CN107226505A - Dissolved air flotation machine - Google Patents
Dissolved air flotation machine Download PDFInfo
- Publication number
- CN107226505A CN107226505A CN201710173727.3A CN201710173727A CN107226505A CN 107226505 A CN107226505 A CN 107226505A CN 201710173727 A CN201710173727 A CN 201710173727A CN 107226505 A CN107226505 A CN 107226505A
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- China
- Prior art keywords
- air
- water
- groove
- air supporting
- bubble
- Prior art date
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- Pending
Links
- 238000009300 dissolved air flotation Methods 0.000 title abstract 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 125
- 239000008213 purified water Substances 0.000 claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 15
- 239000002351 wastewater Substances 0.000 claims abstract description 13
- 230000008093 supporting effect Effects 0.000 claims description 66
- 238000000746 purification Methods 0.000 claims description 23
- 239000012530 fluid Substances 0.000 claims description 12
- 238000007789 sealing Methods 0.000 claims description 11
- 239000003643 water by type Substances 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 2
- 210000001364 upper extremity Anatomy 0.000 claims 4
- 238000002955 isolation Methods 0.000 claims 1
- 230000002093 peripheral effect Effects 0.000 claims 1
- 238000005188 flotation Methods 0.000 abstract description 8
- 238000007599 discharging Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 9
- 238000005381 potential energy Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 229920001084 poly(chloroprene) Polymers 0.000 description 4
- 235000003140 Panax quinquefolius Nutrition 0.000 description 3
- 240000005373 Panax quinquefolius Species 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 108010022579 ATP dependent 26S protease Proteins 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1431—Dissolved air flotation machines
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1443—Feed or discharge mechanisms for flotation tanks
- B03D1/1456—Feed mechanisms for the slurry
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1443—Feed or discharge mechanisms for flotation tanks
- B03D1/1462—Discharge mechanisms for the froth
-
- 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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biotechnology (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physical Water Treatments (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
The apparatus is a dissolved air flotation machine, whose operation in terms of hydraulics is based on the principle of speed cancellation. The apparatus comprises: a cylindrical groove (33) provided with an upper edge on its side wall; a supply device for supplying the wastewater to be treated to the tank (33); a collecting and discharging device that collects and discharges the purified water produced by the dissolved air flotation; -an air-flotation bubble collecting device that collects air-flotation bubbles present in the surface of the liquid contained in the tank (33) after dissolved air flotation; -a movable rotating turret placed at the central region of the tank (33) and at the upper edge of the side wall of the tank, said movable rotating turret carrying said feeding means, the purified water collecting means and the flotation bubble collecting means for feeding the wastewater to be treated to the tank; the water supply device to be treated has a range extending from the center of the tank (33) toward the outer periphery of the tank and below the upper liquid level of the liquid contained in the tank (33).
Description
Technical field
Suspended material present in liquid (being usually water) is entered by using air-dissolving air-float technology the present invention relates to one kind
The device of row separation, and operation of the device in terms of fluid power is based on speed offset principle, and the principle is public in the art
Know.In everyday practice, such device is referred to as " dissolved gas floatator ".The device can be used for purifying waste water.
Background technology
Air-dissolving air-float purification techniques uses air (or other gases) microbubble, and these microbubbles are attached to be present in and wait to locate
The solid particle (suspended material) in water is managed to cause solid particle to rise to surface.Thus, pollution solid material is separated from water,
So as to which water is cleaned, the solid matter is collected on surface.Each dissolved gas floatator includes two main elements.
First element is microbubble generation system, and the system constitutes the core of each air-dissolving air-float cleaning equipment.It is more general
Everywhere, microbubble is obtained by making a part of purified water cycle through booster pump and forced air dissolver.Should be rich in molten
The pressure (hydraulic) water of gas, which returns to atmospheric pressure, causes molten gas to be separated out in the form of microbubble.
Second element is groove, carries out the separation of polluter and water for physically in the cell.In the presence of comprising different
Many structures of fluid power concept.The most common center that is used in has accessing pending water input port and is recycled to purified water outer
The circular trough enclosed；Or use has accessing pending water input port in side and has the square of purification water output in opposite side
Shape groove.In the case where not discussing the details of existing each fluid power concept, it is believed that the purpose of research is identical all the time,
Ensuring the flowing of the water between input port and delivery outlet has turbulent flow as few as possible, to cause the separation of polluter and water
Process can carry out closest in the state of laminar flow, and this is most fragile and fine purification process is opened for being proved to be
Exhibition is clearly best.
Operation of the apparatus according to the invention in terms of fluid power is based on speed offset principle, by the structure for ensuring these functions
Part offsets the boot speed of accessing pending water and the gathering speed of purified water respectively.The principle is applied to the equipment with circular trough.
Accessing pending water is allocated by the radial device of the central rotation activity relative to groove, the water of its rotary speed and distributor
Output speed it is identical, and the direction of rotation of radial device and the outbound course of water are opposite.In this way, two speed are mutual
Offset (name for thus obtaining the principle), and each accessing pending water volume importeding into air flotation slot is remained stationary as and waited
The recovery system of purified water is collected to it.Meanwhile, purified water passes through similar to accessing pending water gatherer and link
Collected to the radial device of accessing pending water gatherer, the radial device is located at downstream relative to the outbound course of water.Change speech
It, is not water is moved between input unit and output device (the two is fixed), but make the input unit and
Output device depending on the speed of water-carrying capacity to move, make it that water is not moved but is rested on water and is imported into by input unit
Groove in and wait output device to be collected it.The technology is known and for example in document US 4 022
It is described in 696.The technology has different known embodiments, wherein version the most advanced is with KWI
International companies sell trade name Supercell and be known.Even if the known device is commercially achieved
Huge success, but it result in the concept of fluid power and mechanical aspects and realizes that some relevant are asked with speed offset principle
Topic.
In fact, same in view of its concept, distribution of the accessing pending water in the air flotation slot of these equipment passes through in groove
Rotary engaging member at the heart is completed, and is connected to from air supporting bubble and is collected above central channel by and from activity after the fastener
The pipe-line system passed through below buoyancy tank, the pipe-line system separates in air supporting region with purification water collecting groove, purifies water collecting groove
Itself is located between the gentle floating bubble collecting tank in air supporting region.Above two grooves by certainty from the horizontal plane in the groove with
And pass through above air supporting region.Square this rising needs extra supply pressure, the extra supply to water in the horizontal plane
Pressure can only be relative to the potential energy of the horizontal plane in air supporting region.Compensation of the dispatching device to the potential energy causes very strong disorderly
Stream.
Therefore, for small-size equipment, the potential energy is expressed as 20 to 30cm water column, and this shows as water in dispatching device
Equipped at outlet port is with 1.4 to 1.6m Speed allotments per second.
For large scale equipment, the potential energy can reach 60cm water column, and this shows as the equipped at outlet port in dispatching device
2.4 to 2.6m speed per second.
It is apparent that being difficult compatible with desired effect with this speed injection accessing pending water, that is, set up and most connect with laminar flow
Near flox condition.
Supporting and centring means that rotary components are arranged in the rotary engaging member requirement at equipment center are additionally, there are, this
It result in substantial amounts of mechanical problem.
A kind of difference and advantageous approach for implementing speed offset principle is proposed according to the equipment of the present invention, set with known
Standby to compare, this method makes it possible to solve the problems, such as most machinery and fluid power.
The content of the invention
According to the equipment of the present invention by the collection central channel of the air supporting bubble with air supporting bubble discharge line with being somebody's turn to do
The accessing pending water rotation supply fastener of equipment is combined, and is enable to the water included in the major trough for constituting air supporting chamber
Accessing pending water is imported below the surface of volume and around the air supporting bubble discharge line, accessing pending water is generally in the groove institute
It is directed in the overall depth or height of the liquid of receiving in groove.
The concept is so that can：
- accessing pending water is supplied to groove with minimum pressure, to cause supply hydraulic measurement pipe to be no more than all the time in air supporting chamber
Water upper plane.Therefore, the potential energy that supply belt is come significantly reduces, and this is equally reduced in distribution by the potential energy to kinetic energy
It is inevitably turbulent caused by conversion (water in flotation cell declines again)；
- simple fixed center is used to input unit and the swivel mount of the collection device of purified water including accessing pending water
Bearing.
Brief description of the drawings
By the embodiment that is provided below in illustrative and not restrictive mode and referring to the drawings, realization side of the invention
Formula and thus obtained advantage become readily apparent from.
Fig. 1 a to 1d respectively illustrate the vertical section figure, top view and waste water supply area of the equipment of prior art
Detail cross-sectional view and top view.
Fig. 2 a to 2d are equipment, similar to Fig. 1 a to the 1d view according to first embodiment of the invention.
Fig. 3 a diagrammatically illustrate the more detailed vertical section of frame, and the frame includes the accessing pending water of the equipment in Fig. 2
Distributor and purification water dispenser, Fig. 3 b are schematic top plan view, and Fig. 3 c are detail view.
Fig. 4 a to 4d are second embodiment, similar to Fig. 2 a to the 2d view of the equipment according to the present invention.
Fig. 5 a diagrammatically illustrate the more detailed vertical section of the equipment in Fig. 4, and Fig. 5 b are illustrated in greater detail
The top view of the equipment.
Fig. 6 a and 6b diagrammatically illustrate the plan of the modification of equipment shown in Fig. 2 and 3, according to the present invention.
Fig. 7 a and 7b are respectively the decomposition assembling schematic diagram of the equipment in Fig. 2 and 3.
Fig. 8 a and 8b are equipment, similar with 7b to Fig. 7 a view in Figure 4 and 5.
The description of equipment of prior art
In order to more fully understand the concept of the equipment according to the present invention, prior art is set hereinafter with reference to accompanying drawing 1
Standby 26S Proteasome Structure and Function is described.
The equipment includes：
■ grooves (1), are provided with bottom (2)；
■ air supporting bubble collecting tanks (3), it is coaxial with groove (1)；
■ rotary moveables sleeve pipe (4), it separates the output chamber of the input chamber of accessing pending water and purified water；
■ accessing pending waters distributor (16)；And
■ purification water collectors (14).
Air supporting bubble scoops part (8) by the rotation Sheng driven by reducing motor (15) and scooped out.
Accessing pending water gatherer, purification water collecting device and air supporting bubble discharge device are carried by swivel mount (5).
The rotation of this is ensured by reducing motor (9).
The heart in a device, roller (6) supporting of the frame (5) on the top edge positioned at groove (3) and by being resisted against groove (3)
The roller (7) of the perimeter centers.
Rotary engaging member (12) and crooked pipeline system (11) ensure input port (18) and the distributor of accessing pending water
(16) engagement between, the input port of the accessing pending water is made up of the central tube system fixed, the distributor rotation
And carried by frame (5).
Finally, ring-type electric collecting device (13) makes it possible to two motors (9,15) power supply to being equipped with frame.
The equipment is run, but causes two problems, respectively fluid power property problem and engineering properties problem：
In fact, crooked pipeline system (11) should pass through from the top edge of groove (3) and revoling tube (4).In this way, water
Supply the water level progress of the water included in the groove for defining air supporting chamber (1) is substantially higher than.The water-head produces the gesture of water
Can, the potential energy should be compensated by the distribution control valve (21) being provided on distributor (16).
In order to keep crooked pipeline system (11) and distributor (16) in pressurization (be full of water) state to ensure distribution
Uniformity, such valve (21) should be conditioned can be converted to potential energy the load loss of kinetic energy to produce.Therefore, water is with pole
High speed (many metres per second is up to for large scale equipment) is imported into input chamber (17), and this draws in air flotation slot (1)
Play a large amount of turbulent flows.These turbulent flows extend to 1/3rd of purification region, even half, thus significantly affect purification process from
Body.Obviously, such turbulent flow sets up streamflow regime as tranquil as possible departing from desired effect in equipment, so that
Must purify can be carried out closer under conditions of laminar flow.
In order to protect rotary engaging member (12) from the damage of mechanical stress, the frame (5) positioned at center centering and propping up
Hold dependent on roller (6) and (7), the roller is rolled on the roller track being made up of Large Scale Cold operation workpiece.In fact, in machine
In terms of tool, the component of the roller/roller track is relatively accurate.This causes roller (6) and (7) too early mechanical loss and inevitable
Cause the mechanical loss of rotary engaging member (12), so as to cause high mid-term maintenance cost.
Embodiment
It is particularly described according to the first embodiment of the invention according to reference picture 2,3 and 7, the equipment is similarly molten gas
Air floatation machine, its run be based on speed offset principle, the dissolved gas floatator include circular trough (33) and equipped with：
- newel (30), wherein being disposed with lateral openings (41), the lateral openings are mixed as accessing pending water/pressure (hydraulic) water
The input port of compound.The newel is attached to the bottom of groove (33) and is therefore static；
- air supporting bubble collecting tank (40), it is fixed on newel (30) and is attached to the newel, and is equipped with
State the discharge line (31) of air supporting bubble.The groove also includes supporting member (39), supporting member carrying centre bearing (36)；
The delivery outlet (32) of-purified water；
- moving rotary frame (referring to Fig. 3 b), including：
The input chamber (42) of ■ accessing pending waters, its have water generally accommodated in groove (33) entire depth or
In height and at least exceed half or center more than 1/3rd slave units, more accurately from rotation along the height of water
Pivoted housing pipe (37) extends to the scope of equipment periphery, and the chamber is provided with circular shape, accessing pending water guide slot (49)；
The output chamber (43) of ■ purified waters, the entire depth or height of its water generally accommodated in groove (33)
Periphery upper and that equipment is at least extended to along the center more than half or more than 1/3rd slave units of the height of water,
Equipped with the purification water collector (46) for being provided with opening or space (47), and defined by revoling tube (34), the rotary sleeve
Pipe is coaxial with sleeve pipe (37) and outside in sleeve pipe (37).The purification water chamber (43) is arranged to generally with inputting chamber
(42) in identical (vertical) level and around input chamber；
■ sealing devices (38), such as, including neoprene lobe, the sealing device makes it possible to the defeated of accessing pending water
Enter chamber (42) with output chamber (43) fluid power of purified water to isolate；
■ sealing devices (52), such as, including neoprene lobe, the sealing device makes it possible to static air flotating chamber
Room (54) isolates with purification water chamber (43).
■ rotation Sheng scoop part (50) (being represented by dotted lines in Fig. 2 b plan), its equipped be able to ensure that the rotation contain
Scoop the reducing motor (51) of part rotation；
■ supporting structures (35), it supports above-mentioned apparatus components and is placed in center on centre bearing (36),
And be placed in periphery by supporting member (60) on two rollers (53).
Frame component is driven by reducing motor (61).
The apparatus according to the invention works in the following ways：
The accessing pending water mixed with pressure (hydraulic) water enters in newel (30), arrives dispensed chambers (42) through lateral openings (41)
In, through guide slot (49) and along arrow (45) direction reach air supporting chamber (54).According to the present invention key character and
It can find out in Fig. 2 c and 3a, air flotating chamber is entered below the liquid level for the liquid that accessing pending water is accommodated in the air supporting chamber
Room.
With accessing pending water enter air supporting chamber (54), frame in the counterclockwise direction with generally with air supporting chamber (54)
Water the equal speed rotation (rotation retract) of input speed.Use air supporting well known in the art is carried out in the chamber
Purification, therefore need not be described in detail herein.
In this way, the air supporting bubble that the purification is produced rises to the upper surface of air supporting chamber (54), and it is present in the gas
In the floating chamber, water layer below air supporting bubble is progressively purified until frame completes to rotate for one week.Purified water is in arrow (48)
Discharged on direction first via opening (47) and then via purification water chamber (43) from air supporting chamber (54), with finally via output
Mouth (32) leaves equipment.
Certainly, air supporting bubble is scooped part (50) and scooped out by containing, and is flowed into afterwards in groove (40), and last via air supporting bubble
Output pipe (31) is discharged.
Liquid level in equipment is maintained by external device (ED) (not shown), and for example the self-shooter by servo in liquid level sensor is tieed up
Hold.
It is apparent that being realized according to the frame of equipment and the different elements of core of the present invention by various ways.
In this way, allocation model of the water between guide slot (49) can be used or determining without using the uniformity for ensuring distribution
Diameter opening is realized.If it is necessary, groove (49) can be removed, thus water is via the simple opening being arranged in chamber (42)
Or space enters in flotation chamber.
Equally, Sealed junction (38) can be realized by various ways, implement flexible or rigid contact surface.
This is the same for the Sealed junction (52) of revoling tube (34).
In addition, if sleeve pipe (37) is arranged on more than the water level in input chamber (42), upper Sealed junction (38) can
To be removed.
The collection of purified water can be using single collector (as shown in Figures 2 and 3) or multiple collectors (14) (as schemed
Shown in 1) realize.
Opening (47) can extend to collect the water on entire depth in most of depth of water layer, or concentrate merely on
The bottom of air supporting chamber.
It is particularly described second embodiment of the invention according to reference picture 4,5 and 8, the equipment is air-dissolving air-float
Machine, its work is based on above-mentioned speed offset principle.The equipment include circular trough (73), and including：
- air supporting bubble collects central channel (80), and it is fixed on the bottom of groove (73) and linked with it, and equipped with air supporting
The discharge line (71) of bubble.The groove (80) also includes upper support (79), upper support carrying centre bearing (76)；
The input port (70) of-pending waste water, it is located at air supporting bubble and collects central channel (80) and rotary moveable sleeve pipe
(77) between, the rotary moveable sleeve pipe (77) limits one of the input chamber of pending waste water together with central channel (80)
Point；
The delivery outlet (72) of-purified water, it is located between rotary moveable sleeve pipe (77) and another rotary moveable sleeve pipe (74),
The rotary moveable sleeve pipe (74) limits a part for the collection chamber of purified water together with sleeve pipe (77)；
- moving rotary frame, it includes：
The input chamber (82) of the pending waste water of ■, its have the entire depth of water that is generally accommodated in groove (73) or
The scope at least extended along the center more than half or more than 1/3rd slave units of the height in height and to the periphery,
And terminate at guide slot (99)；
The output chamber (83) of ■ purified waters, it is equipped with the collector (96) including opening (97) and by revoling tube
(74) defined with moving casing (77), the revoling tube (74) is provided with sealing device (92).Purification water chamber (83) quilt
It is set to generally with input chamber (82) in identical (vertical) level and around input chamber, and generally in groove (73)
In water entire depth or height on and at least the water height exceed half or more than 1/3rd on extend.
■ sealing devices (78), the neoprene lobe for example provided by way of example, enabling will be pending useless
The input chamber (82) of water is isolated with output chamber (83) fluid power of purified water；
■ sealing devices (78), the neoprene lobe for example provided by way of example, enabling by air supporting chamber
(94) isolate with purification water chamber (83).
■ rotation Sheng scoop part (90) (being represented by dotted lines in Fig. 4 b plan), its equipped be able to ensure that the rotation contain
The reducing motor (91) of part rotation is scooped,
■ supporting structures (75), it supports above-mentioned apparatus components, and is placed in center on centre bearing (76),
Two rollers (93) are placed in periphery.
Worked in the following ways according to the equipment of the second embodiment：
The accessing pending water mixed with pressure (hydraulic) water is entered, through dispensed chambers (82), by guide slot by input port (70)
(99) and along the direction of arrow (45) air supporting chamber (94) is reached.
With dampening enter air supporting chamber (94), frame in the counterclockwise direction with generally with the water in air supporting chamber (94)
The equal speed rotation of input speed (rotation retracts).
Carry out using pneumatically supported purification in the chamber (94).Thus, air supporting bubble rises to the surface of the chamber, and
And water layer is gradually purified until frame completes to rotate for one week.Purified water in the side of arrow (48) thus by passing upward through opening first
(97) and then by purification water chamber (83) discharged from air supporting chamber (94), so that final left via delivery outlet (72) sets
It is standby.
Air supporting bubble scoops part (90) collection by containing, and flows into afterwards in groove (80), and the last output via air supporting bubble
Pipeline (71) is discharged.
Liquid level in equipment is maintained by external device (ED) (not pointing out), and for example the self-shooter by servo in liquid level sensor is tieed up
Hold.
It is apparent that according to the frame of equipment and the different elements of core of the second embodiment of the present invention by a variety of sides
Formula is realized.
In this way, allocation model of the water between guide slot (99) can be used or realized without using diameter opening is determined.Such as
It is necessary, groove (99) can be removed.
In addition, Sealed junction (38) can be realized by various ways, it implements flexible or rigid contact surface.
This is as revoling tube (74) is also for (78) with the Sealed junction (92) of (77).
The collection of purified water can be using single collector (as shown in Figures 4 and 5) or multiple collectors (14) (as schemed
Shown in 1) realize.
Opening (97) can extend to collect the water on entire depth in most of depth of water layer, or concentrate merely on
Bottom.
The third embodiment of the present invention more particularly described according to reference picture 6, the equipment and reference picture 2,3 and 7
In show first embodiment description equipment it is similar.However, the equipment does not include single input (42)/output (43)
Rotary components, but including two input/output rotary components, two components are connected to each other and each other on equipment center
Radially symmetrically arrange.The configuration enables each component to distribute the accessing pending water of half and collects the purification of half respectively
Water.For identical input flow rate, the rotary speed of the frame formed by the two components thus reduces half.
Used and worked with first embodiment identical mode according to the equipment of the 3rd embodiment, but two components
In each distribution and collect half water.It is also such for air supporting bubble：Each scooped in part is contained in two rotations
Air supporting bubble is collected respectively.
Clearly：
- according to identical logic, equipment can equipped be not two but multiple (three or four etc.) inputs/defeated
Go out component, its groove center around groove (33,73) is arranged symmetrically；
- same concept is also adapted for the second embodiment of equipment shown in Fig. 4,5 and 8, according to the present invention.
No matter implementing which embodiment, the whole volume of pending water is uniformly led in the whole height or depth of groove
Enter, and the inevitable purified water that same volume is collected into according to same height or depth.Thus, speed offset principle is obtained completely
To satisfaction, suitable for generating optimal fluid power condition, thus the condition avoids turbulent flow close to inactive state.
Claims (4)
1. a kind of water correction plant of use air-dissolving air-float, including：
Cylinder groove (33,73), its side wall is provided with upper limb；
Feedway, it supplies pending waste water to the groove (33,73)；
Collect and discharger, it collects and discharged the purified water produced by air-dissolving air-float；
Air supporting bubble collecting device, its collection is present in the liquid that the groove (33,73) is accommodated after air-dissolving air-float
Air supporting bubble in surface；
Moving rotary frame, it is placed in the central area of the groove (33,73) and is placed at the upper limb of side wall of the groove,
The moving rotary frame carries to the groove and supplies the feedway of pending waste water, purifies water collecting device and described
Air supporting bubble collecting device；
Characterized in that, accessing pending water feedway has peripheral direction from the center of the groove (33,73) towards the groove simultaneously
And the scope extended under the upper liquid level of the liquid accommodated in the groove (33,73), the scope is generally in the groove
Extend on the entire depth or height of the liquid that (33,73) are accommodated.
2. the effluent purifying device of use air-dissolving air-float according to claim 1, it is characterised in that the equipment includes：
■ accessing pending waters backbone post (30), it is fixed on the bottom of the groove (33) and equipped with lateral openings (41)；
■ revoling tubes (37), it is around the newel (30) and is attached to the pending wastewater supplying device (42)；
■ revoling tubes (34), it is coaxial with described sleeve pipe (37) and outside positioned at described sleeve pipe (37), with the rotary sleeve
Pipe (37) limits a part for the purification water collecting device (43) together；
■ air supportings bubble collect upper slot (40), it include the discharger (31) of the air supporting bubble and with the air supporting gas
Steep collection device (50) connection；
■ sealing devices (52), it separates the chamber (43) of the purified water with air supporting region (54),
■ supporting structures (35,60), it supports the adjustable shelf, is respectively placed in above the air supporting bubble collecting tank (40)
Centre bearing (36) on and be placed at the upper limb of the side wall of the groove (33) by means of roller (53)；
■ sealing devices (38), it is in fluid power mode by the accessing pending water feedway and the purified water collection chamber (43)
Isolation, the sealing device (38) is around the air supporting bubble discharge device (31,71) and is placed in outside it.
3. the water correction plant of use air-dissolving air-float according to claim 1, it is characterised in that the equipment includes：
Air supporting bubble collect central channel (80), it include the discharger (71) of the air supporting bubble and with the air supporting gas
Steep collection device (90) connection；
Revoling tube (77), it is collected central channel (80) around the air supporting bubble and is attached to the pending waste water and supplies
Connected on device (82) and with the pending wastewater supplying device；
Revoling tube (74), it is coaxial with the revoling tube (77) and outside positioned at the revoling tube (77), with institute
State revoling tube (77) limit together it is described purification water collecting device (96) a part and with the purification water collecting device
Connection；
Water supplying duct (70), it is fixed to the bottom of the groove (73) and with collecting central channel by the air supporting bubble
(80) volume limited with the revoling tube (77) is connected；
Supporting structure (75,95), it supports the adjustable shelf, and the adjustable shelf is respectively placed in be collected positioned at the air supporting bubble
It is placed on centre bearing (76) above groove (80) and by means of roller (93) at the upper limb of the side wall of the groove (73)；
Sealing device (78,92), it is in fluid power mode respectively by pending wastewater supplying device and purified water collection chamber
(43) isolate, and the purified water collection chamber is isolated with the air supporting chamber (94).
4. the cleaning equipment of use air-dissolving air-float according to any one of claim 1 to 3, including two or more rotations
Frame, the swivel mount is connected to each other and center of relative to the groove (33,73) is symmetrically arranged with one another.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR1652511A FR3049197B1 (en) | 2016-03-24 | 2016-03-24 | DISSOLVED AIR FLOAT |
| FR1652511 | 2016-03-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107226505A true CN107226505A (en) | 2017-10-03 |
Family
ID=56119557
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710173727.3A Pending CN107226505A (en) | 2016-03-24 | 2017-03-22 | Dissolved air flotation machine |
Country Status (3)
| Country | Link |
|---|---|
| CN (1) | CN107226505A (en) |
| FR (1) | FR3049197B1 (en) |
| RU (1) | RU2017109442A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110372058A (en) * | 2019-06-25 | 2019-10-25 | 安溪坤祁德机械科技有限公司 | A kind of molten treatment apparatus of waste water based on secondary treatment |
| CN114534929A (en) * | 2022-04-28 | 2022-05-27 | 徐州华鹏机械科技有限公司 | Nonferrous metal mine flotation equipment |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110372058A (en) * | 2019-06-25 | 2019-10-25 | 安溪坤祁德机械科技有限公司 | A kind of molten treatment apparatus of waste water based on secondary treatment |
| CN114534929A (en) * | 2022-04-28 | 2022-05-27 | 徐州华鹏机械科技有限公司 | Nonferrous metal mine flotation equipment |
| CN114534929B (en) * | 2022-04-28 | 2022-07-22 | 徐州华鹏机械科技有限公司 | Nonferrous metal mine flotation equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| FR3049197B1 (en) | 2020-04-10 |
| FR3049197A1 (en) | 2017-09-29 |
| RU2017109442A (en) | 2018-09-24 |
| RU2017109442A3 (en) | 2020-07-30 |
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