CN103041624B - Hydraulic solid-liquid two phase separator - Google Patents
Hydraulic solid-liquid two phase separator Download PDFInfo
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- CN103041624B CN103041624B CN201110307534.5A CN201110307534A CN103041624B CN 103041624 B CN103041624 B CN 103041624B CN 201110307534 A CN201110307534 A CN 201110307534A CN 103041624 B CN103041624 B CN 103041624B
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Abstract
The invention discloses a kind of hydraulic solid-liquid two phase separator, comprise cylindrical tube, it is that the current stabilization of flat inclination revolves excessive plate that top in cylindrical tube is arranged, current stabilization revolves excessive plate and is divided by solid-liquid the overall tank chamber of filter tank to be divided into revolving excessive room and being positioned at the contour stealth cheek filter chamber below it of the side of being located thereon, swirling flow premium on currency cylinder in the centre that current stabilization revolves excessive plate is arranged, contour stealth cheek filter chamber revolves excessive chamber by interior swirling flow premium on currency cylinder connection, coordinate and be uniformly fixed with gill formula filter separator being positioned at the contour stealth cheek filter chamber on sand discharge funnel, each gill formula filter separator is made up of cube tubular box and branchial plate, the branchial plate that cube tubular box internal fixtion is arranged, the rectangle plane plate body of opposed square tubular box and horizontal plane and integral inclined, parallel each other between branchial plate, the two rectangle plane plate bodys that branchial plate is relative with cube tubular box form gap respectively.Sediment transport emptying effectiveness of the present invention is obviously higher, can further improve the clarity of the water body after sedimentation filtration.
Description
Technical field
The present invention relates to the water treatment sedimentation apparatus that liquid towards non-homogeneous mixture carries out filtration treatment, the solid particle in turbidity and clear water are separated from each other to filter out clear water, belong to muddy water sedimentation separation equipment, particularly hydraulic solid-liquid two phase separator.
Background technology
Existing tube settler is the sedimentation basin being provided with inclined tube in settling zone, in the settling zone of flat flow or vertical sedimentation basin, utilize the parallel pipe of inclination or parallelpiped (also can utilize honeycomb filler) to be separated into a series of shallow layer precipitating layer, the husky mud of processed precipitation mutually moves and is separated in each precipitation shallow-layer, be divided into inverse (different) to stream according to its mutual direction of motion, concurrent and reverse flow three kinds of different separate modes, between every two pieces of inclined paralled plates, (or parallel pipe in) is equivalent to a very shallow sedimentation basin, which utilizes lamina flow principle, improve disposal ability and the water treatment efficiency of sedimentation basin, but its sediment transport emptying effectiveness is lower, water after precipitation is still thoroughly clear not, its clarity is still lower.
Summary of the invention
The object of the present invention is to provide a kind of hydraulic solid-liquid two phase separator, its sediment transport emptying effectiveness is obviously higher, can further improve the clarity of the water body after sedimentation filtration.
The object of the present invention is achieved like this: a kind of hydraulic solid-liquid two phase separator, comprise the solid-liquid be made up of the cylindrical tube erect and sand discharge funnel and divide filter tank, the bell mouth of sand discharge funnel vertically down, sand discharge funnel is fixedly installed on the nozzle of cylindrical tube lower end, the water inlet pipe being communicated with the level in its chamber is fixedly installed at the foot of cylindrical tube, the outlet pipe being communicated with the level in its chamber is fixedly installed at the topmost of cylindrical tube, the tangential direction of the circular nozzle that one end mouth of pipe of water inlet pipe divides the water inlet of filter tank to present from cylindrical tube cross section as solid-liquid passes into the tank chamber that solid-liquid divides filter tank, the delivery port that one end mouth of pipe of outlet pipe is arranged on cylindrical tube barrel passes into the tank chamber that solid-liquid divides filter tank, it is flat current stabilization revolves excessive plate that top in cylindrical tube is arranged, it is inclined fixing that current stabilization revolves excessive plate relative level face, the angle threshold scope that current stabilization revolves the face included angle X of excessive plate and horizontal plane is 1 °≤λ≤5 °, current stabilization revolve excessive plate is provided with erect fixing in swirling flow premium on currency cylinder, interior swirling flow premium on currency cylinder is positioned at the circle centre position of the circle that cylindrical tube cross section presents as interior swirling flow delivery port, current stabilization revolves excessive plate and is divided by solid-liquid the overall tank chamber of filter tank to be divided into revolving excessive room and being positioned at the contour stealth cheek filter chamber below it of the side of being located thereon, contour stealth cheek filter chamber revolves excessive chamber by described interior swirling flow premium on currency cylinder connection, contour stealth cheek filter chamber is communicated with water inlet pipe, revolve excessive chamber and be communicated with outlet pipe, coordinate and be uniformly fixed with gill formula filter separator being positioned at the contour stealth cheek filter chamber on sand discharge funnel, each gill formula filter separator is made up of cube tubular box and branchial plate, whole box walls of cube tubular box are by the first rectangle plane plate body, second rectangle plane plate body, 3rd rectangle plane plate body and the 4th rectangle plane plate body connect and compose, the adjacent two rectangle plane plate bodys of cube tubular box are mutually vertical, relative two rectangle plane plate bodys are parallel to each other, be the closed rectangle of perimeter line to make the shape of cross section of cube tubular box, its whole rectangle plane plate body of each cube tubular box is all erect and is fixedly installed, gill formula filter separator is all fixedly mounted with along horizontal direction and forms at least one deck vertical separation cheek group, the relative rectangle of the corresponding formation of cube tubular box two in upright state is uncovered uncovered towards vertical direction, one rectangle of cube tubular box is uncovered is positioned at cube tubular box and upward topmost, its another rectangle is uncovered is positioned at cube tubular box bottom and down, fixing gap is equipped with between the adjacent two cube tubular box erect, cube tubular box internal fixtion arranges the identical branchial plate of N block, N >=2, each branchial plate is the plate body in the parallelogram with four edges of boards, first edges of boards of branchial plate are relative with the 3rd edges of boards to be parallel to each other, second edges of boards of branchial plate are relative with the 4th edges of boards to be parallel to each other, spacing W between each branchial plate its first relatively isometric edges of boards and the 3rd edges of boards is greater than the spacing J between the first rectangle plane plate body and the 3rd rectangle plane plate body, the first rectangle plane plate body that first edges of boards of each branchial plate are relative with cube tubular box respectively with the 3rd edges of boards contacts with the 3rd rectangle plane plate body and affixed, its second edges of boards of each branchial plate and the first rectangle plane plate body, the first right angled triangle hole is formed between second rectangle plane plate body, and its 4th edges of boards of each branchial plate and the 3rd rectangle plane plate body, the second right angled triangle hole is formed between 4th rectangle plane plate body, or the second edges of boards of each branchial plate and the first rectangle plane plate body, second rectangle plane plate body, the first right-angled trapezium hole is formed between 3rd rectangle plane plate body, 4th edges of boards of each branchial plate and the 3rd rectangle plane plate body, 4th rectangle plane plate body, the second right-angled trapezium hole is formed between first rectangle plane plate body, all branchial plates vertically arrange point-blank along the length direction of cube tubular box with relative level face, the box chamber of cube tubular box is separated into N-1 unit cheek chamber by N block branchial plate, each unit cheek chamber is all often between adjacent two pieces of branchial plates, its second edges of boards of each branchial plate second dihedral with its first edges of boards with four edges of boards between formed most advanced and sophisticated with the first dihedral that the 3rd edges of boards are formed is most advanced and sophisticated relative and its equal angle δ is acute angle, four pieces of the opposed square tubular box of all branchial plates rectangle plane plate bodys and horizontal plane erect and integral inclined, parallel each other between all branchial plates, all branchial plates and the first rectangle plane plate body or and the 3rd rectangular flat face body between its angle threshold scope of face angle α be 5 °≤α≤85 °, all branchial plates and the second rectangle plane plate body or and the 4th rectangle plane plate body between its angle threshold scope of face angle β be 5 °≤β≤85 °, its angle threshold scope of face angle theta between all branchial plates and horizontal plane is 5 °≤θ≤85 °, N row limbers group is set respectively on the first rectangle plane plate body and on the 3rd rectangle plane plate body, often arrange limbers group to be made up of M limbers, M >=2, often row limbers each branchial plate of group corresponding matching that first rectangle plane plate body and the 3rd rectangle plane plate body are arranged respectively, the limbers group of often arranging that first rectangle plane plate body is arranged is positioned at the corresponding orthographic projection boundary on the first rectangle plane plate body of each branchial plate, the limbers group of often arranging that 3rd rectangle plane plate body is arranged is positioned at the corresponding orthographic projection boundary on the 3rd rectangle plane plate body of each branchial plate, described contour stealth cheek filter chamber is arranged limbers group by two of each branchial plate above-mentioned and corresponding and is communicated with its corresponding unit cheek chamber, adjacent two unit cheek chambeies are all interconnected by above-mentioned right angled triangle hole or right-angled trapezium hole, and unit cheek chamber is also by the rectangle uncovered connection contour stealth cheek filter chamber of the most upper and lower end of above-mentioned right angled triangle hole or right-angled trapezium hole and cube tubular box corresponding formation respectively.
The present invention first makes fluid enter its chamber along cylindrical tube tangent line, form centrifugal force and produce outer whirlpool in its tank chamber, make large grain silt under the action of the centrifugal, inner circumferential cylinder wall along rounded cylindrical tank body declines, the muddy water of eddy flow forms outer eddy-currents, current stabilization revolves excessive plate isolates the clear water of the muddy water entered from bottom in cylindrical tube and its internal upper part overflow, play resistance from effect, and the larger fine deposit of muddy water medium viscosity enters gill formula filter separator, gill formula filter separator is made up of cube tubular box and branchial plate, branchial plate in gill formula filter separator is fixed in cube tubular box with the three dimensions angled manner of 5-85 °, relative to the face angle angle between the rectangle plane plate body of cube tubular box and horizontal plane all between 5-85 °, the opposing parallel wall of cube tubular box is distributed with limbers (mesh), form the sand discharge section of full reclining in three dimensions and cross clear water section, thus there is in each branchial plate both sides (in unit cheek chamber) the reverse shunting of solid-liquid that flows vertically to, further clear water is separated from the muddy water current of high sediment charge, fine deposit is also settled down to sand discharge bucket under gravity, assembled by sand discharge bucket, utilize waterpower to discharge to discharge from the bell mouth of sand discharge funnel, clear water in muddy water is separated further with sand grain, the clear water of isolated high clarity by the muddy water of the water inlet pipe input dividing bottom, filter tank tank chamber to arrange from solid-liquid thrust and rise, simultaneously, under the effect of eddy-currents outside, swirling water current in clear water in interior swirling flow premium on currency cylinder produces, clear water by the effect of interior swirling water current through interior swirling flow premium on currency cylinder rise to current stabilization revolve arrange above excessive plate revolve excessive room, overflowed from revolving excessive room by outlet pipe revolve the water conservancy diversion of excessive plate at current stabilization under, enter next procedure.Current stabilization revolves excessive plate relative level face tilt 1-5 °, to reduce the resistance that interior swirling water current causes, alleviate simultaneously from small-bore enter heavy caliber time the flow velocity bust water surface turbulent flow that causes, clear water is flowed out from the outlet pipe as overflow water channel reposefully.
The present invention has broken conventional at plane (two dimension) advection sedimentation Design Mode, also traditional inclined-plate clarifying basin and the pipe chute precipitating equipment with dual space incline structure is different from, prove through practice test, sediment transport emptying effectiveness of the present invention can significantly improve 19% and 73% than the flat cross section of the settling apparatus with swash plate and inclined pipe structrue respectively.Its sediment transport emptying effectiveness of the present invention is obviously higher, can further improve the clarity of the water body after sedimentation filtration, namely reduces its turbidity further.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the invention will be further described.
Fig. 1 is overall structure perspective diagram of the present invention;
Fig. 2 be in Fig. 1 A-A to overlooking sectional structure schematic diagram (relative Fig. 1);
Fig. 3 be gill formula filter separator embodiment 1 of the present invention a side outside depending on schematic diagram (there is the 3rd rectangle plane plate body of limbers group as front);
Fig. 4 is the side perspective structural representation of gill formula filter separator embodiment 1 of the present invention;
Fig. 5 is that B-B in Fig. 4 is to cross-sectional structure schematic diagram (relative Fig. 4);
Fig. 6 is the another side perspective structure schematic diagram (relative Fig. 4, to have the first rectangle plane plate body of limbers group as front) of gill formula filter separator embodiment 1 of the present invention;
Fig. 7 is a side perspective structure schematic diagram (to have the first rectangle plane plate body of limbers group as front) of gill formula filter separator embodiment 2 of the present invention;
Fig. 8 is the another side perspective structure schematic diagram (having the 3rd rectangle plane plate body of limbers group as front) of gill formula filter separator embodiment 2 of the present invention;
Fig. 9 is the cross-sectional structure schematic diagram (relative Fig. 4) of gill formula filter separator embodiment 3 of the present invention;
Figure 10 be each branchial plate in cube tubular box of the present invention relative to two rectangle plane plate bodys perpendicular in this cube tubular box, horizontal plane (space angle) stereogram (only as be convenient to understand branchial plate space obliquity schematic diagram);
Figure 11 be each branchial plate in cube tubular box of the present invention tilt relative to two rectangle plane plate bodys perpendicular in this cube tubular box face angle schematic diagram (only as be convenient to understand the face angle definition between branchial plate and rectangle plane plate body schematic diagram);
Figure 12 is the contour structures schematic diagram of branchial plate of the present invention.
Detailed description of the invention
A kind of hydraulic solid-liquid two phase separator, as depicted in figs. 1 and 2, comprise the solid-liquid be made up of the cylindrical tube 6 erect and sand discharge funnel 9 and divide filter tank, the bell mouth 10 of sand discharge funnel 9 vertically down, sand discharge funnel 9 is fixedly installed on the nozzle of cylindrical tube 6 lower end, the water inlet pipe 8 being communicated with the level in its chamber is fixedly installed at the foot of cylindrical tube 6, the outlet pipe 2 being communicated with the level in its chamber is fixedly installed at the topmost of cylindrical tube 6, the tangential direction of the circular nozzle that one end mouth of pipe 8a of water inlet pipe 8 divides the water inlet of filter tank to present from cylindrical tube 6 cross section as solid-liquid passes into the tank chamber that solid-liquid divides filter tank, the delivery port 2b that one end mouth of pipe 2a of outlet pipe 2 is arranged on cylindrical tube 6 barrel passes into the tank chamber that solid-liquid divides filter tank, it is flat current stabilization revolves excessive plate 6a that top in cylindrical tube 6 is arranged, it is inclined fixing that current stabilization revolves excessive plate 6a relative level face, the angle threshold scope that current stabilization revolves the face included angle X of excessive plate 6a and horizontal plane 19 is 1 °≤λ≤5 °, current stabilization revolve excessive plate 6a is provided with erect fixing in swirling flow premium on currency cylinder 13, interior swirling flow premium on currency cylinder 13 is positioned at the circle centre position of the circle that cylindrical tube 6 cross section presents as interior swirling flow delivery port, current stabilization revolves excessive plate 6a and is divided by solid-liquid the overall tank chamber of filter tank to be divided into revolving excessive room 7a and being positioned at the contour stealth cheek filter chamber 7b below it of the side of being located thereon, contour stealth cheek filter chamber 7b revolves excessive chamber 7a by described interior swirling flow premium on currency cylinder 13 connection, contour stealth cheek filter chamber 7b is communicated with water inlet pipe 8, revolve excessive chamber 7a and be communicated with outlet pipe 2, coordinate and be uniformly fixed with gill formula filter separator 5 being positioned at the contour stealth cheek filter chamber 7b on sand discharge funnel 9, as Fig. 3, shown in Fig. 4 and Fig. 6, each gill formula filter separator 5 is made up of cube tubular box 60 and branchial plate 17, whole box walls of cube tubular box 60 are by the first rectangle plane plate body 15b, second rectangle plane plate body 13a, 3rd rectangle plane plate body 15a and the 4th rectangle plane plate body 13b connects and composes, as shown in Figure 5, the adjacent two rectangle plane plate bodys of cube tubular box 60 are mutually vertical, relative two rectangle plane plate bodys are parallel to each other, be the closed rectangle of perimeter line to make the shape of cross section of cube tubular box 60, as shown in Figure 1, its whole rectangle plane plate body of each cube tubular box 60 is all erect and is fixedly installed, gill formula filter separator 5 is all fixedly mounted with along horizontal direction and forms at least one deck vertical separation cheek group, the uncovered 16a of rectangle that the corresponding formation of cube tubular box 60 two in upright state is relative, 16b is uncovered towards vertical direction, as Fig. 3 to Fig. 6 and Fig. 7, shown in Fig. 8, one rectangle of cube tubular box 60 is uncovered is positioned at cube tubular box 60 and upward topmost, its another rectangle is uncovered is positioned at cube tubular box 60 bottom and down, fixing gap is equipped with between the adjacent two cube tubular box 60 erect, cube tubular box 60 internal fixtion arranges the identical branchial plate 17 of N block, N >=2, each branchial plate 17 is the plate body in the parallelogram with four edges of boards, as depicted in figure 5 and figure 12, first edges of boards 17a of branchial plate 17 is relative with the 3rd edges of boards 17c to be parallel to each other, second edges of boards 17b of branchial plate 17 is relative with the 4th edges of boards 17d to be parallel to each other, spacing W between its first relatively isometric edges of boards 17a and the 3rd edges of boards 17c of each branchial plate 17 is greater than the spacing J between the first rectangle plane plate body 15b and the 3rd rectangle plane plate body 15a, as Fig. 3, Fig. 4 and Fig. 6 and Fig. 7, shown in Fig. 8, the first rectangle plane plate body 15b that first edges of boards 17a of each branchial plate 17 is relative with cube tubular box 60 respectively with the 3rd edges of boards 17c contacts with the 3rd rectangle plane plate body 15a and affixed, as shown in Figure 5, its the second edges of boards 17b of each branchial plate 17 and the first rectangle plane plate body 15b, the first right angled triangle hole 18a is formed between second rectangle plane plate body 13a, and its 4th edges of boards 17d of each branchial plate 17 and the 3rd rectangle plane plate body 15a, the second right angled triangle hole 18b is formed between 4th rectangle plane plate body 13b, or as shown in Figure 9, second edges of boards 17b of each branchial plate 17 and the first rectangle plane plate body 15b, second rectangle plane plate body 13a, the first right-angled trapezium hole 21a is formed between 3rd rectangle plane plate body 15a, 4th edges of boards 17d of each branchial plate 17 and the 3rd rectangle plane plate body 15a, 4th rectangle plane plate body 13b, the second right-angled trapezium hole 21b is formed between first rectangle plane plate body 15b, as Fig. 4, shown in Fig. 6 to Fig. 8, all branchial plates 17 vertically arrange point-blank along the length direction of cube tubular box 60 with relative level face 19, the box chamber of cube tubular box 60 is separated into N-1 unit cheek chamber 160 by N block branchial plate 17, each unit cheek chamber 160 is all often between adjacent two pieces of branchial plates 17, as shown in figs. 5 and 9, its second edges of boards of each branchial plate 17 17b and the 3rd edges of boards 17c is formed the most advanced and sophisticated A1 of the first dihedral are with its first edges of boards 17a is relative with the most advanced and sophisticated A2 of the second dihedral formed between the 4th edges of boards 17d and its equal angle δ is acute angle, four pieces of the opposed square tubular box 60 of all branchial plates 17 rectangle plane plate bodys and horizontal plane 19 erect and integral inclined, as shown in Fig. 3 to Fig. 9 and Figure 10, parallel each other between all branchial plates 17, all branchial plates 17 and the first rectangle plane plate body 15b or and the 3rd rectangular flat face body 15a between its angle threshold scope of face angle α be 5 °≤α≤85 °, all branchial plates 17 and the second rectangle plane plate body 13a or and the 4th rectangle plane plate body 13b between its angle threshold scope of face angle β be 5 °≤β≤85 °, its angle threshold scope of face angle theta between all branchial plates 17 and horizontal plane 19 is 5 °≤θ≤85 °, as shown in Figure 10, the branchial plate 17 of complanation is in plane 20, the plane at branchial plate 17 place represented in Figure 11 overlaps with plane 20, the plane that locus its place plane of branchial plate 17 of fixing extends around it is plane 20, plane 20 and the first rectangle plane plate body 15b, second rectangle plane plate body 13a and horizontal plane 19 intersect respectively (even if non-intersect, its space angle still exists), and corresponding three angles forming correspondence, certainly, first rectangle plane plate body 15b, second rectangle plane plate body 13a is vertical with horizontal plane 19, wherein, face angle α is the fixing three-dimensional angle of (crossing form) between the first rectangle plane plate body 15b (or with the 3rd rectangular flat face body 15a), face angle β is the fixing three-dimensional angle (intersecting and form) between the second rectangle plane plate body 13a (the 4th rectangle plane plate body 13b), face angle theta is the three-dimensional angle fixed with (crossing form) between horizontal plane 19, face included angle=﹛ α shown in Figure 11, β ﹜, 5 °≤φ≤85 °, the solid angle that formed for two Plane intersects defined in solid geometry of said included angle herein, as shown in Fig. 3 to Fig. 9, N row limbers group is set respectively on the first rectangle plane plate body 15b and on the 3rd rectangle plane plate body 15a, often arrange limbers group to be made up of M limbers 14, M >=2, often row limbers each branchial plate 17 of group corresponding matching that first rectangle plane plate body 15b and the 3rd rectangle plane plate body 15a are arranged respectively, the limbers group of often arranging that first rectangle plane plate body 15b is arranged is positioned at the orthographic projection boundary of each branchial plate 17 correspondence on the first rectangle plane plate body 15b, the limbers group of often arranging that 3rd rectangle plane plate body 15a is arranged is positioned at the orthographic projection boundary of each branchial plate 17 correspondence on the 3rd rectangle plane plate body 15a, described contour stealth cheek filter chamber 7b arranges limbers group by two of each branchial plate 17 above-mentioned and corresponding and is communicated with its corresponding unit cheek chamber 160, adjacent two unit cheek chambeies 160 are all interconnected by above-mentioned right angled triangle hole or right-angled trapezium hole, and unit cheek chamber 160 is also by the rectangle uncovered connection contour stealth cheek filter chamber 7b of the most upper and lower end of above-mentioned right angled triangle hole or right-angled trapezium hole and cube tubular box 60 corresponding formation respectively.
As shown in Figure 1, muddy water containing sand grain is tangentially flowed into its chamber from cylindrical tube 6 foot along its barrel by the present invention, flow into rotating around the axis that cylindrical tube 6 is extending longitudinally containing silt muddy water in cylindrical tube 6 chambeies, produce outer swirling water current, make containing the proportion in silt muddy water larger, viscosity is larger, (particle is larger) thick silt 11 gets rid of on the inner periphery barrel of cylindrical tube 6 because of centrifugal force, and along the inner periphery barrel of cylindrical tube 6 because gravity weight is in sand discharge funnel 9, gathered by sand discharge funnel 9, and discharge downwards from the bell mouth 10 of sand discharge funnel 9 by gravity, and the cyclonic action that the current 12 being lowered turbidity are subject to the muddy water entered through water inlet pipe 8 firmly rises, and carry out precipitate and separate through gill formula filter separator 5, gill formula filter separator 5 can be less by the proportion in muddy water, viscosity is less, thin mud (particle) the husky precipitate and separate of (particle is less or less than normal) out, the turbidity of muddy water is made obviously to reduce further, precipitated fine deposit is discharged by the bell mouth 10 of Action of Gravity Field through sand discharge funnel 9 again, by the high clarity clear water separating treatment from muddy water after gill formula filter separator 5 further process, what in producing by interior swirling flow premium on currency cylinder, from contour stealth cheek filter chamber 7b, swirling water current upwards flow to that the current stabilization with relative level face tilt revolves excessive plate 6a through swirling flow premium on currency cylinder again revolves in excessive room 7a, overflow from the outlet pipe revolving excessive plate 6a the top 3 near current stabilization.
As shown in Figure 1, top in described contour stealth cheek filter chamber 7b is fixed wtih bracing frame 4, its cube tubular box 60 of the gill formula filter separator 5 of all settings is in strip, its the top of the cube tubular box 60 erect is all affixed with bracing frame 4 body, makes gill formula filter separator 5 fixedly be suspended on the below of bracing frame 4.
As shown in Figure 1, longitudinal total length L of cube tubular box 60 and bracing frame 4 are 0.3≤(L/D)≤0.6 apart from the ratio range of the height D bottom cylindrical tube 6.
As shown in Figure 1, to revolve the top 3 of excessive plate 6a concordant with outlet pipe 2 lower side tube wall 30 for current stabilization.
As shown in Fig. 3 to Fig. 9, the aperture size of limbers 14 is 15-20mm.Described α=45 °, β=45 °, θ=60 °.50°≤δ≤55°。The two limbers groups corresponding to each branchial plate 17 linearly arrange respectively, the first limbers group in two limbers groups is pressed close to branchial plate 17 first edges of boards 17a and is laid, the second limbers group in two limbers groups is pressed close to branchial plate 17 the 3rd edges of boards 17c and is laid, and above-mentioned its straight line be respectively arranged in of two limbers groups is parallel with the first edges of boards 17a with Qi tri-edges of boards 17c of branchial plate 17.
As shown in Figure 1, the barrel 1 of interior swirling flow premium on currency cylinder 13 upper end nozzle is concordant with the upper face that current stabilization revolves excessive plate 6a, and revolves excessive plate 6a with current stabilization and be connected as a single entity.
Described current stabilization revolves excessive plate 6a, cube tubular box 60 and branchial plate 17 and forms by PVC board, and the thickness that current stabilization revolves excessive plate 6a, cube tubular box 60 and branchial plate 17 respective is 3mm.
Claims (10)
1. a hydraulic solid-liquid two phase separator, comprise the solid-liquid be made up of the cylindrical tube erect (6) and sand discharge funnel (9) and divide filter tank, the bell mouth (10) of sand discharge funnel (9) vertically down, sand discharge funnel (9) is fixedly installed on the nozzle of cylindrical tube (6) lower end, the water inlet pipe (8) being communicated with the level in its chamber is fixedly installed at the foot of cylindrical tube (6), the outlet pipe (2) being communicated with the level in its chamber is fixedly installed at the topmost of cylindrical tube (6), the tangential direction of the circular nozzle that one end mouth of pipe (8a) of water inlet pipe (8) divides the water inlet of filter tank to present from cylindrical tube (6) cross section as solid-liquid passes into the tank chamber that solid-liquid divides filter tank, the delivery port (2b) that one end mouth of pipe (2a) of outlet pipe (2) is arranged on cylindrical tube (6) barrel passes into the tank chamber that solid-liquid divides filter tank, it is characterized in that: it is flat current stabilization revolves excessive plate (6a) that the top in cylindrical tube (6) is arranged, it is inclined fixing that current stabilization revolves excessive plate (6a) relative level face, it is 1 °≤λ≤5 ° that current stabilization revolves excessive plate (6a) with the angle threshold scope of the face included angle X of horizontal plane (19), the interior swirling flow premium on currency cylinder (13) excessive plate (6a) being provided with and erectting and fix is revolved at current stabilization, interior swirling flow premium on currency cylinder (13) is positioned at the circle centre position of the circle that cylindrical tube (6) cross section presents as interior swirling flow delivery port, current stabilization revolves excessive plate (6a) and is divided by solid-liquid the overall tank chamber of filter tank to be divided into revolving excessive room (7a) and being positioned at the contour stealth cheek filter chamber (7b) below it of the side of being located thereon, contour stealth cheek filter chamber (7b) revolves excessive chamber (7a) by described interior swirling flow premium on currency cylinder (13) connection, contour stealth cheek filter chamber (7b) is communicated with water inlet pipe (8), revolve excessive chamber (7a) and be communicated with outlet pipe (2), being positioned at, the cooperation of the contour stealth cheek filter chamber (7b) on sand discharge funnel (9) is uniform is fixed with gill formula filter separator (5), each gill formula filter separator (5) is made up of cube tubular box (60) and branchial plate (17), whole box walls of cube tubular box (60) are by the first rectangle plane plate body (15b), second rectangle plane plate body (13a), 3rd rectangle plane plate body (15a) and the 4th rectangle plane plate body (13b) connect and compose, the adjacent two rectangle plane plate bodys of cube tubular box (60) are mutually vertical, relative two rectangle plane plate bodys are parallel to each other, be the closed rectangle of perimeter line to make the shape of cross section of cube tubular box (60), its whole rectangle plane plate body of each cube tubular box (60) is all erect and is fixedly installed, gill formula filter separator (5) is all fixedly mounted with along horizontal direction and forms at least one deck vertical separation cheek group, the rectangle uncovered (16a) that cube tubular box (60) corresponding formation two in upright state is relative, (16b) uncovered towards vertical direction, one rectangle of cube tubular box (60) is uncovered is positioned at cube tubular box (60) and upward topmost, its another rectangle is uncovered is positioned at cube tubular box (60) bottom and down, fixing gap is equipped with between the adjacent two cube tubular box (60) erect, cube tubular box (60) internal fixtion arranges the identical branchial plate (17) of N block, N >=2, each branchial plate (17) is the plate body in the parallelogram with four edges of boards, first edges of boards (17a) of branchial plate (17) are relative with the 3rd edges of boards (17c) to be parallel to each other, second edges of boards (17b) of branchial plate (17) are relative with the 4th edges of boards (17d) to be parallel to each other, spacing W between each branchial plate (17) its relatively isometric the first edges of boards (17a) and the 3rd edges of boards (17c) is greater than the spacing J between the first rectangle plane plate body (15b) and the 3rd rectangle plane plate body (15a), the first rectangle plane plate body (15b) that first edges of boards (17a) of each branchial plate (17) are relative with cube tubular box (60) respectively with the 3rd edges of boards (17c) contacts with the 3rd rectangle plane plate body (15a) and affixed, its second edges of boards (17b) of each branchial plate (17) and the first rectangle plane plate body (15b), the first right angled triangle hole (18a) is formed between second rectangle plane plate body (13a), and its 4th edges of boards (17d) of each branchial plate (17) and the 3rd rectangle plane plate body (15a), the second right angled triangle hole (18b) is formed between 4th rectangle plane plate body (13b), or second edges of boards (17b) of each branchial plate (17) and the first rectangle plane plate body (15b), second rectangle plane plate body (13a), the first right-angled trapezium hole (21a) is formed between 3rd rectangle plane plate body (15a), 4th edges of boards (17d) and the 3rd rectangle plane plate body (15a) of each branchial plate (17), 4th rectangle plane plate body (13b), the second right-angled trapezium hole (21b) is formed between first rectangle plane plate body (15b), all branchial plates (17) vertically arrange point-blank along the length direction of cube tubular box (60) with relative level face (19), the box chamber of cube tubular box (60) is separated into N-1 unit cheek chamber (160) by N block branchial plate (17), each unit cheek chamber (160) is all positioned at often between adjacent two pieces of branchial plates (17), its second edges of boards (17b) of each branchial plate (17) are with the first dihedral tip (A1) that the 3rd edges of boards (17c) are formed is relative with the second dihedral tip (A2) formed between its first edges of boards (17a) with the 4th edges of boards (17d) and its equal angle δ is acute angle, four pieces of the opposed square tubular box of all branchial plates (17) (60) rectangle plane plate bodys and horizontal plane (19) erect and integral inclined, parallel each other between all branchial plates (17), all branchial plates (17) and the first rectangle plane plate body (15b) or and the 3rd rectangle plane plate body (15a) between its angle threshold scope of face angle α be 5 °≤α≤85 °, all branchial plates (17) and the second rectangle plane plate body (13a) or and the 4th rectangle plane plate body (13b) between its angle threshold scope of face angle β be 5 °≤β≤85 °, its angle threshold scope of face angle theta between all branchial plates (17) and horizontal plane (19) is 5 °≤θ≤85 °, at the first rectangle plane plate body (15b), above with on the 3rd rectangle plane plate body (15a) N row limbers group is set respectively, often arrange limbers group to be made up of M limbers (14), M >=2, the often row limbers each branchial plate of group corresponding matching (17) that first rectangle plane plate body (15b) and the 3rd rectangle plane plate body (15a) are arranged respectively, the upper often row limbers group arranged of first rectangle plane plate body (15b) is positioned at the corresponding orthographic projection boundary on the first rectangle plane plate body (15b) of each branchial plate (17), the upper often row limbers group arranged of 3rd rectangle plane plate body (15a) is positioned at the corresponding orthographic projection boundary on the 3rd rectangle plane plate body (15a) of each branchial plate (17), described contour stealth cheek filter chamber (7b) is arranged limbers group by two of above-mentioned and corresponding each branchial plate (17) and is communicated with its corresponding unit cheek chamber (160), adjacent two unit cheek chambeies (160) are all interconnected by above-mentioned right angled triangle hole or right-angled trapezium hole, and unit cheek chamber (160) is also by rectangle uncovered connection contour stealth cheek filter chamber (7b) of the most upper and lower end of above-mentioned right angled triangle hole or right-angled trapezium hole and cube tubular box (60) corresponding formation respectively.
2. hydraulic solid-liquid two phase separator according to claim 1, it is characterized in that: the top in described contour stealth cheek filter chamber (7b) is fixed wtih bracing frame (4), its cube tubular box (60) of the gill formula filter separator (5) of all settings is in strip, its the top of the cube tubular box (60) erect is all affixed with bracing frame (4) body, makes gill formula filter separator (5) fixedly be suspended on the below of bracing frame (4).
3. hydraulic solid-liquid two phase separator according to claim 2, is characterized in that: the ratio range of the height D of longitudinal total length L of cube tubular box (60) and bracing frame (4) distance cylindrical tube (6) bottom is 0.3≤(L/D)≤0.6.
4. hydraulic solid-liquid two phase separator according to claim 1, is characterized in that: the top (3) that current stabilization revolves excessive plate (6a) is concordant with outlet pipe (2) lower side tube wall (30).
5. hydraulic solid-liquid two phase separator according to claim 1, is characterized in that: the aperture size of limbers (14) is 15-20mm.
6. hydraulic solid-liquid two phase separator according to claim 1, is characterized in that: described α=45 °, β=45 °, θ=60 °.
7. hydraulic solid-liquid two phase separator according to claim 1, is characterized in that: 50 °≤δ≤55 °.
8. hydraulic solid-liquid two phase separator according to claim 1, it is characterized in that: the two limbers groups corresponding to each branchial plate (17) linearly arrange respectively, the first limbers group in two limbers groups is pressed close to branchial plate (17) first edges of boards (17a) and is laid, the second limbers group in two limbers groups is pressed close to branchial plate (17) the 3rd edges of boards (17c) and is laid, and above-mentioned its straight line be respectively arranged in of two limbers groups is parallel with its 3rd edges of boards (17c) with first edges of boards (17a) of branchial plate (17).
9. hydraulic solid-liquid two phase separator according to claim 1, it is characterized in that: the barrel (1) of interior swirling flow premium on currency cylinder (13) upper end nozzle is concordant with the upper face that current stabilization revolves excessive plate (6a), and revolve excessive plate (6a) with current stabilization and be connected as a single entity.
10. hydraulic solid-liquid two phase separator according to claim 1, it is characterized in that: described current stabilization revolves excessive plate (6a), cube tubular box (60) and branchial plate (17) and forms by PVC board, and the thickness that current stabilization revolves excessive plate (6a), cube tubular box (60) and branchial plate (17) respective is 3mm.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| EP2886177A1 (en) * | 2013-12-20 | 2015-06-24 | Rio Tinto Alcan International Limited | Settler and method for separating clarified liquid from mineral slurries |
| CN104225972B (en) * | 2014-10-14 | 2015-11-18 | 成都育芽科技有限公司 | A kind of small-scale sewage settler |
| CN105498943B (en) * | 2015-12-16 | 2018-03-06 | 通辽矽砂工业公司 | Current stabilization uses silica sand pump pond |
| CN105854409B (en) * | 2016-05-31 | 2018-05-29 | 湛江港石化码头有限责任公司 | A kind of impurity separating device for petroleum storage tank |
| CN109499148A (en) * | 2018-12-23 | 2019-03-22 | 新疆水利水电科学研究院 | A kind of fish gill formula dynamic continuously filters constant-current stabilizer |
| CN109678301A (en) * | 2019-02-21 | 2019-04-26 | 新疆德安环保科技股份有限公司 | Each door type sewage disposal device |
| CN109650429B (en) * | 2019-02-21 | 2021-02-09 | 新疆德安环保科技股份有限公司 | Carbide slag recycling treatment process |
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| CN201006341Y (en) * | 2006-09-25 | 2008-01-16 | 邱秀云 | Vertical density flow type mixed flow separating lamella |
| CN201441862U (en) * | 2009-01-09 | 2010-04-28 | 青岛东岳泡花碱有限公司 | Sodium silicate phase separator |
| CN202237569U (en) * | 2011-10-12 | 2012-05-30 | 新疆德安环保科技有限公司 | Hydraulic solid-liquid two-phase separator |
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| JPS5877795A (en) * | 1981-10-30 | 1983-05-11 | Sanshu Kaken Kogyo Kk | Solid-liquid separator |
| CN201006341Y (en) * | 2006-09-25 | 2008-01-16 | 邱秀云 | Vertical density flow type mixed flow separating lamella |
| CN201441862U (en) * | 2009-01-09 | 2010-04-28 | 青岛东岳泡花碱有限公司 | Sodium silicate phase separator |
| CN202237569U (en) * | 2011-10-12 | 2012-05-30 | 新疆德安环保科技有限公司 | Hydraulic solid-liquid two-phase separator |
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Address after: 830002 Urumqi economic and Technological Development Zone (Toutun River District), Taishan street, No. 100, No. Patentee after: Xinjiang De'an environmental Polytron Technologies Inc Address before: 830002 Urumqi economic and Technological Development Zone (Toutun River District), Taishan street, No. 100, No. Patentee before: Xinjiang Dean Environmental Protection Technology Co., Ltd. |