CN208038286U - Sludge treating system and Treatment of Sludge vehicle - Google Patents
Sludge treating system and Treatment of Sludge vehicle Download PDFInfo
- Publication number
- CN208038286U CN208038286U CN201820115472.5U CN201820115472U CN208038286U CN 208038286 U CN208038286 U CN 208038286U CN 201820115472 U CN201820115472 U CN 201820115472U CN 208038286 U CN208038286 U CN 208038286U
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- sludge
- mud
- mixing tube
- filter press
- settling tank
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Abstract
The utility model discloses a kind of sludge treating system and Treatment of Sludge vehicles, the mud mouth of slush pump is connected with the mud inlet of impurity knockout drum, the mud inlet of first mixing tube is connected to impurity knockout drum mud mouth, flocculant feed unit discharge port, the mud mouth of first mixing tube is connected to settling tank mud inlet, and the mud mouth of settling tank bottom is connected by pipeline with the feeding mouth of filter press.In the mixed sludge pumping to settling tank of flocculant, only it is by the feeding mouth of the floccule body of settling tank bottom, sludge pumping to filter press, greatly reduce treating capacity of the filter press to sludge, improve the treatment effeciency of sludge, squeezer efficiently separates mud, water in sludge, dry mud convenience in transport after squeezing, reduces the processing cost of sludge.
Description
Technical field
The utility model is related to sludge treatment field, mud, water detach in specially a kind of sludge processing system and sludge
Handle vehicle.
Background technology
The landscape water bodies such as municipal lake pool, river are component part important in human settlement environment in city, resident living sewage
And rubbish enters river, due to the features such as river environmental capacity of water is small, water body self-purification ability is poor, bottom of river channel largely has accumulation
The nutriments such as machine carbon, nitrogen, phosphorus cause water hypoxia and darkly smelly state so as to cause a large amount of consumption of Dissolved Oxygen in Water.It is existing
Have in technology, is generally pumped with soil pick-up and transport bed-silt suction tank car, but the sludge quantity that river bed is not dehydrated is big, causes not take off
Sewage sludge cost of wheeling is higher, and is susceptible to sludge leakage because transporting in transportational process not in time, and secondary dirt is brought to environment
Dye;In addition, when needing the length for clearing up river longer, the sludge treatment device of fixed form is caused to move cumbersome, significantly
Increase the labor intensity of worker.
Utility model content
The purpose of this utility model is to provide a kind of sludge treating system, can effectively divide mud, water in sludge
From reducing the processing cost of sludge.
To achieve the goals above, the technical solution used for:A kind of sludge treating system, the mud mouth of slush pump with it is miscellaneous
The mud inlet of matter knockout drum is connected, and mud inlet and impurity knockout drum mud mouth, the flocculant feed unit of the first mixing tube discharge
Mouth connection, the mud mouth of the first mixing tube are connected to settling tank mud inlet, and the mud mouth of settling tank bottom passes through pipeline and press filtration
The feeding mouth of machine is connected.
Compared with prior art, the technique effect of the application is:In the mixed sludge pumping to settling tank of flocculant,
Only it is that the feeding mouth of the floccule body of settling tank bottom, sludge pumping to filter press is greatly reduced into place of the filter press to sludge
Reason amount improves the treatment effeciency of sludge, and squeezer efficiently separates mud, water in sludge, and the dry mud after squeezing is convenient
Transport, reduces the processing cost of sludge.
Another purpose of the utility model is to provide a kind of Treatment of Sludge vehicle, and the occupancy for reducing sludge treating system is empty
Between, and sludge treating system is facilitated to shift.
To achieve the goals above, the technical solution used for:A kind of Treatment of Sludge vehicle, including car bottom plate, the underbody
Settling tank, flocculant feed unit, impurity separation and filter press, the dry mud of filter press are laid with by headstock to tailstock sequence on plate
Outlet is located at the tailstock, and the first mixing tube is laid with above settling tank, and the second mixing tube, impurity separation are laid with above thickener
It is disposed with thickener above tank and filter press pan feeding side.
Compared with prior art, the technique effect of the application is:Sludge treating system is arranged on car bottom plate, is not only subtracted
The occupied space of small sludge treating system, and sludge treating system transfer is greatly facilitated, reduce the labor intensity of worker.
Description of the drawings
Fig. 1 is the flow chart of the utility model;
Fig. 2 is the schematic diagram of the utility model pipeline arrangement;
Fig. 3 is the dimensional structure diagram of the utility model arrangement on the car body;
Fig. 4 is to remove the schematic diagram after the first and second mixing tube in Fig. 3;
Fig. 5 is the side view of the utility model;
Fig. 6 is the vertical view of the utility model.
Specific implementation mode
It is described in further detail with reference to Fig. 1 to 6 pairs of the utility model.
The mud mouth of a kind of sludge treating system, slush pump 10 is connected with the mud inlet of impurity knockout drum 20, the first mixing
The mud inlet of pipe 31 is connected to 20 mud mouth of impurity knockout drum, 50 discharge port of flocculant feed unit, and the first mixing tube 31 goes out
Mud mouth is connected to 40 mud inlet of settling tank, and the mud mouth of 40 bottom of settling tank is connected by pipeline with the feeding mouth of filter press 60.
In said program, flocculant, flocculant and dirt are passed through into the first mixing tube 31 by flocculant feed unit 50
Mud mixes, and colloid and fine suspension in sludge is made tentatively to be gathered into the floccule body with separable characteristic, mixed with flocculant
Only it is to enter the floccule body of 40 bottom of settling tank, sludge pumping to filter press 60 in sludge pumping to settling tank 40 after conjunction
Material mouth greatly reduces treating capacity of the filter press 60 to sludge, improves the treatment effeciency of sludge, filter press 60 to mud in sludge,
Water is efficiently separated, and the dry mud convenience in transport after squeezing reduces the processing cost of sludge.
The second mixing tube 32, the mud inlet and settling tank of the second mixing tube 32 are laid between settling tank 40 and filter press 60
40 mud mouths, the connection of 50 discharge port of flocculant feed unit, the mud mouth of the second mixing tube 32 and the feeding mouth phase of filter press 10
Even.
The mixture water content of the sludge, floccule body that are pumped out by settling tank 40 reduces, by sludge, the mixture of floccule body
It is mixed again with flocculant through the second mixing tube 32, so that the Free water in sludge is precipitated, improve the squeezing effect of filter press.
The pipeline of first and second mixing tube 31,32 is in detour shape, and concentration is provided between the second mixing tube 32 and filter press 10
Machine 70, the feed inlet of thickener 70 are connected to the mud mouth of the second mixing tube 32, and 70 discharge end of thickener enters with filter press 10
Expect side linking.Material is delivered to thickener 70 through mud mouth after being handled in second mixing tube 32, and thickener 70 can be further
The water content in material is reduced, filter press 60 is reduced to the treating capacity of material, greatly improves the treatment effeciency of sludge.
As the specific medicament kind of flocculant and supply sequence, flocculant feed unit 50 includes PAM medicament blenders
The discharge port of 51 and PAC medicaments blender 52, PAM medicaments blender 51 connects with the feed inlet of the first and second mixing tube 31,32 respectively
Logical, medicament is sent into from the first and second mixing tube 31,32 middle section positions in tube chamber by PAC medicaments blender 52 respectively.PAM medicaments
PAM medicaments are added in blender 52, PAM is polyacrylamide, PAC medicaments is added in PAC medicaments blender 52, PAC is
Aluminium polychloride.
PAM medicaments are first passed through so that fine grained is initially formed bigger floc sedimentation in sludge, and accelerates the speed of precipitation, so
After be passed through PAC medicaments so that iron, fluorine, cadmium, radioactive pollution in muddy water, floating oil etc. are attached on floc sedimentation, pass sequentially through
Flocculant is added in first and second mixing tube 31,32 to be handled, ensures that the water after conditioning can reach processing requirement, Neng Gouzhi
It connects and drains back in river again, not only facilitate processing, but also prevent from causing secondary pollution to environment.
It is provided with partition board 43 in the settling tank 40 and settling tank is separated into the first and second chamber 41,42, institute by the partition board 43
31 mud mouth of the first mixing tube is stated by pipeline connection to first chamber 41, the liquid in first chamber 41 crosses 43 overflow of partition board
To second chamber 42, the liquid outlet on 42 top of second chamber by pipeline respectively with the filter cloth cleaning head of thickener 70, press filtration
Filter cloth cleaning head water inlet, the PAM medicaments blender 51 of machine 10 are connected with the inlet of PAC medicaments blender 52, the first and second chamber
Room 41,42 bottoms mud mouth be connected to 32 feed inlet of the second mixing tube.
It is delivered to during the first chamber 42 of settling tank 40 in first mixing tube 31, upsets in first chamber 41 and precipitated
Journey is normally carried out, and the upper materials in first chamber 41 are crossed in partition board 43 overflow to second chamber 42, such second chamber 42
Interior precipitation process is normally carried out, and supernatant liquor can be sent into PAM medicaments blender 51 and PAC medicament blenders in second chamber 42
In 52 filter is cleaned as the filter cloth cleaning head water inlet of the filter cloth cleaning head of solvent and feeding thickener 70, filter press 10
Cloth, the water in sludge can be efficiently utilized, and worker is not necessarily to volume external adding water, reduces the labor intensity of worker.
As 70 preferred arrangement of thickener, the thickener 70 includes channel-shaped rack 74, is arranged in channel-shaped rack 74
There is the slot that shaft core is mutually parallel and the filter cloth 71 of winding is located at channel-shaped rack 74 in two shafts of same level, two shafts
Intracavitary, is provided with cross bar 75 on the cell wall of channel-shaped rack 74, on cross bar 75 suspention have a head 73, head 73 in triangular prism shape and its
End face is connected with 72 rod end of connecting rod, other end is bonded with the side cloth cover of 71 support sludge of filter cloth, and head 73 is in filter cloth
71 cloth wide direction uniform intervals setting at least two.
Sludge on the filter cloth 71 of thickener 70, ooze out from filter cloth 71 under gravity by the Free water in sludge,
Reducing the water content in sludge, wherein head 73 is provided with two aspect effects, one is, sludge can be stirred, sludge is made
In Free water quickly ooze out;The second is head 73 plays the role of homocline, the in this way sludge on filter cloth 71 on filter cloth 71
It uniformly drops down onto on filter press 60, improves the press filtration effect of filter press 60.
The lower position of filter press 60 and thickener 70 is provided with water receiving tank 80, and the leakage fluid dram on 80 top of water receiving tank will be upper
Clear liquid discharge, bottom are connected to by pipeline with the feed inlet of the first mixing tube 31.
As the preferred embodiment of impurity knockout drum 20, the impurity knockout drum 20 includes tank body 21, is set in the tank body 21
It is equipped with the filter screen being consistent with 21 Internal periphery of tank body, wire side and tank skin arranged for interval in tank body 21, the slush pump of the filter screen
10 mud mouth is connected in the region that filter screen surrounds, and the mud inlet of the mud mouth of 21 bottom of tank body and the first mixing tube 31 connects
It is logical.Stone, branch stay in filter screen in this way, and sludge is sent into from the mesh of filter screen by and from the mud mouth of 21 bottom of tank body
First mixing tube 31.
A kind of Treatment of Sludge vehicle, including car bottom plate 90 are laid with precipitation on the car bottom plate 90 by headstock to tailstock sequence
The dry mud outlet of case 40, flocculant feed unit 50, impurity knockout drum 20 and filter press 60, filter press 60 is located at the tailstock, sinks
Case 40 top in shallow lake is laid with the first mixing tube 31, and 70 top of thickener is laid with the second mixing tube 32, impurity knockout drum 20 and pressure
It is disposed with thickener 70 above 60 pan feeding side of filter.Sludge treating system is compactly arranged on car bottom plate 90, sludge is reduced
The occupied space of processing system greatly facilitates sludge treating system and shifts, at sludge when needing the length for clearing up river longer
By Li Chekai to river, you can it directly works, without arranging the component in sludge treating system, reduces the labor intensity of worker,
Treatment of Sludge is quickly, efficiently.
The filter press 60 is belt filter press and it is close to 90 a side of car bottom plate arrangement, 90 another side cloth of car bottom plate
It is equipped with switch board 1, car bottom plate 90 and filter press are provided with water receiving tank 80 between 60 bottom.
Claims (10)
1. a kind of sludge treating system, it is characterised in that:The mud inlet of the mud mouth and impurity knockout drum (20) of slush pump (10)
It is connected, mud inlet and impurity knockout drum (20) mud mouth, flocculant feed unit (50) discharge port of the first mixing tube (31) connect
Logical, the mud mouth of the first mixing tube (31) is connected to settling tank (40) mud inlet, and the mud mouth of settling tank (40) bottom passes through pipe
Road is connected with the feeding mouth of filter press (60).
2. sludge treating system according to claim 1, it is characterised in that:Cloth between settling tank (40) and filter press (60)
Equipped with the second mixing tube (32), mud inlet and settling tank (40) mud mouth, the flocculant feed unit of the second mixing tube (32)
(50) discharge port is connected to, and the mud mouth of the second mixing tube (32) is connected with the feeding mouth of filter press (60).
3. sludge treating system according to claim 2, it is characterised in that:The pipeline of first and second mixing tube (31,32) is in
Detour shape is provided with thickener (70), the feed inlet of thickener (70) and between the second mixing tube (32) and filter press (60)
The mud mouth of two mixing tubes (32) is connected to, and thickener (70) discharge end is connected with the pan feeding side of filter press (60).
4. sludge treating system according to claim 2 or 3, it is characterised in that:Flocculant feed unit (50) includes PAM
Medicament blender (51) and PAC medicaments blender (52), the discharge port of PAM medicaments blender (51) are mixed with first and second respectively
The feed inlet connection of (31,32) is managed, PAC medicaments blender (52) is by medicament respectively from section in the first and second mixing tube (31,32)
Place is set to be sent into tube chamber.
5. sludge treating system according to claim 4, it is characterised in that:It is provided with partition board in the settling tank (40)
(43) and settling tank is separated into the first and second chamber (41,42) by the partition board (43), and the first mixing tube (31) mud mouth passes through
Pipeline connection to first chamber (41), cross in partition board (43) overflow to second chamber (42) by the liquid in first chamber (41),
The liquid outlet on second chamber (42) top by pipeline respectively with the filter cloth cleaning head of thickener (70), the filter cloth of filter press (60)
Cleaning head water inlet, PAM medicaments blender (51) are connected with the inlet of PAC medicaments blender (52), the first and second chamber (41,
42) mud mouth of bottom is connected to the second mixing tube (32) feed inlet.
6. sludge treating system according to claim 1, it is characterised in that:Thickener (70) includes channel-shaped rack (74),
It is provided with shaft core in channel-shaped rack (74) to be mutually parallel and positioned at two shafts of same level, the filter cloth of winding in two shafts
(71) it is located in the vallecular cavity of channel-shaped rack (74), cross bar (75) is provided on the cell wall of channel-shaped rack (74), is hanged on cross bar (75)
Head (73), head (73) connected, other end and filter cloth in triangular prism shape and one end and connecting rod (72) rod end are hung
(71) the side cloth cover fitting of support sludge, head (73) are arranged at least two in filter cloth (71) cloth wide direction uniform intervals.
7. sludge treating system according to claim 5, it is characterised in that:The lower part of filter press (60) and thickener (70)
Water receiving tank (80) is provided at position, supernatant discharge, bottom are passed through pipeline and first by the leakage fluid dram on water receiving tank (80) top
The feed inlet of mixing tube (31) is connected to.
8. sludge treating system according to claim 1, it is characterised in that:The impurity knockout drum (20) includes tank body
(21), the filter screen being consistent with tank body (21) Internal periphery, the wire side and tank body of the filter screen are provided in the tank body (21)
(21) mud mouth of interior tank skin arranged for interval, slush pump (10) is connected in the region that filter screen surrounds, tank body (21) bottom
Mud mouth is connected to the mud inlet of the first mixing tube (31).
9. a kind of Treatment of Sludge vehicle based on sludge treating system described in claim 1, it is characterised in that:Including car bottom plate
(90), settling tank (40), flocculant feed unit (50), impurity are laid with by headstock to tailstock sequence on the car bottom plate (90)
The dry mud outlet of knockout drum (20) and filter press (60), filter press (60) is located at the tailstock, and the is laid with above settling tank (40)
One mixing tube (31), thickener (70) top are laid with the second mixing tube (32), and impurity knockout drum (20) and filter press (60) enter
Material is disposed with thickener (70) above side.
10. Treatment of Sludge vehicle according to claim 9, it is characterised in that:The filter press (60) be belt filter press and
It arranges that car bottom plate (90) another side is disposed with switch board (1), car bottom plate (90) and press filtration close to car bottom plate (90) a side
It is provided with water receiving tank (80) between machine (60) bottom.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201820115472.5U CN208038286U (en) | 2018-01-24 | 2018-01-24 | Sludge treating system and Treatment of Sludge vehicle |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201820115472.5U CN208038286U (en) | 2018-01-24 | 2018-01-24 | Sludge treating system and Treatment of Sludge vehicle |
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CN208038286U true CN208038286U (en) | 2018-11-02 |
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CN201820115472.5U Active CN208038286U (en) | 2018-01-24 | 2018-01-24 | Sludge treating system and Treatment of Sludge vehicle |
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CN (1) | CN208038286U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110921799A (en) * | 2019-11-01 | 2020-03-27 | 象山德曼机械有限公司 | Eddy current solid-liquid separation device |
CN110981024A (en) * | 2019-12-25 | 2020-04-10 | 华东师范大学重庆研究院 | Movable garbage leakage liquid treatment equipment |
-
2018
- 2018-01-24 CN CN201820115472.5U patent/CN208038286U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110921799A (en) * | 2019-11-01 | 2020-03-27 | 象山德曼机械有限公司 | Eddy current solid-liquid separation device |
CN110981024A (en) * | 2019-12-25 | 2020-04-10 | 华东师范大学重庆研究院 | Movable garbage leakage liquid treatment equipment |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP02 | Change in the address of a patent holder |
Address after: 230000 industrial cluster, Zipeng Town, Feixi County, Hefei City, Anhui Province Patentee after: ANHUI TONGYUAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: 231202 zier Road, Taohua Industrial Park, Hefei City, Anhui Province Patentee before: ANHUI TONGYUAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |
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CP02 | Change in the address of a patent holder |