CN206580728U - The system of on-site slurry dehydration - Google Patents
The system of on-site slurry dehydration Download PDFInfo
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- CN206580728U CN206580728U CN201621476159.1U CN201621476159U CN206580728U CN 206580728 U CN206580728 U CN 206580728U CN 201621476159 U CN201621476159 U CN 201621476159U CN 206580728 U CN206580728 U CN 206580728U
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- 239000002002 slurry Substances 0.000 title claims abstract description 44
- 230000018044 dehydration Effects 0.000 title claims description 28
- 238000006297 dehydration reaction Methods 0.000 title claims description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 108
- 238000005189 flocculation Methods 0.000 claims abstract description 22
- 230000016615 flocculation Effects 0.000 claims abstract description 22
- 238000001125 extrusion Methods 0.000 claims abstract description 9
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- 238000005265 energy consumption Methods 0.000 abstract description 4
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Landscapes
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
Abstract
The utility model provides the system that a kind of on-site slurry is dehydrated, including the sifter for being removed the gred to mud, the slurry outlet connection flocculation concentration device of sifter, the outlet of sewer connection water leg of flocculation concentration device, the concentration slurry outlet of flocculation concentration device connects mixer entrance through slush pump, dispensing canister for configuring mud tackifier connects mixer entrance, the mud feed pipe connection of mixer outlet and mud dewatering apptss, the mud inlet of the walk outlet connection device for separating mud and water of mud dewatering apptss, the abjection water out connection water leg and dispensing canister of mud dewatering apptss, the mud mouth connection Spiral extrusion conveyor of device for separating mud and water.The system that the utility model is provided can realize mud live a large amount of, fast dewatering on the spot, and processing speed is more than 5 times of the conventional sheet frame filtration system of tradition, and floor space is only the 50% of conventional sheet frame filtration system, energy consumption is low, can continuously run, and simple and reliable, service life is long, and stability is good.
Description
Technical field
The system that the utility model is related to a kind of dehydration of on-site slurry, for river course, lake, drainage dredging and other
The discarded slurry that approach is produced, fast dewatering processing is carried out with producing in mud.
Background technology
River course, lake, drainage pipeline networks desilting be solve water body treating must be through step, but traditional Dredging Construction mode
Landfill disposal turns into pollution source to the mud of generation nearby, and the mud without producing secondary pollution focuses on mode then mud
Cost of transportation is high, speed is slow, land seizure is more, the bottleneck factor as restriction water body treating.
At present, the Dredging Construction mode for the non-secondary pollution that most of Dredging Construction enterprise uses is as follows：Built first
Dam stop operation, then break up bottom sludge using hydraulic giant, then by mud be drawn into tank car transport to Treatment stations store, finally
Sedimentation concentration and filter-press dehydration are carried out in Treatment stations to fill into mud cake outward transport.This traditional operating type takes time and effort, especially
Be slurry transportation link occupy processing cost more than half.
The method that can be dehydrated on the spot to mud in desilting site is still the bottleneck of dredging operation technology.It is clear at present
Silt slurry dehydration, which is also no lack of, there are some new techniques, such as folded spiral shell machine evaporation, but comparatively speaking, mud at present
Dehydration production or using the high energy consumptions such as traditional high-pressure filteration, centrifugal force separate, reduction process speed as main flow dewatering process.
First, conventional mud dewatering
There are high pressure sheet frame filtration method, sleeping spiral shell centrifugal separation, belt filter press technique using more mud dewaterion method at present
Deng.
1. high pressure sheet frame filtration method
High pressure plate-frame filtering is a kind of filtering dewatering method of batch (-type), is typically used to compare a small amount of slurry dewatering, greatly
The plate-frame filtering device of type is huge, and installed power is high, it is necessary to which firm carrying is basic.High pressure plate-frame filtering is generally adapted in fixation
Mud conditioning workshop in use, live simple and crude environment is used with being less compliant in desilting mud output.
2. sleeping spiral shell centrifugal separation
Sleeping spiral shell centrifugal separation is a kind of continuous filtering dewatering method, is generally used for small, a small amount of slurry dewatering of density,
Large-scale centrifuge is bulky, and installed power is very high, it is necessary to which the basis especially consolidated, is not suitable for often mobile place and uses.
Horizontal screw centrifuge is generally adapted to be used in fixed mud conditioning workshop, be not suitable for substantially desilting mud output it is existing
The simple and crude environment of field is used.
3. belt filter press technique
Belt filter press technique is a kind of filtering dewatering method of continous way, is typically used to compare at the slurry dewatering easily filtered
Reason.Large-scale belt filter press is bulky, and installation accuracy is high, and the technical requirements of maintenance maintenance are high, it is necessary to the carrying base consolidated
Plinth.Belt press filtration is generally adapted to be used in fixed mud conditioning workshop, is less compliant in the simple and crude of desilting mud output ground
Environment is used.
2nd, slurry dewatering new method
Above-mentioned mud dewaterion method is the widest main stream approach of current domestic application.In recent years, some new mud take off
Water method is also constantly being emerged in large numbers, than it is more typical be exactly folded spiral shell press dewatering method.
The main body of folded spiral shell squeezing dewatering machine is layered on top of each other by retainer ring and travelling ring, the mistake that helical axis is formed therethrough
Device is filtered, leading portion is concentrating part, and back segment is de-watering section, form filter seam between retainer ring and travelling ring, the pitch of helical axis is from dense
Contracting portion is tapered into de-watering section.After flocculation concentration, de-watering section is shifted onto by helical axis in concentrating part for mud, in the mistake of advance
As filter seam and pitch are tapered into journey, and back pressure plate barrier effect, produce great internal pressure, volume constantly contracts
It is small, reach the purpose being fully dehydrated.
Folded spiral shell press dewatering acc power is smaller, device volume is small, is increasingly becoming the head of sewage plant dehydrating residual active sludge
Choosing, but be due to its dehydration dependent on the filter seam abjection moisture formed between retainer ring and travelling ring, when there is sand in mud
When, tiny sand can be extruded in filter seam, cause filter seam to be stretched, and mud and water fold spiral shell directly from filtering in seam out
Press dewatering can not just be carried out；After other sand is entered in filter seam, ditch is ground on retainer ring, travelling ring and helical axis
Groove, retainer ring, travelling ring and helical axis are just scrapped and need to change.Due to a large amount of sands of generally existing in desilting mud,
And it is substantially totally unrealistic that these sands, which are removed, therefore the clear slurry dewatering effect of folded spiral shell machine is very unstable, main
Wanting part, the life-span is very short because of sand abrasion, so being still difficult in adapt to large-scale production and application at present.
Utility model content
The technical problems to be solved in the utility model is how to realize that a large amount of desilting mud are producing the live quick, low energy in ground
Consume, be stably dehydrated.
In order to solve the above-mentioned technical problem, what the technical solution of the utility model was to provide a kind of dehydration of on-site slurry is
System, it is characterised in that：Including the sifter for being removed the gred to mud, the slurry outlet of sifter connects flocculation concentration device,
The outlet of sewer connection water leg of flocculation concentration device, the concentration slurry outlet of flocculation concentration device enters through slush pump connection blender
The mud of mouth, the dispensing canister connection mixer entrance for configuring mud tackifier, mixer outlet and mud dewatering apptss enters
Expects pipe is connected, the mud inlet of the walk outlet connection device for separating mud and water of mud dewatering apptss, the abjection water of mud dewatering apptss
Outlet connection water leg and dispensing canister, the bucket that goes out of device for separating mud and water connect Spiral extrusion conveyor；
Mud dewatering apptss include rotating cylinder and the drive device for driving rotating cylinder to rotate；Rotating cylinder is by rotating cylinder straight length and turns
Cylinder Taper Pipe section is formed by connecting, and the rotating cylinder straight length other end goes out provided with abjection water overfall, the rotating cylinder Taper Pipe section other end provided with walk
Mouthful；Rotating cylinder straight length and rotating cylinder Taper Pipe section inwall are equipped with spiral plate, and it is exported from abjection water overfall to walk in rotating cylinder
Between formed through helical duct；Mud feed pipe is out of abjection water overfall insertion rotating cylinder straight length；
Device for separating mud and water includes screen drum and the drive device for driving screen drum to rotate；Screen drum two ends are provided with baffle plate, one
The baffle plate at end is provided with mud inlet, and the baffle plate of the other end is provided with mud mouth；The screen cloth face of screen drum encompasses spiral shell by stainless steel wire
Shape is revolved to constitute.
Preferably, the drive device for being used to drive rotating cylinder to roll includes the roller located at the cylinder bottom, described
Rotating cylinder outer wall is supported on roller circumferentially arranged with rotation track, rotating cylinder by rotation track, roller connection motor.Roller
By driving rotating cylinder to be rotated along rotation track with the frictional force of rotation track.
Preferably, the range of speeds of the rotating cylinder is 0~10rpm.
Preferably, the cone angle of the rotating cylinder Taper Pipe section is 10 °~90 °.
Preferably, the helical duct insertion of the through of the spiral plate formation in the rotating cylinder straight length extends to overflow
The helical duct insertion of the through of spiral plate formation in delivery port, rotating cylinder Taper Pipe section extends to walk outlet.
Preferably, in rotating cylinder Taper Pipe section, the outlet from one end be connected with rotating cylinder straight length to walk, helical duct by
Contracting is tapered to diminish.
Preferably, the depth of the plug-in type mud feed pipe insertion rotating cylinder straight length is the 20% of rotating cylinder flow development length
~100%；Spacing is kept between the plug-in type mud charging pipe outer wall and abjection water overfall.
Preferably, it is provided with the adverse current for being used to assemble and guiding abjection water to be flowed to overfall direction in the rotating cylinder Taper Pipe section
Inner cylinder.
Preferably, the adverse current inner cylinder is in funnel-form, is that one section of continuous contraction or point multistage shrink；Adverse current inner cylinder perisporium is close
Cloth is easy to the hole that water body enters.
It is highly preferred that the maximum gauge of the adverse current inner cylinder is less than or equal to the spiral plate open interior diameter of rotating cylinder straight length
D, a diameter of 1.1d~10d of rotating cylinder straight length, adverse current inner cylinder minimum diameter are 0.05d~0.5d, and adverse current inner cylinder length is to turn
0.2~2 times of cylinder Taper Pipe segment length, the diameter ratio of rotating cylinder total length and rotating cylinder straight length is 1~10, and the pitch of spiral plate is
0.05d~0.5d.
Preferably, the drive device for being used to drive screen drum to rotate includes the roller located at the screen drum bottom, described
Screen drum outer wall is supported on roller circumferentially arranged with guide groove, screen drum by guide groove, roller connection motor；Roller passes through
Screen drum is driven to be rotated along guide groove with the frictional force of guide groove；
Preferably, a row or multi-row recoil cleaning sprayer is distributed with outside the screen drum in the axial direction, recoil cleaning sprayer
It is connected to provide the air inlet pipe of compressed air and/or for providing the water inlet pipe with pressure rinse water, so as to the non-of screen drum
Filtering position carries out sieve aperture dredging from outside to inside.
Preferably, the mud mouth bottom is provided with bucket.
Preferably, the range of speeds of the screen drum is 0~10rpm.
Preferably, the section of the stainless steel wire is trapezoidal.
Preferably, the bar shaped screen hole formed between the stainless steel wire of adjacent turn is interior narrow outer width structure.
Preferably, it is outside provided with axial brace rod on the screen cloth face.
Preferably, the draw ratio of the screen drum is 1~10.
The utility model additionally provides a kind of method of on-site slurry dehydration, using the system of above-mentioned on-site slurry dehydration,
It is characterised in that it includes following steps：
Step 1：Flocculant is added after the screened device slagging-off of mud, is well mixed and flows into flocculation concentration device, flocculate dense
The sewage that contracting device is separated is discharged to water leg, and the concentration mud that flocculation concentration device is separated drains into blender through slush pump
In；
Step 2：The tackifier of dispensing canister configuration are added in blender, and are well mixed, the mud of viscosity is formed；
Step 3：The mud of viscosity enters in mud dewatering apptss, because the particle surface in mud has viscosity, is turning
Cylinder is with the mud rotary course in it, and the particle in mud is mutually bonded, rolling is rubbed and grows up into walk, and walk is swept along
Dampening is bored the outlet of tube section ends walk through rotating cylinder and extruded, into the mud inlet of device for separating mud and water；Walk is in rotary course simultaneously
In, the abjection water under own wt extruding flows out from the abjection water overfall of rotating cylinder straight length end；Deviate from water part conveying
Into dispensing canister, the water that remainder is discharged in water leg, water leg is discharged or used as erosion and deposition water on the spot；
Step 4：In device for separating mud and water, screen drum rotation, the water that walk is swept along is sized away inflow water leg, walk patch
Screen cloth face rolling, and using spiral helicine stainless steel wire provide thrust moved to mud mouth direction, final dewatering sludge from
Mud mouth is discharged；
Step 5：The walk discharged from device for separating mud and water by Spiral extrusion conveyor is finally dehydrated into clod, and fills
Car is transported outward.
Preferably, in the step 2, tackifier are one or more of mixed in polyacrylonitrile, polyacrylamide, glycan
Compound.
The system that the utility model is provided overcomes the deficiencies in the prior art, and can realizing mud, scene is a large amount of, fast on the spot
Speed dehydration, compared to the system of the conventional sheet frame filtration treatment of more equal installed power, the system processing speed reaches more than 5 times,
Spiral shell dewaterer is folded relatively reaches more than 2.5 times, and floor space is only the 50% of conventional sheet frame filtration treatment method, and energy consumption
It is low, can continuously it run, simple and reliable, service life is long, stability is good.
Brief description of the drawings
Fig. 1 is the system schematic that on-site slurry is dehydrated；
Fig. 2 is the section shaft side figure of mud dewatering apptss 1/4；
Fig. 3 is device for separating mud and water shaft side figure；
Fig. 4 is screen cloth face structural representation.
Embodiment
With reference to specific embodiment, the utility model is expanded on further.It should be understood that these embodiments are merely to illustrate this
Utility model rather than limitation scope of the present utility model.In addition, it is to be understood that reading the content of the utility model instruction
Afterwards, those skilled in the art can make various changes or modifications to the utility model, and these equivalent form of values equally fall within this Shen
Please appended claims limited range.
Fig. 1 is the system structure diagram that on-site slurry is dehydrated, the system of described on-site slurry dehydration by sifter 1,
Flocculation concentration device 2, water leg 3, slush pump 4, blender 5, quenched medicament dispensing canister 6, mud dewatering apptss 7, mud-water separation dress
Put the composition such as 8, Spiral extrusion conveyor 9.
Sifter 1 is used to remove the gred to mud, the slurry outlet connection flocculation concentration device 2 of sifter 1, flocculation concentration device
2 outlet of sewer connection water leg 3, the concentration slurry outlet of flocculation concentration device 2 connects the entrance of blender 5 through slush pump 4, made up a prescription
Tank 6 connects the entrance of blender 5, and the outlet of blender 5 is connected with the mud feed pipe of mud dewatering apptss 7, mud dewatering apptss 7
The mud inlet of walk outlet connection device for separating mud and water 8, the abjection water out of mud dewatering apptss 7 connects water leg 5 and made up a prescription
Tank 6, the mud mouth connection Spiral extrusion conveyor 9 of device for separating mud and water 8.
The porch of flocculation concentration device 2, which is provided with mixing chamber, mixing chamber, is provided with agitator 21, and mixing chamber is additionally provided with flocculant and added
Entrance.Gap 22 is provided with the top of the exit of flocculation concentration device 2, the bottom of flocculation concentration device 2 is provided with concentration slurry outlet 23.
Dispensing canister 6 is used for the tackifier for being allocated to mud thickening.
With reference to Fig. 2, mud dewatering apptss 7 are by plug-in type mud feed pipe 71, abjection water overfall 72, rotating cylinder straight length
73rd, the first return idler 74, the first active roller 75, rotation track 76, rotating cylinder Taper Pipe section 77, walk outlet 78, adverse current inner cylinder
79 grades are constituted.
Rotating cylinder is formed by connecting by rotating cylinder straight length 73 and rotating cylinder Taper Pipe section 77, and the other end of rotating cylinder straight length 73 is provided with abjection water
Overfall 72, rotating cylinder Taper Pipe 77 other ends of section are provided with walk outlet 78.The cone angle of rotating cylinder Taper Pipe section 77 is at 10 °~90 °.Rotating cylinder is straight
Pipeline section 73 and rotating cylinder Taper Pipe 77 inwalls of section are equipped with the spiral shell of the through of the spiral plate formation in spiral plate, rotating cylinder straight length 73
The helical duct of the through for the spiral plate formation that rotation passage insertion is extended in overflow delivery port 72, rotating cylinder Taper Pipe section 77 is passed through
It is logical to extend to walk outlet 78, the spiral that through is formed between 78 is exported from abjection water overfall 72 to walk in rotating cylinder
Passage.
Cylinder bottom is provided with the first return idler 74 and the first active roller 75, and rotating cylinder outer wall is provided with rotation track 76, turns
The rotation track 76 of cylinder is supported on the first return idler 74 and the first active roller 75.Roller with rotation track 76 by rubbing
Wiping power drives rotating cylinder to rotate, the power needed for the offer rotation of the first active roller 75, the first passively rotation of return idler 74, and with
First active roller 75 supports rotating cylinder together.The rotating speed of rotating cylinder, rotating speed are controlled by adjusting the rotating speed of the first active roller 75
Scope is 0~10rpm.
Plug-in type mud feed pipe 11 is out of the abjection insertion rotating cylinder of water overfall 72 straight length 73, and insertion depth is that rotating cylinder is straight
The 20%~100% of pipeline section 73.Plug-in type feed pipe 71, which is used to send into mud in rotating cylinder, to be fed, and passes through helical duct, mud
Interior particle is mutually bonded, rolling is rubbed and grows up into walk, and walk rolls the stillpot for growing up and being deposited in portion under water, is being turned
Helical duct formation promotes walk to go out to walk from rotating cylinder straight length 73 to the motive force in 77 directions of rotating cylinder Taper Pipe section during cylinder rotation
Mouth 78 is moved.Walk is moved to after rotating cylinder Taper Pipe section 77, and its inner passage, which is gradually tapered up, to diminish, and finally extends to walk outlet
78, walk extrudes rotating cylinder and is dehydrated, and finally discharges rotating cylinders from walk outlet 78.
Adverse current inner cylinder 79 is in rotating cylinder Taper Pipe section 77, and adverse current inner cylinder 79 is in funnel-form (one end close to walk outlet 78
Opening is smaller), gather aperture thereon, and the abjection water of adverse current enters adverse current inner cylinder 79 to abjection water overfall 72 direction stream from aperture
It is dynamic.Spacing is kept between the outer wall of plug-in type mud feed pipe 71 and abjection water overfall 72, abjection water is overflow from abjection water
Head piece 72 smoothly flows out.
The internal diameter of adverse current inner cylinder 79 can be that one section of continuous contraction or point multistage shrink, and the maximum diameter of adverse current inner cylinder 79 is small
In or equal to rotating cylinder straight length 73 spiral plate open interior diameter d, a diameter of 1.1d~10d of rotating cylinder straight length 73, adverse current in
A diameter of 0.05d~0.5d at the minimum of cylinder 79, the length of adverse current inner cylinder 79 is 0.2~2 times of rotating cylinder Taper Pipe 77 length of section, and rotating cylinder is total
The diameter ratio of length and rotating cylinder straight length 73 is 1~10, and spiral plate pitch is 0.05d~0.5d.
Mud dewatering apptss are in use, the first active roller 75 drive rotating cylinder plays auxiliary along the low speed rotation of rotation track 76
Support the first return idler 74 also synchronous rotary of rotating cylinder；Mud is fed after adding glutinous medicament to adjust by plug-in type mud
Pipe 71 enters rotating cylinder straight length 73, and the rotation of rotating cylinder drives mud to rotate together, and the spiral by the spiral plate formation in rotating cylinder leads to
Road is constrained, and mud exports 78 directions to walk and promoted；During rotation, using sand present in mud as core, mud
Middle sticky flco is adsorbed onto in these cores more and more turns into walk, and walk is grown up as snowball, and walk is continuous
Water therein is extruded in increased deadweight；Walk is moved to after rotating cylinder Taper Pipe section 77, and the passage of the spiral plate formation in it is gradually
Contraction diminishes, and walk is squeezed further dehydration, finally discharges Taper Pipes section 77 from walk outlet 78；Muddy water is in rotating cylinder Taper Pipe section 77
While movement to walk outlet 78, muddy water liquid level is lifted to the height adverse current backward more than spiral plate, and adverse current inner cylinder 79 is in
Funnel-form, gather aperture thereon, and the abjection water of adverse current enters adverse current inner cylinder 79 to the flowing of abjection water overfall 72 direction from aperture；
In rotating cylinder straight length 73, abjection water crosses the spiral plate reverse flow in it step by step, real from the abjection outflow rotating cylinder of water overfall 72
Now deviate from the unpowered discharge of water.
Under this dewatering type, with constantly growing up for walk, walk surface area is doubled and redoubled, in walk adhesion mud
The speed of particle is faster, is being accelerated as snowball, thus device can be easily achieved it is quick, be located on a large scale
Mud is managed, while the gravity that dehydration relies primarily on walk itself extrudes to complete, therefore the energy consumption of dehydration is very low.
With reference to Fig. 3, device for separating mud and water 8 is by mud inlet 81, baffle plate 82, screen drum 83, guide groove 84, the second active roller
85th, the group such as the second return idler 86, mud mouth 87, bucket 88, screen cloth face 89, recoil cleaning sprayer 810, air inlet/water inlet pipe 811
Into.
The two ends of screen drum 83 are equipped with to be provided with mud inlet 81, the baffle plate 82 of the other end on baffle plate 82, the baffle plate 82 of one end and are provided with
Mud mouth 87.The bottom of mud mouth 87 is provided with bucket 88.
Circumferentially arranged with two circle guide grooves 84, second the 85, second driven rolling of active roller outside the screen cloth face 89 of screen drum 83
The arrangement of wheel 86 and the bottom of screen drum 83, screen drum 83 are supported on the second active roller 85, on the second return idler 86 by guide groove 84.
Roller is controlled by driving screen drum 3 to rotate with the frictional force of rail groove 86 by adjusting the rotating speed of the second active roller 85
The rotating speed of screen drum 83, the range of speeds of screen drum 83 is 0~10rpm.
With reference to Fig. 4, screen cloth face 89 is constituted using the stainless steel wire 812 of trapezoidal cross-section around curl, and adjacent turn is not
The bar shaped screen hole 814 formed between rust steel wire is interior narrow outer width structure.When walk moving direction and the circular spiral of stainless steel wire
When direction is identical, the helical form stainless steel wire on screen cloth face 89 is provided when rotating promotes walk toward moving that the direction of mud mouth 87 is moved
Power.
It is outside equipped with axial brace rod 813 on screen cloth face 89, to ensure the intensity in screen cloth face.
The draw ratio of screen drum 83 is 1~10.
Device for separating mud and water in use, the second active roller 85 drive screen drum 83 rotated along guide groove 84, rise Auxiliary support
The return idler 86 of effect is also driven synchronous rotary；Take cement group from mud inlet 81 to enter after the screen drum 83 of rotation, screen drum
83 with the rotation of cement group is taken, and the water that walk is carried is filtered out by the sieve aperture on screen cloth face 89；Baffle plate 82 and the spiral of screen cloth face 89
The thrust that line rotation is produced makes walk be moved to the direction of mud mouth 87, and rolls out from mud mouth 87 defeated to outside bucket 88.
In order to prevent the sieve aperture on silt blocking screen wire side 89, the drainage capacity of screen drum 83 is influenceed, in the outer axle of screen drum 83
Line directional spreding has a row or multi-row recoil cleaning sprayer 810, and recoil cleaning sprayer 810 provides pressure by air inlet/water inlet pipe 811
Contracting air/band pressure rinse water, sieve aperture dredging is carried out to the non-filtered position of screen drum 83 from outside to inside.
With specific embodiment, the utility model is described in further detail below.
Embodiment 1
A kind of system of on-site slurry dehydration, as shown in Figure 1.
A) by 60m3The somewhere desilting mud of aqueous the 98.0% of/H enters sifter, and pipe may be blocked or damage by screening out
The slag thing of pipeline equipment, mud flows into tank diameter and adds flocculant poly iron chloride, and agitator mixes flocculant and mud
It is uniform and carry out flocculation reaction, overflow water outlet 30m3/ H, the mud of bottom concentration is aqueous to reach 96.0%；
b)30m3/ H concentration mud enters slurry dewatering by the lifting of pump and the solution of addition polyacrylonitrile after mixing
Overflow water outlet 18.6m during device, rotation3/ H, fraction overflow water is back to the dispensing canister of quenched tackifier, and walk enters
Enter device for separating mud and water；
C) in device for separating mud and water, rotary screen shaft screen removes the water swept along in walk, obtains aqueous 75.5% walk
4.9m3/H。
D) Spiral extrusion conveyor finally removes a small amount of water, obtains aqueous 72.7% clod 4.4m3/H。
Embodiment 2
A kind of system of on-site slurry dehydration, as shown in Figure 1.
A) by 60m3The somewhere desilting mud of aqueous the 96.0% of/H enters sifter, and pipe may be blocked or damage by screening out
The slag thing of pipeline equipment, mud flows into tank diameter and adds flocculant poly iron chloride, and agitator mixes flocculant and mud
It is uniform and carry out flocculation reaction, overflow water outlet 12m3/ H, the mud of bottom concentration is aqueous to reach 95.0%；
b)48m3/ H concentration mud is de- into mud after mixing by the lifting of pump and the solution of addition polyacrylamide
Overflow water outlet 30m during water installations, rotation3/ H, fraction overflow water is back to the dispensing canister of quenched tackifier, and walk enters
Enter device for separating mud and water；
C) in device for separating mud and water, rotary screen shaft screen removes the water swept along in walk, obtains aqueous 75.0% walk
9.6m3/H。
D) Spiral extrusion conveyor finally removes a small amount of water, obtains aqueous 72.4% clod 8.7m3/H。
Embodiment 3
A kind of system of on-site slurry dehydration, as shown in Figure 1.
A) by 60m3The somewhere desilting mud of aqueous the 94.0% of/H enters sifter, and pipe may be blocked or damage by screening out
The slag thing of pipeline equipment, mud flows into tank diameter and adds flocculant poly iron chloride, and agitator mixes flocculant and mud
It is uniform and carry out flocculation reaction, overflow water outlet 4m3/ H, the mud of bottom concentration is aqueous to reach 93.6%；
b)56m3/ H concentration mud is entered slurry dewatering and filled by the lifting of pump and the solution of addition glycan after mixing
Put, overflow water outlet 35m during rotation3/ H, fraction overflow water is back to the dispensing canister of quenched tackifier, and walk enters mud
Water separation device；
C) in device for separating mud and water, rotary screen shaft screen removes the water swept along in walk, obtains aqueous 74.3% walk 14m3/
H。
D) Spiral extrusion conveyor finally removes a small amount of water, obtains aqueous 72.3% clod 13m3/H。
In the step a) of various embodiments above, sifter has used vibration separation screen, the slag thing screened out include broken plastic sheet,
Broken fiber, handstone, small fragment of brick and cement block etc.；Overflow water is entered flow and the unstable shadow of solid content by desilting mud
Ring, the flow being previously mentioned is the specified treating capacity of certain specific system, is average discharge in 8 hours, the mud being previously mentioned is aqueous
Rate is the average value in 8 hours.
In various embodiments above step b), overflow Water circulation amount is set according to the demand of dispensing canister, slurry material composition
Composition needs to match the specific kind of quenched medicament and addition, is generally specifically determined by compatibility mechanism.
In various embodiments above step d), the content of the moisture content of the dewatering cake finally given and organic matter in former mud
Correlation, the content of organic matter is lower, and obtained dewatering cake moisture content is lower.
Using system of the present utility model, realize to on-site slurry fast dewatering, it is normal compared to more equal installed power
The system of straightedge frame filtration treatment, the system processing speed reaches more than 5 times (folding spiral shell dewaterer relatively, reach more than 2.5 times),
And floor space is only the 50% of conventional sheet frame filtration treatment method, preferable technique effect is achieved.
Claims (10)
1. a kind of system of on-site slurry dehydration, it is characterised in that：Including the sifter (1) for being removed the gred to mud, sieve
Divide the slurry outlet connection flocculation concentration device (2) of device (1), the outlet of sewer connection water leg (3) of flocculation concentration device (2), flocculation
The concentration slurry outlet of inspissator (2) connects blender (5) entrance through slush pump (4), for configuring making up a prescription for mud tackifier
Tank (6) connects blender (5) entrance, and blender (5) outlet is connected with the mud feed pipe of mud dewatering apptss (7), and mud takes off
The mud inlet of the walk outlet connection device for separating mud and water (8) of water installations (7), the abjection water out of mud dewatering apptss (7) connects
Connect water leg (3) and dispensing canister (6), the mud mouth connection Spiral extrusion conveyor (9) of device for separating mud and water (8)；
Mud dewatering apptss (7) include rotating cylinder and the drive device for driving rotating cylinder to rotate；Rotating cylinder is by rotating cylinder straight length (73)
It is formed by connecting with rotating cylinder Taper Pipe section (77), rotating cylinder straight length (73) other end is provided with abjection water overfall (72), rotating cylinder Taper Pipe section
(77) other end is provided with walk outlet (78)；Rotating cylinder straight length (73) and rotating cylinder Taper Pipe section (77) inwall are equipped with spiral plate,
Form the helical duct of through in rotating cylinder between outlet (78) from abjection water overfall (72) to walk；Mud feed pipe
(71) out of abjection water overfall (72) insertion rotating cylinder straight length (73)；
Device for separating mud and water (8) includes screen drum (83) and the drive device for driving screen drum (83) to rotate；Screen drum (83) two ends
Provided with baffle plate (82), the baffle plate (82) of one end is provided with mud inlet (81), and the baffle plate (82) of the other end is provided with mud mouth (87)；
The screen cloth face (89) of screen drum (83) is made up of stainless steel wire (812) around curl.
2. a kind of system of on-site slurry dehydration as claimed in claim 1, it is characterised in that：It is described to be used to drive rotating cylinder to roll
Drive device include located at the cylinder bottom the first roller, the rotating cylinder outer wall circumferentially arranged with rotation track (76),
Rotating cylinder is supported on the first roller by rotation track (76), the first roller connection motor；First roller by with rotation
The frictional force of track (76) drives rotating cylinder to be rotated along rotation track (76)；
The drive device for being used to drive screen drum (83) to rotate includes the second roller located at the screen drum (83) bottom, described
Screen drum (83) outer wall is supported on the second roller circumferentially arranged with guide groove (84), screen drum (83) by guide groove (84), and second
Roller connects motor；Second roller with the frictional force of guide groove (84) by driving screen drum (83) to be revolved along guide groove (84)
Turn.
3. a kind of system of on-site slurry dehydration as claimed in claim 1, it is characterised in that：The rotating speed model that the rotating cylinder is rolled
Enclose for 0~10rpm, the range of speeds of the screen drum (83) is 0~10rpm.
4. a kind of system of on-site slurry dehydration as claimed in claim 1, it is characterised in that：In the rotating cylinder Taper Pipe section (77)
Provided with for assembling and guiding abjection water to the adverse current inner cylinder (79) of abjection water overfall (72) direction flowing.
5. a kind of system of on-site slurry dehydration as claimed in claim 4, it is characterised in that：The adverse current inner cylinder (79) is in leakage
It is bucket-shaped, it is that one section of continuous contraction or point multistage shrink；Adverse current inner cylinder (79) perisporium, which gathers, is easy to the hole of water body entrance.
6. a kind of system of on-site slurry dehydration as claimed in claim 1, it is characterised in that：In the rotating cylinder straight length (73)
The helical duct insertion of through of spiral plate formation extend in abjection water overfall (72), rotating cylinder Taper Pipe section (77)
The helical duct insertion of the through of spiral plate formation extends to walk outlet (78).
7. a kind of system of on-site slurry dehydration as claimed in claim 1, it is characterised in that：The rotating cylinder Taper Pipe section (77)
It is interior, (78) are exported from the one end being connected with rotating cylinder straight length (73) to walk, helical duct, which is gradually tapered up, to diminish.
8. a kind of system of on-site slurry dehydration as claimed in claim 1, it is characterised in that：The stainless steel wire (812)
Section is trapezoidal；The bar shaped screen hole (814) formed between the stainless steel wire (812) of adjacent turn is interior narrow outer width structure.
9. a kind of system of on-site slurry dehydration as claimed in claim 1, it is characterised in that：Set outside the screen cloth face (89)
There is axial brace rod (813).
10. a kind of system of on-site slurry dehydration as claimed in claim 1, it is characterised in that：Screen drum (83) outer axle
Line directional spreding has a row or multi-row recoil cleaning sprayer (810), and recoil cleaning sprayer (810) is connected to provide compressed air
Air inlet pipe and/or for providing the water inlet pipe with pressure rinse water.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621476159.1U CN206580728U (en) | 2016-12-30 | 2016-12-30 | The system of on-site slurry dehydration |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621476159.1U CN206580728U (en) | 2016-12-30 | 2016-12-30 | The system of on-site slurry dehydration |
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ID=60109862
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106673394A (en) * | 2016-12-30 | 2017-05-17 | 吴惠霞 | System and method for dewatering in slurry field |
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2016
- 2016-12-30 CN CN201621476159.1U patent/CN206580728U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106673394A (en) * | 2016-12-30 | 2017-05-17 | 吴惠霞 | System and method for dewatering in slurry field |
| CN106673394B (en) * | 2016-12-30 | 2023-08-04 | 吴惠霞 | System and method for on-site dehydration of slurry |
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Effective date of registration: 20230912 Address after: Room 401, No. 52, Lane 1323, Wan'an Road, Hongkou District, Shanghai, 200434 Patentee after: Wang Feng Address before: Room 307, No. 3843, Pudong South Road, Pudong New Area, Shanghai, 200120 Patentee before: Wu Huixia Patentee before: SHANGHAI ZHONGLI ENVIRONMENTAL TECHNOLOGY Co.,Ltd. |
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Effective date of registration: 20231025 Address after: No.23076, Building 2, No. 5 Xindong Road, Development Zone, Nantong City, Jiangsu Province, 226010 Patentee after: Jiangsu Yuneng Technology Co.,Ltd. Address before: Room 401, No. 52, Lane 1323, Wan'an Road, Hongkou District, Shanghai, 200434 Patentee before: Wang Feng |
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