CN202237569U

CN202237569U - Hydraulic solid-liquid two-phase separator

Info

Publication number: CN202237569U
Application number: CN2011203861305U
Authority: CN
Inventors: 李洪; 王磊
Original assignee: Xinjiang Dean Environmental Protection Technology Co Ltd
Current assignee: Xinjiang Dean Environmental Protection Technology Co Ltd
Priority date: 2011-10-12
Filing date: 2011-10-12
Publication date: 2012-05-30
Anticipated expiration: 2021-10-12

Abstract

The utility model discloses a hydraulic solid-liquid two-phase separator which comprises a cylindrical barrel body. A flat inclined steady flow swirl overflow plate is arranged at the upper part inside the cylindrical barrel body, and the steady flow swirl overflow plate partitions the entire tank cavity of a solid-liquid separate filtering tank into a swirl overflow chamber above and an outer vortex gill filtering chamber below; the central position of the steady flow swirl overflow plate is provided with an inner vortex water lifting barrel, and the outer vortex gill filtering chamber is communicated with the swirl overflow cavity through the inner vortex water lifting barrel; and fixedly installed gill type filter separators are evenly distributed in the outer vortex gill filtering chamber above a sand discharge hopper, each gill type filter separator comprises a cubic tube type box body and gills, the gills fixedly arranged in the cubic tube type box body are entirely inclined in relative to the rectangular surface plate bodies and the horizontal plane of the cubic tube type box body, the gills are parallel to each other, and the gills respectively form gaps together with two opposite rectangular surface plate bodies of the cubic tube type box body. The sand transportation and water transportation efficiency of the hydraulic solid-liquid two-phase separator is obviously improved, and the clarity of precipitated and filter water can be further increased.

Description

Waterpower solid-liquid two phase separator

Technical field

The utility model relates to the water treatment deposition device that the liquid towards non-homogeneous mixture carries out filtration treatment, and solid particle in the turbidity and clear water are separated from each other to filter out clear water, belongs to muddy water sedimentation separation equipment, particularly waterpower solid-liquid two phase separator.

Background technology

Existing tube settler is the sedimentation basin that in the settling zone, is provided with inclined tube; In the settling zone of flat flow or vertical sedimentation basin, utilize the parallel pipe or the parallelpiped (honeycomb filler also capable of using) that tilt to be separated into a series of shallow layer precipitating layers; The husky mud of the deposition that is processed is motion and separation each other in each deposition shallow-layer; Be divided into contrary (different) to stream, three kinds of different separate modes of concurrent and reverse flow according to its mutual direction of motion, (or in parallel pipe) is equivalent to a very shallow sedimentation basin between per two inclined paralled plates, and it has utilized lamina flow principle; The disposal ability and the water treatment efficiency of sedimentation basin have been improved; But its sediment transport emptying effectiveness is lower, and the water of post precipitation still passes through clearly inadequately, and its clarity is still lower.

The utility model content

The purpose of the utility model is to provide a kind of waterpower solid-liquid two phase separator, and its sediment transport emptying effectiveness is obviously higher, can further improve the clarity of the water body after sedimentation is filtered.

The purpose of the utility model is achieved in that a kind of waterpower solid-liquid two phase separator; Comprise that the solid-liquid of being made up of cylindrical tube of erectting and sand discharge funnel divides 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; Fixedly installing the water inlet pipe of the level that is communicated with its chamber at the foot of cylindrical tube, fixedly installing the outlet pipe of the level that is communicated with its chamber at the topmost of cylindrical tube, an end mouth of pipe of water inlet pipe divides filter tank as solid-liquid water inlet feeds the jar chamber that solid-liquid divides filter tank from the tangential direction of the circular nozzle that the cylindrical tube cross section is appeared; The delivery port that the one end mouth of pipe of outlet pipe is provided with on the cylindrical tube barrel feeds the jar chamber that solid-liquid divides filter tank; Top in cylindrical tube is being provided with and is being flat current stabilization and revolves excessive plate, and it is inclined fixing that current stabilization revolves the relative horizontal plane of plate that overflows, and the angle threshold scope that current stabilization revolves the face included angle X of overflow plate and horizontal plane is 1 °≤λ≤5 °; Current stabilization revolves the plate that overflows and is provided with the fixing interior swirling flow premium on currency tube of setting; Interior swirling flow premium on currency tube is positioned at the circle centre position of the circle that the cylindrical tube cross section appeared as interior swirling flow delivery port, and current stabilization revolves the plate that overflows and divides the whole jar chamber of filter tank to be divided into to be positioned at revolving of its top overflow chamber and the outer eddy flow cheek filter chamber that is positioned at its below with solid-liquid, and outer eddy flow cheek filter chamber is communicated with through swirling flow premium on currency tube in described and revolves excessive chamber; Outer eddy flow cheek filter chamber is communicated with water inlet pipe, revolves the chamber of overflowing and is communicated with outlet pipe; Cooperate to be uniformly distributed with and be fixed with gill formula filter separator being positioned at outer eddy flow cheek filter chamber on the 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 connected and composed by the first rectangle plane plate body, the second rectangle plane plate body, the 3rd rectangle plane plate body and the 4th rectangle plane plate body; The adjacent two rectangle plane plate bodys of cube tubular box are vertical each other; Relative two rectangle plane plate bodys are parallel to each other; So that the shape of cross section of cube tubular box is the closed rectangle of perimeter line; Its whole rectangle plane plate bodys of each cube tubular box are all erect and are fixedly installed, and gill formula filter separator all installs along horizontal direction and constitutes the vertical separation cheek of one deck group at least, and it is uncovered uncovered towards vertical direction to be the relative rectangle of the corresponding formation of the cube tubular box of upright state two; One rectangle of cube tubular box is uncovered to be positioned at the cube tubular box and up topmost; Its another rectangle is uncovered to be positioned at the cube tubular box bottom and down, is equipped with fixed gap between the cube tubular box of adjacent two settings, is fixedly installing the identical branchial plate of N piece in the cube tubular box; N>=2; Each branchial plate is the plate body that is the parallelogram with four edges of boards, and first edges of boards and the 3rd edges of boards of branchial plate are parallel to each other relatively, and second edges of boards and the 4th edges of boards of branchial plate are parallel to each other relatively; Its first isometric relatively edges of boards of each branchial plate and the spacing W between the 3rd edges of boards are greater than the spacing J between the first rectangle plane plate body and the 3rd rectangle plane plate body, and the first rectangle plane plate body that first edges of boards of each branchial plate are relative with the cube tubular box respectively with the 3rd edges of boards contacts with the 3rd rectangle plane plate body and be affixed; Form the first right angled triangle hole between its second edges of boards of each branchial plate and the first rectangle plane plate body, the second rectangle plane plate body; And form the second right angled triangle hole between its 4th edges of boards of each branchial plate and the 3rd rectangle plane plate body, the 4th rectangle plane plate body; Perhaps form the first right-angled trapezium hole between second edges of boards of each branchial plate and the first rectangle plane plate body, the second rectangle plane plate body, the 3rd rectangle plane plate body, form the second right-angled trapezium hole between the 4th edges of boards of each branchial plate and the 3rd rectangle plane plate body, the 4th rectangle plane plate body, the first rectangle plane plate body; All branchial plates are vertically arranged point-blank with relative horizontal plane along the length direction of cube tubular box; The box chamber of cube tubular box is separated into cheek chamber, N-1 unit by N piece branchial plate; Each cheek chamber, unit is all between every adjacent two branchial plates; First dihedral that its second edges of boards of each branchial plate and the 3rd edges of boards form most advanced and sophisticated with its first edges of boards and the 4th edges of boards between relative and its angle same δ in second dihedral tip that forms be acute angle; The rectangle plane plate body of four settings of the opposed square tubular box of all branchial plates and horizontal plane and integral inclination; 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 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 the face angle theta between all branchial plates and the horizontal plane is 5 °≤θ≤85 °; On the first rectangle plane plate body with on the 3rd rectangle plane plate body N row limbers group is being set respectively; Every row limbers group is made up of M limbers; M>=2; Every row limbers each branchial plate of group corresponding matching that on the first rectangle plane plate body and the 3rd rectangle plane plate body, is provided with respectively; The every row limbers group that is provided with on the first rectangle plane plate body is positioned at the orthographic projection boundary of each branchial plate correspondence on the first rectangle plane plate body, and the every row limbers group that is provided with on the 3rd rectangle plane plate body is positioned at the orthographic projection boundary of each branchial plate correspondence on the 3rd rectangle plane plate body; Described outer eddy flow cheek filter chamber is communicated with its corresponding cells cheek chamber through above-mentioned with two row limbers groups of corresponding each branchial plate; Cheek chamber, adjacent two unit all is interconnected through above-mentioned right angled triangle hole or right-angled trapezium hole, and cheek chamber, unit is also through the upper and lower end of above-mentioned right angled triangle hole or right-angled trapezium hole and the cube tubular box outer eddy flow cheek filter chamber of the uncovered connection of rectangle of corresponding formation respectively.

The utility model makes fluid get into its chamber along the cylindrical tube tangent line earlier, and whirlpool outside formation centrifugal force produces in its jar chamber makes big grain silt under the action of the centrifugal; Interior all barrels along the rounded cylindrical tank body descend, and the muddy water of eddy flow forms outer eddy-currents, and current stabilization revolves the plate that overflows will isolate from the muddy water of bottom entering in the cylindrical tube and the clear water of its internal upper part overflow; Play the effect that resistance is left; And the bigger fine deposit of muddy water medium viscosity gets into gill formula filter separator, and gill formula filter separator is made up of cube tubular box and branchial plate, and the branchial plate in the gill formula filter separator is fixed in the cube tubular box with 5-85 ° three dimensions inclination mode; With respect to the rectangle plane plate body of cube tubular box and the face angle angle between the horizontal plane all between 5-85 °; On the opposing parallel wall of cube tubular box, be distributed with limbers (mesh), the husky section of row that is formed in full reclining in the three dimensions with cross the clear water section, thereby in each branchial plate both sides (in the cheek chamber, unit) occur vertical current to the reverse shunting of solid-liquid; Further clear water is separated from the muddy water current of high sediment charge; Fine deposit is the husky bucket of the row of being settled down under the gravity effect also, assembles through arranging husky bucket, utilizes waterpower to discharge from the bell mouth of sand discharge funnel and discharges; Clear water in the muddy water is further separated with sand grain; The clear water of isolated high clarity rises by the thrust of the muddy water of the water inlet pipe input that divides bottom, filter tank jar chamber to be provided with from solid-liquid, simultaneously, and outside under the effect of eddy-currents; Produce interior swirling water current through the clear water in the interior swirling flow premium on currency tube; The effect of clear water through interior swirling water current rises to current stabilization through interior swirling flow premium on currency tube and revolves the excessive chamber of revolving that the plate top of overflowing is provided with, and revolves at current stabilization under the water conservancy diversion of the plate that overflows to overflow through outlet pipe from revolving the chamber of overflowing, and gets into next procedure.Current stabilization revolves 1-5 ° of the relative horizontal plane inclination of plate of overflowing, and with the resistance that swirling water current in reducing causes, the water surface turbulent flow that the flow velocity bust causes when alleviating from small-bore entering heavy caliber simultaneously flows out clear water reposefully from the outlet pipe as the overflow water channel.

The utility model has been broken conventional (two dimension) advection sedimentation Design Mode on the plane; Also be different from traditional inclined-plate clarifying basin and tube settling equipment with dual space incline structure; Prove that through practice test the utility model sediment transport emptying effectiveness can significantly improve 19% and 73% than the flat cross section of the settling apparatus with swash plate and inclined tube structure respectively.Its sediment transport emptying effectiveness of the utility model is obviously higher, can further improve the clarity of the water body after sedimentation is filtered, and promptly further reduces its turbidity.

Description of drawings

To combine accompanying drawing that the utility model is described further below.

Fig. 1 is the overall structure perspective diagram of the utility model;

Fig. 2 for A-A among Fig. 1 to overlooking sectional structure sketch map (Fig. 1 relatively);

Fig. 3 looks sketch map (the 3rd rectangle plane plate body with limbers group is as the front) for outside the side of the utility model gill formula filter separator embodiment 1;

Fig. 4 is the side perspective structural representation of the utility model gill formula filter separator embodiment 1;

Fig. 5 is that B-B among Fig. 4 is to cross-sectional structure sketch map (relatively Fig. 4);

Fig. 6 is the another side perspective structure sketch map (relative Fig. 4, with the first rectangle plane plate body with limbers group as the front) of the utility model gill formula filter separator embodiment 1;

Fig. 7 is the side perspective structural representation of the utility model gill formula filter separator embodiment 2 (with the first rectangle plane plate body with limbers group as the front);

Fig. 8 is the another side perspective structure sketch map (the 3rd rectangle plane plate body with limbers group is as the front) of the utility model gill formula filter separator embodiment 2;

Fig. 9 is the cross-sectional structure sketch map (Fig. 4 relatively) of the utility model gill formula filter separator embodiment 3;

Figure 10 is each branchial plate in the utility model cube tubular box perpendicular two rectangle plane plate bodys in this cube tubular box, (space angle) stereogram that horizontal plane the tilts sketch map of the usefulness of being convenient to understand branchial plate space obliquity (only as) relatively;

The face angle sketch map that Figure 11 tilts for two perpendicular rectangle plane plate bodys in relative this cube tubular box of each branchial plate in the utility model cube tubular box (only as the sketch map of being convenient to understand the usefulness of the face angle definition between branchial plate and the rectangle plane plate body);

Figure 12 is the contour structures sketch map of the utility model branchial plate.

The specific embodiment

A kind of waterpower solid-liquid two phase separator; As depicted in figs. 1 and 2; Comprise that the solid-liquid of being made up of cylindrical tube of erectting 6 and sand discharge funnel 9 divides filter tank; The bell mouth 10 of sand discharge funnel 9 vertically down; Sand discharge funnel 9 is fixedly installed on the cylindrical tube 6 lower end nozzles; Fixedly installing the water inlet pipe 8 of the level that is communicated with its chamber at the foot of cylindrical tube 6, fixedly installing the outlet pipe 2 of the level that is communicated with its chamber at the topmost of cylindrical tube 6, an end mouth of pipe 8a of water inlet pipe 8 divides filter tank as solid-liquid water inlet feeds the jar chamber that solid-liquid divides filter tank from the tangential direction of the circular nozzle that cylindrical tube 6 cross sections are appeared; The delivery port 2b that one end mouth of pipe 2a of outlet pipe 2 is provided with on cylindrical tube 6 barrels feeds the jar chamber that solid-liquid divides filter tank; Top in cylindrical tube 6 is being provided with and is being flat current stabilization and revolves the plate 6a that overflows, and it is inclined fixing that current stabilization revolves the relative horizontal plane of plate 6a that overflows, and the angle threshold scope that current stabilization revolves the face included angle X of overflow plate 6a and horizontal plane 19 is 1 °≤λ≤5 °; Current stabilization revolves the plate 6a that overflows and is provided with the fixing interior swirling flow premium on currency tube 13 of setting; Interior swirling flow premium on currency tube 13 is positioned at the circle centre position of the circle that cylindrical tube 6 cross sections are appeared as interior swirling flow delivery port, and current stabilization revolves the plate 6a that overflows and divides the whole jar chamber of filter tank to be divided into to be positioned at revolving of its top overflow chamber 7a and the outer eddy flow cheek filter chamber 7b that is positioned at its below with solid-liquid, and outer eddy flow cheek filter chamber 7b is communicated with through swirling flow premium on currency tube in described 13 and revolves the chamber 7a that overflows; Outer eddy flow cheek filter chamber 7b is communicated with water inlet pipe 8, revolves the chamber 7a that overflows and is communicated with outlet pipe 2; Cooperate to be uniformly distributed with and be fixed with gill formula filter separator 5 being positioned at outer eddy flow cheek filter chamber 7b on the sand discharge funnel 9; Like Fig. 3, Fig. 4 and shown in Figure 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 connected and composed by the first rectangle plane plate body 15b, the second rectangle plane plate body 13a, the 3rd rectangle plane plate body 15a and the 4th rectangle plane plate body 13b; As shown in Figure 5, the adjacent two rectangle plane plate bodys of cube tubular box 60 are vertical each other, and relative two rectangle plane plate bodys are parallel to each other; So that the shape of cross section of cube tubular box 60 is the closed rectangle of perimeter line; As shown in Figure 1, each cube tubular box 60 its whole rectangle plane plate body is all erect and is fixedly installed, and gill formula filter separator 5 all installs along horizontal direction and constitutes the vertical separation cheek of one deck group at least; It is uncovered towards vertical direction to be the corresponding formation of the cube tubular box 60 of the upright state two relative uncovered 16a of rectangle, 16b; Like Fig. 3 to Fig. 6 and Fig. 7, shown in Figure 8, a rectangle of cube tubular box 60 is uncovered to be positioned at cube tubular box 60 and, its another rectangle is uncovered to be positioned at cube tubular box 60 bottom and down topmost up; Be equipped with fixed gap between the cube tubular box 60 of adjacent two settings; Fixedly installing the identical branchial plate of N piece 17 in the cube tubular box 60, N>=2, each branchial plate 17 is for being the plate body of the parallelogram with four edges of boards; Like Fig. 5 and shown in Figure 12; The first edges of boards 17a and the 3rd edges of boards 17c of branchial plate 17 are parallel to each other relatively, and the second edges of boards 17b and the 4th edges of boards 17d of branchial plate 17 are parallel to each other relatively, and each branchial plate 17 its first isometric relatively edges of boards 17a and the spacing W between the 3rd edges of boards 17c are greater than the spacing J between the first rectangle plane plate body 15b and the 3rd rectangle plane plate body 15a; Like Fig. 3, Fig. 4 and Fig. 6 and Fig. 7, shown in Figure 8, the first edges of boards 17a of each branchial plate 17 contacts with the 3rd rectangle plane plate body 15a with the cube tubular box 60 first relative rectangle plane plate body 15b respectively with the 3rd edges of boards 17c and is affixed; As shown in Figure 5; Form the first right angled triangle hole 18a between each branchial plate 17 its second edges of boards 17b and the first rectangle plane plate body 15b, the second rectangle plane plate body 13a; And form the second right angled triangle hole 18b between each branchial plate 17 its 4th edges of boards 17d and the 3rd rectangle plane plate body 15a, the 4th rectangle plane plate body 13b; Perhaps as shown in Figure 9; Form the first right-angled trapezium hole 21a between the second edges of boards 17b of each branchial plate 17 and the first rectangle plane plate body 15b, the second rectangle plane plate body 13a, the 3rd rectangle plane plate body 15a, form the second right-angled trapezium hole 21b between the 4th edges of boards 17d of each branchial plate 17 and the 3rd rectangle plane plate body 15a, the 4th rectangle plane plate body 13b, the first rectangle plane plate body 15b; Like Fig. 4, Fig. 6 to shown in Figure 8; All branchial plates 17 are vertically arranged point-blank with relative horizontal plane 19 along the length direction of cube tubular box 60; The box chamber of cube tubular box 60 is separated into cheek chamber, N-1 unit 160 by N piece branchial plate 17, and each cheek chamber, unit 160 is all between every adjacent two branchial plates 17, like Fig. 5 and shown in Figure 9; Relative and its angle same δ of second dihedral tip A2 that forms between the most advanced and sophisticated A1 of first dihedral that each branchial plate 17 its second edges of boards 17b and the 3rd edges of boards 17c form and its first edges of boards 17a and the 4th edges of boards 17d is an acute angle; The rectangle plane plate body of four settings of all branchial plate 17 opposed square tubular box 60 and horizontal plane 19 and integral inclination is like Fig. 3 to Fig. 9 and shown in 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 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 the face angle theta between all branchial plates 17 and the horizontal plane 19 is 5 °≤θ≤85 °, and is shown in figure 10; The branchial plate 17 of complanation is in plane 20; The plane at represented branchial plate 17 places overlaps with plane 20 among Figure 11, and fixing branchial plate 17 its its planes of extending on every side, planes, place, locus are plane 20, and plane 20 and the first rectangle plane plate body 15b, the second rectangle plane plate body 13a and horizontal plane 19 intersect (even non-intersect respectively; Its space angle still exists); And correspondingly form three corresponding angles, certainly, the first rectangle plane plate body 15b, the second rectangle plane plate body 13a are vertical with horizontal plane 19; Wherein, The face angle is the fixing three-dimensional angle of (intersect and form) between the first rectangle plane plate body 15b (or and the 3rd rectangular flat face body 15a), and face angle β is the fixing three-dimensional angle that (intersects and form) between the second rectangle plane plate body 13a (the 4th rectangle plane plate body 13b), the face angle theta for and horizontal plane 19 between the fixing three-dimensional angle of (intersect and form); Face included angle=﹛ α β ﹜ shown in Figure 11,5 °≤φ≤85 °, a said here included angle is the formed solid angle of defined two Plane intersects in the solid geometry; Extremely shown in Figure 9 like Fig. 3; On the first rectangle plane plate body 15b with on the 3rd rectangle plane plate body 15a N row limbers group is being set respectively; Every row limbers group is made up of M limbers 14; M>=2; Each branchial plate 17, the first rectangle plane plate body 15b of every row limbers group corresponding matching that on the first rectangle plane plate body 15b and the 3rd rectangle plane plate body 15a, are provided with respectively go up the every row limbers group that is provided with and are positioned at the orthographic projection boundary of each branchial plate 17 correspondence on the first rectangle plane plate body 15b, and the 3rd rectangle plane plate body 15a goes up the every row limbers group that is provided with and is positioned at the orthographic projection boundary of each branchial plate 17 correspondence on the 3rd rectangle plane plate body 15a; Described outer eddy flow cheek filter chamber 7b is communicated with its corresponding cells cheek chamber 160 through two row limbers groups of above-mentioned and corresponding each branchial plate 17; Cheek chamber, adjacent two unit 160 all is interconnected through above-mentioned right angled triangle hole or right-angled trapezium hole, and cheek chamber, unit 160 is also through the upper and lower end of above-mentioned right angled triangle hole or right-angled trapezium hole and the cube tubular box 60 outer eddy flow cheek filter chamber 7b of the uncovered connection of rectangle of corresponding formation respectively.

As shown in Figure 1; The muddy water that the utility model will contain sand grain flows into its chamber from cylindrical tube 6 foots along its barrel tangential; Flow into the axis rotation that the silt muddy water centers on cylindrical tube 6 longitudinal extensions that contains in 6 chambeies of cylindrical tube; Produce outer swirling water current; Make that the proportion that contains in the silt muddy water is big, viscosity is big, (particle is bigger) 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 of gravity weighs down to sand discharge funnel 9, gathered by sand discharge funnel 9, and lean on gravity to discharge downwards from the bell mouth 10 of sand discharge funnel 9; And the current 12 that are lowered turbidity receive the firmly rising of cyclonic action of the muddy water that gets into through water inlet pipe 8; And carrying out precipitate and separate through gill formula filter separator 5, gill formula filter separator 5 can be less with the proportion in the muddy water, viscosity is less, the husky precipitate and separate of the thin mud of (particle is less or less than normal) (particle) is come out, and the turbidity of muddy water is obviously reduced; The fine deposit that is precipitated is discharged from through the bell mouth 10 of gravity effect through sand discharge funnel 9 again; By the high clarity clear water separating treatment from muddy water after gill formula filter separator 5 further the processing, the interior swirling water current that is produced by interior swirling flow premium on currency tube more upwards flow to the current stabilization with relative horizontal plane inclination through swirling flow premium on currency tube and revolves in the excessive chamber 7a of revolving of the plate 6a that overflows from outer eddy flow cheek filter chamber 7b, go out from revolve excessive plate 6a 3 outlet pipe overflow topmost near current stabilization.

As shown in Figure 1; Bracing frame 4 is being fixed on top in the described outer eddy flow cheek filter chamber 7b; Gill formula filter separator 5 its cube tubular box 60 of all settings are strip; Cube tubular box 60 its tops of erectting are all affixed with bracing frame 4 bodies, make gill formula filter separator 5 fixed suspension below bracing frame 4.

As shown in Figure 1, vertical 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 of cylindrical tube 6 bottoms.

As shown in Figure 1, it is concordant with outlet pipe 2 lower side tube walls 30 that current stabilization revolves the top 3 of the plate 6a that overflows.

To shown in Figure 9, the aperture size of limbers 14 is 15-20mm like Fig. 3.Described α=45 °, β=45 °, θ=60 °.50°≤δ≤55°。Corresponding to two limbers groups of each branchial plate 17 respectively along arranged in a straight line; The first limbers group in the two limbers groups is pressed close to branchial plate 17 first edges of boards 17a and is laid; The second limbers group in the two limbers groups is pressed close to branchial plate 17 the 3rd edges of boards 17c laying, and above-mentioned its straight line that respectively is arranged in of two limbers groups is parallel with Qi Di three edges of boards 17c with the first edges of boards 17a of branchial plate 17.

As shown in Figure 1, it is concordant that the barrel 1 of interior swirling flow premium on currency tube 13 upper end nozzles and current stabilization revolve the upper face of the plate 6a that overflows, and revolve the plate 6a that overflows with current stabilization and be connected as a single entity.

Described current stabilization revolves overflow plate 6a, cube tubular box 60 and branchial plate 17 and constitutes by PVC sheet material, and current stabilization revolves overflow plate 6a, cube tubular box 60 and branchial plate 17 thickness separately and is 3mm.

Claims

1. waterpower solid-liquid two phase separator; Comprise that the solid-liquid of being made up of cylindrical tube of erectting (6) and sand discharge funnel (9) divides 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; Fixedly installing the water inlet pipe (8) of the level that is communicated with its chamber at the foot of cylindrical tube (6); Fixedly installing the outlet pipe (2) of the level that is communicated with its chamber at the topmost of cylindrical tube (6); The one end mouth of pipe (8a) of water inlet pipe (8) divides filter tank as solid-liquid water inlet feeds the jar chamber that solid-liquid divides filter tank from the tangential direction of cylindrical tube (6) the circular nozzle that cross section appeared, and the delivery port (2b) that an end mouth of pipe (2a) of outlet pipe (2) is provided with on cylindrical tube (6) barrel feeds the jar chamber that solid-liquid divides filter tank, it is characterized in that: the top in cylindrical tube (6) is being provided with and is being flat current stabilization and revolves excessive plate (6a); Current stabilization revolves excessive plate (6a), and horizontal plane is inclined fixing relatively; 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 °, and current stabilization revolves excessive plate (6a) and is provided with and erects fixing interior swirling flow premium on currency tube (13), and interior swirling flow premium on currency tube (13) is positioned at the circle centre position of cylindrical tube (6) circle that cross section appeared as interior swirling flow delivery port; Current stabilization revolves excessive plate (6a) and revolves excessive chamber (7a) and the outer eddy flow cheek filter chamber (7b) that is positioned at below it with what solid-liquid divided whole jar of chamber of filter tank to be divided into to be positioned at its top; Outer eddy flow cheek filter chamber (7b) revolves excessive chamber (7a) through swirling flow premium on currency tube (13) connection in described, and outer eddy flow cheek filter chamber (7b) is communicated with water inlet pipe (8), revolves excessive chamber (7a) and is communicated with outlet pipe (2); Cooperate to be uniformly distributed with and be fixed with gill formula filter separator (5) being positioned at outer eddy flow cheek filter chamber (7b) on the sand discharge funnel (9); 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 connected and composed by the first rectangle plane plate body (15b), the second rectangle plane plate body (13a), the 3rd rectangle plane plate body (15a) and the 4th rectangle plane plate body (13b); The adjacent two rectangle plane plate bodys of cube tubular box (60) are vertical each other; Relative two rectangle plane plate bodys are parallel to each other; So that the shape of cross section of cube tubular box (60) is the closed rectangle of perimeter line; Its whole rectangle plane plate bodys of each cube tubular box (60) are all erect and are fixedly installed; Gill formula filter separator (5) all installs along horizontal direction and constitutes the vertical separation cheek of one deck group at least; It is uncovered towards vertical direction to be the corresponding formation of the cube tubular box (60) of upright state two relative rectangle uncovered (16a), (16b); One rectangle of cube tubular box (60) is uncovered to be positioned at cube tubular box (60) and up topmost; Its another rectangle is uncovered to be positioned at cube tubular box (60) bottom and down, is equipped with fixed gap between the cube tubular box (60) of adjacent two settings, is fixedly installing the identical branchial plate of N piece (17) in the cube tubular box (60); N>=2; Each branchial plate (17) is for being the plate body of the parallelogram with four edges of boards, and first edges of boards (17a) and the 3rd edges of boards (17c) of branchial plate (17) are parallel to each other relatively, and second edges of boards (17b) and the 4th edges of boards (17d) of branchial plate (17) are parallel to each other relatively; Its isometric relatively first edges of boards (17a) of each branchial plate (17) and the spacing W between the 3rd edges of boards (17c) are greater than the spacing J between the first rectangle plane plate body (15b) and the 3rd rectangle plane plate body (15a), and 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 be affixed; Form the first right angled triangle hole (18a) between its second edges of boards (17b) of each branchial plate (17) and the first rectangle plane plate body (15b), the second rectangle plane plate body (13a); And form the second right angled triangle hole (18b) between its 4th edges of boards (17d) of each branchial plate (17) and the 3rd rectangle plane plate body (15a), the 4th rectangle plane plate body (13b); Perhaps form the first right-angled trapezium hole (21a) between second edges of boards (17b) of each branchial plate (17) and the first rectangle plane plate body (15b), the second rectangle plane plate body (13a), the 3rd rectangle plane plate body (15a), form the second right-angled trapezium hole (21b) between the 4th edges of boards (17d) of each branchial plate (17) and the 3rd rectangle plane plate body (15a), the 4th rectangle plane plate body (13b), the first rectangle plane plate body (15b); All branchial plates (17) are vertically arranged point-blank with relative horizontal plane (19) along the length direction of cube tubular box (60); The box chamber of cube tubular box (60) is separated into cheek chamber, N-1 unit (160) by N piece branchial plate (17); Each cheek chamber, unit (160) all is positioned between every adjacent two branchial plates (17); Relative and its angle same δ in second dihedral tip (A2) that forms between first dihedral that its second edges of boards (17b) of each branchial plate (17) and the 3rd edges of boards (17c) form most advanced and sophisticated (A1) and its first edges of boards (17a) and the 4th edges of boards (17d) is an acute angle; The rectangle plane plate body of four settings of the opposed square tubular box of all branchial plates (17) (60) and horizontal plane (19) and integral inclination; 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 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 the horizontal plane (19) is 5 °≤θ≤85 °; Upward with on the 3rd rectangle plane plate body (15a) N row limbers group is being set respectively at the first rectangle plane plate body (15b); Every row limbers group is made up of M limbers (14); M>=2; Every row limbers each branchial plate of group corresponding matching (17) that on the first rectangle plane plate body (15b) and the 3rd rectangle plane plate body (15a), is provided with respectively; The first rectangle plane plate body (15b) is gone up the every row limbers group that is provided with and is positioned at the corresponding orthographic projection boundary on the first rectangle plane plate body (15b) of each branchial plate (17), and the 3rd rectangle plane plate body (15a) is gone up the every row limbers group that is provided with and is positioned at the corresponding orthographic projection boundary on the 3rd rectangle plane plate body (15a) of each branchial plate (17); Described outer eddy flow cheek filter chamber (7b) is communicated with its corresponding cells cheek chamber (160) through the two row limbers groups of above-mentioned and corresponding each branchial plate (17); Adjacent cheek chamber, two unit (160) all is interconnected through above-mentioned right angled triangle hole or right-angled trapezium hole, and cheek chamber, unit (160) is also through the upper and lower end of above-mentioned right angled triangle hole or right-angled trapezium hole and cube tubular box (60) the outer eddy flow cheek filter chamber (7b) of the uncovered connection of rectangle of corresponding formation respectively.

2. waterpower solid-liquid two phase separator according to claim 1; It is characterized in that: bracing frame (4) is being fixed on the top in the described outer eddy flow cheek filter chamber (7b); Its cube tubular box (60) of the gill formula filter separator (5) of all settings is strip; Its top of the cube tubular box of erectting (60) is all affixed with bracing frame (4) body, makes the below of gill formula filter separator (5) fixed suspension in bracing frame (4).

3. waterpower solid-liquid two phase separator according to claim 2 is characterized in that: vertical 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 of cylindrical tube (6) bottom.

4. waterpower solid-liquid two phase separator according to claim 1 is characterized in that: it is concordant with outlet pipe (2) lower side tube wall (30) that current stabilization revolves the top (3) of excessive plate (6a).

5. waterpower solid-liquid two phase separator according to claim 1 is characterized in that: the aperture size of limbers (14) is 15-20mm.

6. waterpower solid-liquid two phase separator according to claim 1 is characterized in that: described α=45 °, β=45 °, θ=60 °.

7. waterpower solid-liquid two phase separator according to claim 1 is characterized in that: 50 °≤δ≤55 °.

8. waterpower solid-liquid two phase separator according to claim 1; It is characterized in that: corresponding to the two limbers groups of each branchial plate (17) respectively along arranged in a straight line; The first limbers group in the two limbers groups is pressed close to branchial plate (17) first edges of boards (17a) and is laid; The second limbers group in the two limbers groups is pressed close to branchial plate (17) the 3rd edges of boards (17c) laying, and above-mentioned its straight line that respectively is 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. waterpower solid-liquid two phase separator according to claim 1 is characterized in that: the barrel (1) of interior swirling flow premium on currency tube (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.

10. waterpower 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 constitutes by PVC sheet material, and current stabilization revolves excessive plate (6a), cube tubular box (60) and branchial plate (17) thickness separately and is 3mm.