CN105923703A - Cyclone slag removing and collecting device - Google Patents
Cyclone slag removing and collecting device Download PDFInfo
- Publication number
- CN105923703A CN105923703A CN201610435359.0A CN201610435359A CN105923703A CN 105923703 A CN105923703 A CN 105923703A CN 201610435359 A CN201610435359 A CN 201610435359A CN 105923703 A CN105923703 A CN 105923703A
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- China
- Prior art keywords
- slagging
- collection device
- eddy flow
- sewage
- separator
- 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.)
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Classifications
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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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
Abstract
The invention provides a cyclone slag removing and collecting device, and belongs to the field of treatment of sewage. The cyclone slag removing and collecting device comprises an eddy separator, a communication tube and a spiral gathering device, wherein the eddy separator is provided with a separating cavity and a slag discharging opening; the cross section of the separating cavity is circular; the spiral gathering device comprises a gathering device shell, spiral rotating blades, a rotating shaft and driving equipment driving the rotating shaft to rotate; the rotating blades and the rotating shaft are arranged in the gathering device shell; the rotating blades are arranged on the rotating shaft; a liquid outlet and a liquid inlet are formed in the gathering device shell; one end of the communication tube is connected with the liquid outlet; and the other end of the communication tube extends into the separating cavity and is tangent to the inner side wall of the eddy separator. By the cyclone slag removing and collecting device, time of separation of sewage and scum in the eddy separator can be shortened effectively, and treatment efficiency of the scum in the sewage is improved. In addition, by the cyclone removing and collecting device, mass flow of sewage and scum are collected automatically, and investment cost of sewage treatment is greatly reduced.
Description
Technical field
The present invention relates to sewage treatment area, in particular to a kind of eddy flow slagging-off collection device.
Background technology
Generally, the sewage of oil-containing and scum silica frost is discharge when, in order to avoid causing environmental pollution, and meeting
Oil contained in water and scum silica frost is removed by sewage disposal device.At present, conventional equipment is for coalescence tiltedly
Plate settling tank, although this equipment can shorten the time of sewage sedimentation, but this equipment is when long
Between use after, sewage treating efficiency is low, it is impossible to completely remove the oil in water and scum silica frost, and follow-up place
The fund input of reason is big, is unfavorable for life-time service.
Summary of the invention
The invention provides a kind of eddy flow slagging-off collection device, it is intended to improve the floating of existing deslagging device
The inefficient problem of Slag treatment.
The present invention is achieved in that
A kind of eddy flow slagging-off collection device, including whirlpool separator, communicating pipe and helix poly storage,
Whirlpool separator has separation cavity and slag-drip opening, and the cross section separating cavity is circular, spiral
Collector includes that collector housing, spiral helicine rotating vane, rotating shaft and drive shaft rotate
Driving equipment, rotating vane and rotating shaft be arranged in collector housing, and rotating vane is arranged at
Rotating shaft, collector housing is provided with liquid outlet and inlet, and one end of communicating pipe is connected with liquid outlet,
The other end of communicating pipe stretches into separation cavity tangent with the medial wall of whirlpool separator.
Further, in preferred embodiment of the present invention, the close inlet of above-mentioned rotating vane
Side be impingement area, rotating vane is provided with multiple boss, and boss is positioned at impingement area place
Side.
Further, in preferred embodiment of the present invention, above-mentioned communicating pipe includes interconnective
Straight tube and bend pipe, straight tube stretches into separation cavity along the tangential direction of whirlpool separator, bend pipe with go out
Liquid mouth connects.
Further, in preferred embodiment of the present invention, the medial wall of above-mentioned whirlpool separator sets
Being equipped with conducting element, conducting element is the circumferentially extending arc knot of the medial wall along whirlpool separator
Structure, conducting element has importing end and derives end, imports end near the exit of communicating pipe.
Further, in preferred embodiment of the present invention, the central angle of above-mentioned conducting element is 160
Degree-200 degree.
Further, in preferred embodiment of the present invention, above-mentioned conducting element is mozzle or water conservancy diversion
Plate.
Further, in preferred embodiment of the present invention, above-mentioned collector housing is tubulose, poly-
Storage housing includes the first housing and the second housing removably connected, and liquid outlet is arranged at second
Housing, inlet is arranged at the first housing.
Further, in preferred embodiment of the present invention, above-mentioned eddy flow slagging-off collection device also wraps
Including scum silica frost collecting tank, scum silica frost collecting tank is provided with charging aperture, is provided with between charging aperture and slag-drip opening
Scum pipe.
Further, in preferred embodiment of the present invention, above-mentioned eddy flow slagging-off collection device also wraps
Including skid base, whirlpool separator, helix poly storage and scum silica frost collecting tank are mounted on skid
Base.
Further, in preferred embodiment of the present invention, it is provided with bottom above-mentioned scum silica frost collecting tank
Leakage fluid dram, leakage fluid dram is connected with inlet.
The invention has the beneficial effects as follows:
The eddy flow slagging-off collection device that the present invention is obtained by above-mentioned design, whirlpool separator and helix poly
Storage was interconnected by communicating pipe.Whirlpool separator has shell separator and separates cavity.
Disengagement chamber body is positioned at inside shell separator, and the cross section separating cavity is circular, separates cavity
Offer place is separated with scum silica frost for water in sewage.Slag-drip opening connects with separating cavity, is separating
The scum silica frost being separated from water in cavity is discharged from slag-drip opening.
Helix poly storage is in an auxiliary equipment outside whirlpool separator, is conducive to into one
Step improves the separation efficiency of scum silica frost and water.Rotating vane in helix poly storage is helical form, rotation
Rotating vane sheet is fixing with rotating shaft to be connected, when rotating shaft is at when being rotated by of equipment of driving, pivoting leaf
Sheet is driven by rotating shaft and rotates along direction clockwise or counter-clockwise.The inlet of collector housing with
Oral siphon connects, and the liquid outlet of collector housing was connected with communicating pipe.Communicating pipe is away from liquid outlet
One end stretch into separation cavity tangent with the medial wall of whirlpool separator.
In use, sewage is drained in the housing of helix poly storage from inlet by oral siphon,
Driving device drives rotating shaft in helix poly storage is rotated blade and rotates, by sewage from feed liquor
Mouthful drain into liquid outlet, with after drain in whirlpool separator through communicating pipe.Because rotating vane is spiral
Shape, the sewage discharged from communicating pipe has the inertia force being threadingly advanced.Due to communicating pipe and eddy current
The medial wall of separator is tangent, and the sewage discharged from communicating pipe can continue under the effect of inertia force
Along the medial wall rotary motion of whirlpool separator and form eddy current.During sewage rotates,
Under the influence of centrifugal force, owing to the density of water is big compared with oily and scum silica frost density, whirlpool can be thrown to
The medial wall of stream separator, and scum silica frost and the oily center that can be gathered in whirlpool separator, and along with
The rising of water level in whirlpool separator, discharges from slag-drip opening under the effect of buoyancy of water.Eddy current
Water processed in separator can be after outlet from the middle and lower part of equipment discharges, under entrance
Unit one carries out advanced treating.
This eddy flow slagging-off collection device, by setting up helix poly storage in the outside of whirlpool separator,
There is provided power for sewage separation in whirlpool separator, effectively shorten in whirlpool separator sewage with
The disengaging time of scum silica frost, improves the treatment effeciency of scum silica frost in sewage.Additionally, the slagging-off of this eddy flow is received
Acquisition means, it is achieved that the automatic collection of the sewage scum of big flow, greatly reduces sewage disposal
Cost of investment.
Accompanying drawing explanation
In order to be illustrated more clearly that the technical scheme of embodiment of the present invention, below will be in embodiment
The required accompanying drawing used is briefly described, it will be appreciated that the following drawings illustrate only the present invention's
Some embodiment, is therefore not construed as the restriction to scope, for those of ordinary skill in the art
From the point of view of, on the premise of not paying creative work, it is also possible to obtain other according to these accompanying drawings and be correlated with
Accompanying drawing.
Fig. 1 is the structural representation of the eddy flow slagging-off collection device that embodiment of the present invention provides；
Fig. 2 is the top view of Fig. 1；
Fig. 3 is the structure of eddy current collector in the eddy flow slagging-off collection device that embodiment of the present invention provides
Schematic diagram；
Fig. 4 is that the A-A of Fig. 3 is to sectional view；
Fig. 5 is the structure of helix poly storage in the eddy flow slagging-off collection device that embodiment of the present invention provides
Schematic diagram；
Fig. 6 is that the A-A of Fig. 5 is to sectional view.
Figure acceptance of the bid note is respectively as follows:
Eddy flow slagging-off collection device 100；Whirlpool separator 110；Shell separator 111；Separate cavity
112；Slag-drip opening 113；Discharge outlet 114；Conducting element 115；Import end 116；Derive end 117；Spiral shell
Rotation collector 120；Collector housing 121；First housing 122；Second housing 123；Liquid outlet 124；
Inlet 125；Rotating vane 126；Impingement area 127；Boss 128；Rotating shaft 129；Driving equipment
130；Communicating pipe 140；Straight tube 141；Scum silica frost collecting tank 150；Charging aperture 151；Discharging opening 152；
Leakage fluid dram 153；Scum pipe 154；Glass vision panel 155；Skid base 160；Oral siphon 161.
Detailed description of the invention
For making the purpose of embodiment of the present invention, technical scheme and advantage clearer, below in conjunction with
Accompanying drawing in embodiment of the present invention, carries out clear, complete to the technical scheme in embodiment of the present invention
Describe, it is clear that described embodiment is a part of embodiment of the present invention rather than complete wholely
The embodiment in portion.Based on the embodiment in the present invention, those of ordinary skill in the art are not making
Go out the every other embodiment obtained under creative work premise, broadly fall into the model of present invention protection
Enclose.Therefore, below the detailed description of the embodiments of the present invention provided in the accompanying drawings is not intended to
Limit the scope of claimed invention, but be merely representative of the selected embodiment of the present invention.Base
Embodiment in the present invention, those of ordinary skill in the art are not making creative work premise
Lower obtained every other embodiment, broadly falls into the scope of protection of the invention.
In describing the invention, it is to be understood that term " on ", D score " vertically ", " water
Flat ", the orientation that indicates of " top ", " end ", " interior ", " outward ", " clockwise ", " counterclockwise " etc. or position
Relation of putting, for based on orientation shown in the drawings or position relationship, is for only for ease of the description present invention and Jian
Change and describe rather than indicate or imply that the equipment of indication or element must have specific orientation, Yi Te
Fixed azimuth configuration and operation, be therefore not considered as limiting the invention.
Additionally, term " first ", " second " are only used for describing purpose, and it is not intended that instruction or
Hint relative importance or the implicit quantity indicating indicated technical characteristic.Thus, define " the
One ", the feature of " second " can express or implicitly include one or more this feature.?
In description of the invention, " multiple " are meant that two or more, unless otherwise the most concrete
Limit.
In the present invention, unless otherwise clearly defined and limited, term " install ", " being connected ", " even
Connect ", the term such as " fixing " should be interpreted broadly, connect for example, it may be fixing, it is also possible to be can
Dismounting connects, or integral；Can be to be joined directly together, it is also possible to be indirectly connected to by intermediary,
Can be connection or the interaction relationship of two elements of two element internals.General for this area
For logical technical staff, above-mentioned term concrete meaning in the present invention can be understood as the case may be.
In the present invention, unless otherwise clearly defined and limited, fisrt feature second feature it " on "
Or D score can include that the first and second features directly contact, it is also possible to include that first and second is special
Levy and be not directly contact but by the other characterisation contact between them.And, fisrt feature exists
Second feature " on ", " top " and " above " include fisrt feature directly over second feature and
Oblique upper, or it is merely representative of fisrt feature level height higher than second feature.Fisrt feature is special second
Levy " under ", " lower section " and " below " include fisrt feature immediately below second feature and obliquely downward,
Or it is merely representative of fisrt feature level height less than second feature.
Embodiment 1, referring to figs. 1 through shown in Fig. 6,
The eddy flow slagging-off collection device 100 that the present embodiment provides, as depicted in figs. 1 and 2, including whirlpool
Stream separator 110, communicating pipe 140 and helix poly storage 120.Whirlpool separator 110 and spiral shell
Rotation collector 120 is by being interconnected communicating pipe 140.
Whirlpool separator 110 has shell separator 111 and separates cavity 112.Separator shell
Body 111 is columnar structured or hollow cylindrical structure, shell separator in the present embodiment
111 is cylindrical shape.Separate cavity 112 and be positioned at the inside of shell separator 111, separate cavity
The cross section of 112 is circular, separates cavity 112 and separates offer field with scum silica frost for water in sewage
Institute.Shell separator 111 is provided with and separates the slag-drip opening 113 that cavity 112 is interconnected
With discharge outlet 114.In the present embodiment, slag-drip opening 113 is arranged at shell separator 111
Top, the scum silica frost being separated from water in separating cavity 112 is discharged from slag-drip opening 113；Discharge outlet
114 bottoms being arranged at shell separator 111, remove the water of scum silica frost in separating cavity 112
Discharge from discharge outlet 114, enter next sewage unit and carry out advanced treating.
As it is shown in figure 5, helix poly storage 120 include collector housing 121, rotating vane 126,
Rotating shaft 129 and driving equipment 130.Rotating vane 126 and rotating shaft 129 are arranged at collector
In housing 121, rotating shaft 129 is driven by driving equipment 130.Rotating vane 126 is helical form.
Rotating vane 126 is fixing with rotating shaft 129 to be connected, when rotating shaft 129 driving at driving equipment 130
When rotating under Dong, rotating vane 126 is driven along direction clockwise or counter-clockwise by rotating shaft 129
Rotate.
Collector housing 121 is provided with liquid outlet 124 and inlet 125, collector housing 121
Inlet 125 be connected with oral siphon 161.Collector housing 121 is tubulose, collector shell
Body 121 includes the first housing 122 and the second housing 123, the liquid outlet 124 removably connected
Being arranged at the second housing 123, inlet 125 is arranged at the first housing 122.This detachably
Connected mode can be threaded, clamping or Flange joint, in the present embodiment,
Connected mode between one housing 122 and the second housing 123 is Flange joint.So arrange
It is advantageous in that and is easy to rotating vane 126 and the installation of rotating shaft 129 and cleaning.
In order to further improve the eddy flow slagging-off collection device 100 in the present embodiment to scum silica frost
With the treatment effeciency of elaioleucite, the rotating vane of the eddy flow slagging-off collection device 100 in the present embodiment
Boss 128 it is provided with on 126.As shown in Figure 6, rotating vane 126 is near inlet 125
Side be impingement area 127, rotating vane 126 is provided with in the side at impingement area 127 place
Multiple boss 128.Sewage and rotating vane 126 contact with each other at impingement area 127 and touch
Hitting, the setting of boss 128 increases scum silica frost in sewage or the mutual collision probability of elaioleucite, makes
Short grained elaioleucite or other tiny scum silica frost particle are assembled and adult under the effect of collision
Long-pending bigger particulate matter, beneficially scum silica frost and the cyclonic separation of elaioleucite.The number of boss 128 can
There to be 50-200, those skilled in the art can be arranged the most flexibly.At this
In embodiment, boss 128 is provided with 62.Through inventor's validation trial, it is provided with
The helix poly storage 120 of 62 boss 128 is to the congregational rate of tiny elaioleucite and scum silica frost
Good.
As shown in Figure 3-Figure 5, one end of communicating pipe 140 is connected with liquid outlet 124, connection
The other end of pipe 140 stretches into separation cavity 112 the medial wall phase with whirlpool separator 110
Cut.So arrange and be advantageous in that, flow through the sewage in helix poly storage 120 at rotating vane
There is the centrifugal force in inertia direction, when the other end and the eddy current of communicating pipe 140 under the effect of 126
When the medial wall of separator 110 is tangent, it is possible to reduce sewage and contacting with whirlpool separator 110
Time kinetic energy rejection, and contribute to sewage continue in whirlpool separator 110 eddy current separate
Spinning and move and form eddy current further in the medial wall of device 110, thus carries out scum silica frost and sewage
Separation.
When mounted, the length direction of helix poly storage 120 can be with whirlpool separator 110
Length direction consistent, it is also possible to vertical with the length direction of whirlpool separator 110.In this reality
Execute in example, the length direction of helix poly storage 120 and the length direction one of whirlpool separator 110
Cause, in this type of design, include interconnective straight tube 141 and bend pipe (figure communicating pipe 140
Do not show), straight tube 141 stretches into separation cavity 112 along the tangential direction of whirlpool separator 110,
Bend pipe is connected with liquid outlet 124.Sewage after the liquid outlet 124 of helix poly storage 120 flows out,
Straight tube 141 is flowed to, the most again by tangential along whirlpool separator 110 of straight tube 141 from bend pipe
Direction flows to separate cavity 112.Such design advantageously reduces sewage and flows in runner pipe
Time energy loss.
In order to make the sewage entered in separation cavity 112 be more likely formed eddy current, at the present embodiment
Eddy flow slagging-off collection device 100 in be provided with conducting element 115.Specifically, such as Fig. 4 and Tu
Shown in 5, conducting element 115 is arranged at the medial wall of whirlpool separator 110, and conducting element 115 is
Circumferentially extending arcuate structure along the medial wall of whirlpool separator 110.Conducting element 115
There is importing end 116 and derive end 117, importing end 116 near the exit of communicating pipe 140.
In order to enable sewage to fully enter conducting element 115, import end 116 and be positioned at communicating pipe 140
Lower section.Derive end 117 and importing end 116 may be located at same level height, derive end 117
The horizontal plane at place can also be less than the horizontal plane importing end 116 place.In the present embodiment,
The horizontal plane deriving end 117 place slightly below imports the horizontal plane at end 116 place, so arranges
It is advantageous in that sewage can do rotation along conducting element 115 under gravity downward
Motion, contributes to the quick formation of eddy current.
Meanwhile, between the central angle of the arcuate structure of conducting element 115 is spent at 160 degree-200.
Conducting element 115 in this angular range, from derive end 117 flow out sewage speed and from
Mental and physical efforts more contribute to forming eddy current.In the present embodiment, the arcuate structure of conducting element 115
Central angle is about 175 degree, under the effect of the conducting element 115 of this angle, and whirlpool separator
The separating effect of 110 is best.
Conducting element 115 can be mozzle or the deflector with loop configuration.Work as conducting element
115 when being deflector, and the angle of deflector and the medial wall of whirlpool separator 110 is at 45 degree
Between-135 degree, so arrange it can be avoided that the sewage of larger flow is out-of-date from deflector upstream
Will not overflow from the edge of deflector.When conducting element 115 is mozzle, whirlpool separator
The internal diameter of 110 is 8-10 times of the internal diameter of mozzle, so arranges and is advantageous in that and can make
In the centrifugal force of the sewage in mozzle keeps a bigger scope, beneficially eddy current enter one
Step is formed.
In use, sewage is drained into helix poly storage by oral siphon 161 from inlet 125
In the housing of 120, driving equipment 130 drive shaft 129 in helix poly storage 120 drives
Rotating vane 126 rotates, and from inlet 125, sewage is drained into liquid outlet 124, with after through even
Siphunculus 140 drains in whirlpool separator 110.Because rotating vane 126 is helical form, from connection
The sewage that pipe 140 is discharged has the inertia force being threadingly advanced.Owing to communicating pipe 140 divides with eddy current
Tangent from the medial wall of device 110, and under the effect of conducting element 115, from communicating pipe 140
The sewage discharged can continue to revolve along the medial wall of whirlpool separator 110 under the effect of inertia force
Transhipment is dynamic and forms eddy current.Sewage rotate during, under the influence of centrifugal force, due to
The density of water is big compared with oily and scum silica frost density, can be thrown to the medial wall of whirlpool separator 110,
And scum silica frost and oil can be gathered in the center of whirlpool separator 110, and along with whirlpool separator 110
The rising of interior water level, discharges from slag-drip opening 113 under the effect of buoyancy of water.Whirlpool separator
Water processed in 110 can enter next after outlet from the middle and lower part of equipment discharges
Unit carries out advanced treating.
This eddy flow slagging-off collection device 100, by setting up spiral in the outside of whirlpool separator 110
Collector 120, provides power for sewage separation in whirlpool separator 110, effectively shortens whirlpool
In stream separator 110, sewage and the disengaging time of scum silica frost, improve the treatment effeciency of scum silica frost in sewage.
Additionally, this eddy flow slagging-off collection device 100, it is achieved that the automatic receipts of the sewage scum of big flow
Collection, greatly reduces the cost of investment of sewage disposal.
Further, as depicted in figs. 1 and 2, eddy flow slagging-off collection device 100 also includes floating
Slag collecting tank 150, scum silica frost collecting tank 150 is provided with charging aperture 151, charging aperture 151 and deslagging
It is provided with scum pipe 154 between mouth 113.The scum silica frost separated from whirlpool separator 110 is from row
After cinder notch 113 is discharged, in scum pipe 154 drains into scum silica frost collecting tank 150, periodically locate
Reason is discharged.The glass vision panel 155 facilitating staff to check it is provided with on scum silica frost collecting tank 150.
The top of scum silica frost collecting tank 150 is provided with discharging opening 152, the discharging opening of scum silica frost collecting tank 150
152 are provided with pressure slag-draining device.In tapping process, or pipeline bonding if there is scum silica frost blocks up
During situation about filling in, staff can open air pressure flushing cinder system source of the gas and the extrusion of scum silica frost top be gone.
Being provided with leakage fluid dram 153 bottom scum silica frost collecting tank 150, leakage fluid dram 153 is assembled with spiral
The inlet 125 of device 120 is connected.Scum silica frost collecting tank 150 is looked first at before discharging scum silica frost
Bottom whether have waste liquid.If there being waste liquid, first use the mode of air pressure by waste liquid by leakage fluid dram
Again process in 153 inlets 125 draining into cyclone separator.So it is provided with beneficially
Improve the treatment effeciency of sewage further, and make final bed drain purge reduce, thus reduce floating
The processing cost of slag.
Additionally, for convenience this eddy flow slagging-off collection device 100 carrying, the present invention provide
Eddy flow slagging-off collection device 100 can also include skid base 160, whirlpool separator 110,
Helix poly storage 120 and scum silica frost collecting tank 150 are mounted on skid base 160.Eddy flow removes
The one-tenth sledge integration of slag collection device 100, contributes to the installation resettlement of package unit.
The foregoing is only the preferred embodiment of the present invention, be not limited to the present invention, right
For those skilled in the art, the present invention can have various modifications and variations.All the present invention's
Within spirit and principle, any modification, equivalent substitution and improvement etc. made, should be included in this
Within bright protection domain.
Claims (10)
1. an eddy flow slagging-off collection device, it is characterised in that include whirlpool separator, connection
Pipe and helix poly storage, described whirlpool separator has separation cavity and slag-drip opening, described separation
The cross section of cavity is circular, and described helix poly storage includes collector housing, spiral helicine rotation
Rotating vane sheet, rotating shaft and drive the driving equipment of described axis of rotation, described rotating vane and institute
Stating rotating shaft to be arranged in described collector housing, described rotating vane is arranged at described rotating shaft, institute
State collector housing and be provided with liquid outlet and inlet, one end of described communicating pipe and described liquid outlet
Connect, the other end of described communicating pipe stretch into described separation cavity and with described whirlpool separator
Medial wall is tangent.
Eddy flow the most according to claim 1 slagging-off collection device, it is characterised in that described
The side of the close described inlet of rotating vane is impingement area, and described rotating vane is provided with many
Individual boss, described boss is positioned at the side at described impingement area place.
Eddy flow the most according to claim 1 slagging-off collection device, it is characterised in that described
Include that interconnective straight tube and bend pipe, described straight tube are cut communicating pipe along described whirlpool separator
Stretch into described separation cavity to direction, described bend pipe is connected with described liquid outlet.
Eddy flow the most according to claim 1 slagging-off collection device, it is characterised in that described
The medial wall of whirlpool separator is provided with conducting element, and described conducting element is for separate along described eddy current
The circumferentially extending arcuate structure of the medial wall of device, described conducting element has importing end and derivation
End, described importing end is near the exit of described communicating pipe.
Eddy flow the most according to claim 4 slagging-off collection device, it is characterised in that described
The central angle of conducting element is 160 degree of-200 degree.
Eddy flow the most according to claim 4 slagging-off collection device, it is characterised in that institute
Stating conducting element is mozzle or deflector.
Eddy flow the most according to claim 1 slagging-off collection device, it is characterised in that described
Collector housing is tubulose, and described collector housing includes the first housing and removably connected
Two housings, described liquid outlet is arranged at described second housing, and described inlet is arranged at described
One housing.
Eddy flow the most according to claim 1 slagging-off collection device, it is characterised in that described
Eddy flow slagging-off collection device also includes that scum silica frost collecting tank, described scum silica frost collecting tank are provided with charging aperture,
It is provided with scum pipe between described charging aperture and described slag-drip opening.
Eddy flow the most according to claim 8 slagging-off collection device, it is characterised in that institute
State eddy flow slagging-off collection device and also include skid base, described whirlpool separator, described helix poly
Storage and described scum silica frost collecting tank are mounted on described skid base.
Eddy flow the most according to claim 8 slagging-off collection device, it is characterised in that institute
Stating and be provided with leakage fluid dram bottom scum silica frost collecting tank, described leakage fluid dram is connected with described inlet.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106693514A (en) * | 2017-03-07 | 2017-05-24 | 英泰流体控制科技（天津）有限公司 | High-efficiency deslagging device and high-efficiency deslagging system |
| CN108408886A (en) * | 2018-04-23 | 2018-08-17 | 宁夏大学 | Thermostatic type aeration tank |
| CN111704957A (en) * | 2020-06-23 | 2020-09-25 | 江西黄龙油脂有限公司 | Rice bran oil processing equipment |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1416444A1 (en) * | 1987-01-22 | 1988-08-15 | Предприятие П/Я А-3780 | Separator for purifying oil-containing ship-borne water from petroleum products |
| CN101921014A (en) * | 2009-06-12 | 2010-12-22 | 帕洛阿尔托研究中心公司 | The mixing screw that is used for floc conditioning |
| CN102020336A (en) * | 2009-09-23 | 2011-04-20 | 北京石油化工学院 | Equipment and method for treating oil extraction wastewater with integration of coalescence and hydrocyclone separation |
| CN202173814U (en) * | 2011-06-16 | 2012-03-28 | 吴亮樽 | Pipeline type oil-water separator |
| CN205187964U (en) * | 2015-12-08 | 2016-04-27 | 湖南水之源环保科技工程有限公司 | Sewage treatment equipment |
| CN205676192U (en) * | 2016-06-16 | 2016-11-09 | 重庆坤泉环境工程有限公司 | Eddy flow slagging-off collection device |
-
2016
- 2016-06-16 CN CN201610435359.0A patent/CN105923703B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1416444A1 (en) * | 1987-01-22 | 1988-08-15 | Предприятие П/Я А-3780 | Separator for purifying oil-containing ship-borne water from petroleum products |
| CN101921014A (en) * | 2009-06-12 | 2010-12-22 | 帕洛阿尔托研究中心公司 | The mixing screw that is used for floc conditioning |
| CN102020336A (en) * | 2009-09-23 | 2011-04-20 | 北京石油化工学院 | Equipment and method for treating oil extraction wastewater with integration of coalescence and hydrocyclone separation |
| CN202173814U (en) * | 2011-06-16 | 2012-03-28 | 吴亮樽 | Pipeline type oil-water separator |
| CN205187964U (en) * | 2015-12-08 | 2016-04-27 | 湖南水之源环保科技工程有限公司 | Sewage treatment equipment |
| CN205676192U (en) * | 2016-06-16 | 2016-11-09 | 重庆坤泉环境工程有限公司 | Eddy flow slagging-off collection device |
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| CN106693514A (en) * | 2017-03-07 | 2017-05-24 | 英泰流体控制科技（天津）有限公司 | High-efficiency deslagging device and high-efficiency deslagging system |
| CN108408886A (en) * | 2018-04-23 | 2018-08-17 | 宁夏大学 | Thermostatic type aeration tank |
| CN108408886B (en) * | 2018-04-23 | 2024-03-05 | 宁夏大学 | Constant temperature type aeration tank |
| CN111704957A (en) * | 2020-06-23 | 2020-09-25 | 江西黄龙油脂有限公司 | Rice bran oil processing equipment |
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