried（4）The position beneficial to draining is placed on, connector is used（19）By 50-
The filter screen of 200 mesh（17）Installed in drying dictyosome（4）Surrounding and bottom, filter screen（17）The remaining seam of 45-50cm is left on periphery, uses
Pipeline is respectively by sludge concentration tank（1）, PAM dissolving tanks（2）, stirring pool（3）With dry dictyosome（4）It is connected；
（2）Flocculating agent formulation：Water and polyacrylamide are pressed 1000：The ratio of 0.8-1.2 is injected into PAM dissolving tanks（2）In, open
Dynamic solution stirrer（9）It is stirred under being 63-85 revs/min in rotating speed, after stirring, being made mass percent concentration is
The flocculant solution of 0.08-0.12%；
（3）Material is conveyed：By sludge concentration tank（1）Middle water content is the sludge water of 95-99%, by sewage sludge feed pump（7）By stream
Measure as 10-15m3/h is delivered to stirring pool（3）In, while PAM dissolving tanks（2）In flocculant solution pass through PAM measuring pumps
（10）, by flow for the speed of 200-500L/h is delivered to stirring pool（3）In；
（4）Stirring flocculation：Start stirring pool（3）Agitator（12）, control agitator（12）Rotating speed enter for 63-85 revs/min
Row stirring, when discovery stirring pool（3）In when thering are a large amount of flocculates to occur, start sludge pump（13）, flocculation material is delivered to dry
Dry dictyosome（4）In；
（5）Drying and other treatment：Feeding dries dictyosome（4）Interior flocculation material, its moisture content is respectively from drying dictyosome（4）Surrounding and bottom
The filter screen of 50-200 mesh（17）Middle outflow, through water leg（5）Enter cesspool（6）In, natural air drying is dirty by solid after 3-7 days
Mud is from drying dictyosome（4）Middle taking-up, pack is transported.
2. a kind of device of efficient process sludge dewatering, including sludge concentration tank（1）, PAM dissolving tanks（2）, stirring pool（3）, it is dry
Dry dictyosome（4）, water leg（5）, cesspool（6）, sewage sludge feed pump（7）, solution stirrer（9）, PAM measuring pumps（10）, stirring
Device（12）, sludge pump（13）, filter screen（17）And connector（19）, it is characterised in that：The sludge concentration tank of described device（1）It is built-in
There is sewage sludge feed pump（7）, sludge concentration tank（1）Use material delivery pipe（14）With stirring pool（3）It is connected, material delivery pipe（14）
It is upper that sludge pump valve is housed（8）, PAM dissolving tanks（2）Built with solution stirrer（9）, PAM dissolving tanks（2）Use solution conveyor tube
（15）With stirring pool（3）It is connected, in solution conveyor tube（15）On be respectively provided with PAM measuring pumps（10）And solution control valve
（11）, stirring pool（3）Built with agitator（12）, and with pipeline with dry dictyosome（4）It is connected, sludge pump is housed on pipeline
（13）, dry dictyosome（4）Lower section be provided with water leg（5）, water leg（5）Use drainpipe（16）With cesspool（6）It is connected.
3. the device of efficient process sludge dewatering according to claim 2, it is characterised in that：It is described to dry dictyosome（4）'s
Connector is used in surrounding and bottom respectively（19）Filter screen equipped with 50-200 mesh（17）, dry dictyosome（4）Energy is provided with bottom screen
The mud discharging mouth of switch（18）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710290953.XA CN106915893A (en) | 2017-04-28 | 2017-04-28 | The method and its device of a kind of efficient process sludge dewatering |
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| CN201710290953.XA CN106915893A (en) | 2017-04-28 | 2017-04-28 | The method and its device of a kind of efficient process sludge dewatering |
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| CN106915893A true CN106915893A (en) | 2017-07-04 |
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| CN201710290953.XA Pending CN106915893A (en) | 2017-04-28 | 2017-04-28 | The method and its device of a kind of efficient process sludge dewatering |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109020157A (en) * | 2018-09-19 | 2018-12-18 | 广东华欣环保科技有限公司 | A kind of processing method of high oil-containing wastewater sludge |
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| CN1781853A (en) * | 2005-10-28 | 2006-06-07 | 北京科技大学 | Dewatering method for sludge microbiologically treating life waste water |
| CN101628781A (en) * | 2009-08-24 | 2010-01-20 | 杭州绿鼎压滤机制造有限公司 | SludgeDewatering equipment and sludge dewatering process |
| CN101935140A (en) * | 2010-07-23 | 2011-01-05 | 无锡市通用机械厂有限公司 | Dehydration treatment method for tail water sludge of water-work and special apparatus thereof |
| CN104496139A (en) * | 2015-01-01 | 2015-04-08 | 扬州杰嘉工业固废处置有限公司 | Pretreatment method of heavy metal sludge |
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2017
- 2017-04-28 CN CN201710290953.XA patent/CN106915893A/en active Pending
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| CN1781853A (en) * | 2005-10-28 | 2006-06-07 | 北京科技大学 | Dewatering method for sludge microbiologically treating life waste water |
| CN101628781A (en) * | 2009-08-24 | 2010-01-20 | 杭州绿鼎压滤机制造有限公司 | SludgeDewatering equipment and sludge dewatering process |
| CN101935140A (en) * | 2010-07-23 | 2011-01-05 | 无锡市通用机械厂有限公司 | Dehydration treatment method for tail water sludge of water-work and special apparatus thereof |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109020157A (en) * | 2018-09-19 | 2018-12-18 | 广东华欣环保科技有限公司 | A kind of processing method of high oil-containing wastewater sludge |
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Application publication date: 20170704 |
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