CN2508832Y - High-speed separator - Google Patents
High-speed separator Download PDFInfo
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- CN2508832Y CN2508832Y CN 01225079 CN01225079U CN2508832Y CN 2508832 Y CN2508832 Y CN 2508832Y CN 01225079 CN01225079 CN 01225079 CN 01225079 U CN01225079 U CN 01225079U CN 2508832 Y CN2508832 Y CN 2508832Y
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- water
- blender
- flash
- worm gear
- vertical shaft
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Abstract
The utility model is a Lamera high speed separator. The water quality after treatment can realize that the turbidity can reach 0.7 to 0.5 Ntu, and thereby is a level that only a few water treatment plants in a few European countries can achieve. The utility model has not only good water treatment quality, but also is a kind of pond with highest water treatment efficiency in the world, the water treatment volume can be as high as Q being equal to 30 to 50 m3/m2.hr, compared with domestic advectional pond, the occupied land can be saved over 95 percent, the mechanical equipment can only occupy 1/8 to 1/10. The mixing time is T value less than or equal to a value/second, and thereby increases 240 times to 500 times than the normal design. The central line speed of the serosity mixing: V is less than or equal to 1.5 to 2.0 (first grade flocculation line speed value).
Description
The utility model is that a kind of blue U.S.A draws high fast separator.
Lan Meila (Lamella sepaiater) is the same flow precipitation pond.Present contaminated being on the rise of source water is regarded as a carrier index of water treatment procedure to the turbidity index of processed back water, and pollutant in water especially is harmful to because the decline of turbidity makes, poisonous organic matter and carcinogen all decreases.
The purpose of this utility model is exactly for solving existing problem in the above-mentioned hydrotreater, providing blue U.S.A of a kind of high-speed separation extraction clear water to draw high fast separator.
The utility model is that Lan Mei draws high fast separator.Flash blender 1 is column, its section is rounded or square, the top of flash blender is provided with electric gear shift(ing) 2, the output shaft of electric gear shift(ing) is fixedlyed connected with an end of vertical shaft 13, some paddles 3 are set on the vertical shaft 13, the other end of vertical shaft 13 is connected with the top of turbine-type mixer 4, and is axis.The volume of flash blender 1 stays the time T value and determines in flash blender intermediary with water.The revolution of vertical shaft is to determine according to the requirement of paddle 3 and worm gear blender 4.The quantity of paddle 3 is to cross water according to the shape of flash mixer and container to hold back area and determine, as shown in Figure 1 and Figure 2.
Can some flow deflectors 5 vertically equidistantly vertically be set along inwall on the lower inner wall of flash mixer 1, prevent that current are synchronous.Flow deflector 5 be set vertically on the inwall of flash mixer 1 be that current to occur when preventing to mix synchronous, cause mix inhomogeneous, as shown in Figure 1 and Figure 2.
The bottom of flash blender 1 is provided with worm gear blender 4, the worm gear shell 6 of flash blender 1 is column, and match with flash mixer 1, the worm gear device top board of worm gear blender 4 and vertical shaft 13 axises, fixedly install some turbo blades 8 in worm gear device top board 15 bottoms, the central part of turbine-type mixer 4 is provided with inlet opening 7, with worm gear blender 4 lower vertical opposite positions drug tube 9 is set.Unprocessed water is entered by flash mixer 1 bottom, enters the inlet opening 7 of worm gear blender 4 together with the medicament of drug tube 9, through turbo blade 8 unprocessed water and medicament is forced to mix, and enters flash blender 1 by the outlet of worm gear blender 4.The unprocessed water of confection is fully mixed the back by paddle 3 and flow deflector 5 and enters mechanical flocculator 14 by the outlet on flash container 1 top in flash container 1.Worm gear blender 4 is core positions of flash blender 1, be column, some turbo blades 8 are set in the worm gear blender, the quantity of turbo blade is directly proportional with the water yield, the shape of turbo blade and big I are definite according to the shape of worm gear blender, as shown in Figure 1 and Figure 2.
Throw in the drug tube 9 of chemical agent and can determine that for example: coagulant has molysite and aluminium salt according to different medicaments and medicament kind; Flocculation aid has macromolecule medicaments such as gelatine, sodium metasilicate, sodium alginate; Conditioning agent has lime, hydrofluoric acid and mud to reflux.
V---the effective total measurement (volume) (m of mechanical flocculator
3)
Q---calculate the water yield (m
3/ h)
T---minute
Determine according to the needs of T value what flocculating chamber the flocculating chamber of mechanical flocculator 14 is divided into.The volume of suspension flocculator is definite according to the time T value that water flocculates in the suspension flocculator, as shown in Figure 1 and Figure 2.
One side of suspension flocculator 11 is a separation container 22, the middle part of separation container is provided with separating plate 18, and separating plate is the inclination angle, fixedly installs several water legs 20 below the separating plate 18 and collects clear water, the bottom of separating plate 18 is provided with slip plate 17, and the slip plate is the inclination angle.Separating plate 18 is the less swash plates of angle, and the flco that water forms on swash plate proceeds to tie suede, separation, and the water leg that swash plate is provided with is below collected clear water.Slip plate 17 is the bigger swash plates of angle, the little cotton-shaped dirt that is separated in the suspension flocculator above the slip plate 17 is slipped in the mud enriched chamber 16 concentrate, as Fig. 1, Fig. 2, shown in Figure 3.
The bottom of separation container 22 is mud enriched chamber 16, the dirt of separating is got rid of, as shown in Figure 1 and Figure 2.
The top of separation container 22 is provided with some collector pipes 19, water leg 20 is stretched in the end of collector pipe, in water leg 20, be provided with coattail board 24, make trough inner water continue the flco process coattail board 24 separated downslides of knot suede, several water legs 20 are set in separation container 22 compile the clear water that collector pipe is collected, the upper face of collector pipe arranges that rib of slab 25 constitutes grid 26, and the clear water that collector pipe 19 is collected is pooled in the effluent trough 21, at the end of effluent trough 21 the total groove 23 of water outlet is set.Condition according to waterpower is arranged collector pipe 19 on the back side of every separating plate, and arranges rib of slab 25 on collector pipe, and separating plate is divided into grid, makes water be in very good worker's shape condition, and the thin-slab structure to separating plate has also increased intensity simultaneously.The clear water that water leg 20 is collected collector pipe 19 is pooled in the effluent trough 21, does not produce the water burst phenomenon in order to guarantee effluent trough, at the end of effluent trough 21 the total groove 23 of water outlet is set, as Fig. 1, Fig. 2, shown in Figure 3.
The utility model is that Lan Mei draws high fast separator.The turbidity that water quality after the processing can realize is 0.7～0.5ntu, turbidity is a topmost index of this stage in the water treatment process, also can be described as the unique water index of this rank end, " the outdoor design specification of catchmenting " GBJ 13-86 is defined as: turbidity is no more than 10～15 degree (being referred to as Ntu in the world).Be decided to be and be no more than 3～5Ntu and finished product is turbidity index " drinking water sanitary standard " the GB5749-85 standard of the final running water of water treatment process, and separator delivery turbidity of the present utility model is 0.7～0.5Ntu, reaches the level of having only the extremely indivedual water factories of European a few countries in the world.The utility model is good processed water quality not only, also be one of the most effective pond type of water of handling in the world at present, and it handles water yield can be up to Q=30～50m
3/ m
2.hr, the saving of comparing with domestic horizontal flow basin is taken up an area of more than 95%, and plant equipment only accounts for 1/8～1/10.Incorporation time: T value=0.2～0.5 second, compare with domestic normal design and to have improved 240～500 times.The center line velocity that paddle is mixed: V=1.0～2.0 (one-level flocculation linear velocity value).Adopt the mechanical flocculation mode that adds suspension, the holdup time of mechanical system water: T value ≌ 12～15 minutes; The holdup time of suspended pattern water: T value ≌ 3～5 minutes.The strict control of separating part hydraulics carries out the structure preparation, and wherein: thunder is guaranteed to work under laminar condition as if numerical value (Re)≤400; Fo Luode numerical value (Fr) 〉=10
-4Make hydraulics be in stable state fully: water outlet forces head difference (H)≤450mm ≠ 0 to accomplish uniform water distribution between plate.
The utility model can be applicable to adopt chemical coagulation, clarification to divide dried up separator, as the processing of Drinking Water; The tertiary treatment of city domestic sewage and middle water treatment; The recycling of paper waste and plain boiled water; Metallurgical, electroplating wastewater and adopt the processing of industrial wastewaters such as chemically treated pharmacy, chemical petroleum and neutralization etc.
The blue U.S.A of Fig. 1 draws high the cross-sectional view of fast separator
The blue U.S.A of Fig. 2 draws high the floor map of fast separator
The blue U.S.A of Fig. 3 draws high the structural representation of fast separator water leg
The blue U.S.A of Fig. 4 draws high the structural representation of fast separator
The blue U.S.A of Fig. 5 draws high the structural representation of fast separator
1 flash blender, 2 electric gear shift(ing)s, 3 paddles, 4 turbine-type mixers, 5 flow deflectors, 6 worm gear shells, 7 inlet openings, 8 turbo blades, 9 drug tubes, 10 dividing plates, 11 suspension flocculators, 12 flocculating chambers, 13 vertical shafts, 14 mechanical flocculators, 15 worm gear device top boards, 16 mud enriched chambers, 17 slip plates, 18 separating plates, 19 collector pipes, 20 water legs, 21 effluent troughs, 22 separation containers, the total groove of 23 water outlets, 24 coattail boards, 25 ribs of slab, 26 sub-boxes
Below describe in detail with embodiment.
Embodiment 1
Flash blender 1 is column, and its section is rounded, and the top of flash blender is provided with electric gear shift(ing) 2, the output shaft of electric gear shift(ing) is fixedlyed connected with an end of vertical shaft 13,4 paddles 3 are set on the vertical shaft 13, and the other end of vertical shaft 13 is connected with the top of turbine-type mixer 4, and is axis.About 1 minute of water holdup time in the flash blender.The revolution of vertical shaft is to determine according to the requirement of paddle 3 and worm gear blender 4, as shown in Figure 1 and Figure 2.
The lower inner wall upper edge inwall of flash mixer 1 vertically equidistantly vertically is provided with 4 flow deflectors 5, prevents that current are synchronous, causes mixing inhomogeneous, as shown in Figure 1 and Figure 2.
The bottom of flash blender 1 is provided with worm gear blender 4, the worm gear shell 6 of flash blender 1 is column, and match with flash mixer 1, the worm gear device top board of worm gear blender 4 and vertical shaft 13 axises, fixedly install 6 turbo blades 8 in worm gear device top board 15 bottoms, the central part of turbine-type mixer 4 is provided with inlet opening 7, with worm gear blender 4 lower vertical opposite positions drug tube 9 is set.Unprocessed water is entered by flash mixer 1 bottom, enters the inlet opening 7 of worm gear blender 4 together with the medicament of drug tube 9, through turbo blade 8 unprocessed water and medicament is forced to mix, and enters flash blender 1 by the outlet of worm gear blender 4.The unprocessed water of confection is fully mixed the back by paddle 3 and flow deflector 5 and enters mechanical flocculator 14 by the outlet on flash container 1 top in flash container 1.Worm gear blender 4 is core positions of flash blender 1, is column, and 6 turbo blades 8 are set in the worm gear blender, throws in chemical agent to be: molysite, sodium metasilicate, lime and mud reflux, as shown in Figure 1 and Figure 2.
One side of suspension flocculator 11 is a separation container 22, the middle part of separation container is provided with separating plate 18, and separating plate is the inclination angle, fixedly installs several water legs 20 below the separating plate 18 and collects clear water, the bottom of separating plate 18 is provided with slip plate 17, and the slip plate is the inclination angle.Separating plate 18 is the less swash plates of angle, and the flco that water forms on swash plate proceeds to tie suede, separation, and the water leg that swash plate is provided with is below collected clear water.Slip plate 17 is the bigger swash plates of angle, and the little cotton-shaped dirt that slip plate 17 is separated above slips into mud enriched chamber 16 interior concentrating, as Fig. 1, Fig. 2, shown in Figure 3.
The bottom of separation container 22 is mud enriched chamber 16, the dirt of separating is got rid of, as shown in Figure 1 and Figure 2.
4 collector pipes 19 are set on the back side of every separating plate in the top of separation container 22 18, the end of collector pipe is stretched in the water leg 20,5 water legs 20 are set in separation container 22 compile the clear water that collector pipe is collected, the upper face of collector pipe arranges that rib of slab 25 constitutes sub-box 26, the clear water that collector pipe 19 is collected is pooled in the effluent trough 21, at the end of effluent trough 21 the total groove 23 of water outlet is set.Condition according to waterpower is arranged collector pipe 19 on the back side of every separating plate, and arranges rib of slab 25 on collector pipe, and separating plate is divided into grid, makes water be in very good worker's shape condition, and the thin-slab structure to separating plate has also increased intensity simultaneously.The clear water that water leg 20 is collected collector pipe 19 is pooled in the effluent trough 21, does not produce the water burst phenomenon in order to guarantee effluent trough, at the end of effluent trough 21 the total groove 23 of water outlet is set, as shown in Figure 1 and Figure 2.
Flash blender 1 is column, its section is square, the top of flash blender is provided with electric gear shift(ing) 2, the output shaft of electric gear shift(ing) is fixedlyed connected with an end of vertical shaft 13,4 paddles 3 are set on the vertical shaft 13, the other end of vertical shaft 13 is connected with the worm gear device top board 15 of turbine-type mixer 4, and is axis, as Fig. 1, Fig. 2, shown in Figure 4.
The bottom of flash blender 1 is provided with worm gear blender 4, the worm gear shell 6 of flash blender 1 is column, and match with flash mixer 1, the worm gear device top board of worm gear blender 4 and vertical shaft 13 axises, fixedly install 6 turbo blades 8 in worm gear device top board 15 bottoms, the central part of turbine-type mixer 4 is provided with inlet opening 7, with worm gear blender 4 lower vertical opposite positions drug tube 9 is set.Unprocessed water is entered by flash mixer 1 bottom, enters the inlet opening 7 of worm gear blender 4 together with the medicament of drug tube 9, through turbo blade 8 unprocessed water and medicament is forced to mix, and enters flash blender 1 by the outlet of worm gear blender 4.The unprocessed water of confection is fully mixed the back by paddle 3 and flow deflector 5 and enters mechanical flocculator 14 by the outlet on flash container 1 top in flash container 1.Worm gear blender 4 is core positions of flash blender 1, is column, and 6 turbo blades 8 are set in the worm gear blender, throws in chemical agent to be: aluminium salt, sodium metasilicate, lime, hydrofluoric acid and mud reflux, as shown in Figure 1 and Figure 2.
Side by side machinery flocculator 14 in the two poles of the earth is by being separated into six grades of flocculating chambers 12 on the parallel staggered relatively inwalls that are fixedly installed on mechanical flocculator 14 of dividing plate 10, and the import of each grade flocculating chamber 12 and export relative staggered.Machinery flocculator 14 upper ends are provided with electric gear shift(ing) 2, and the output shaft of electric gear shift(ing) 2 is connected with vertical shaft 13, and vertical shaft runs through dividing plate 10, flocculating chambers at different levels 12 shared axises.Fixedly install 4 paddles 3 on the vertical shaft 13 of each grade flocculating chamber 12, the paddle bar is shortened step by step by primary chamber to six a grade chamber, confection and unprocessed water enter elementary flocculating chamber 12 through after paddle 3 high-speed stirred of vertical shaft 13 by the inlet of a side of flocculating chamber 14, enter the secondary flocculating chamber from the opposite side outlet, inlet by a side of elementary flocculating chamber 14 enters secondary flocculating chamber 12 through after paddle 3 high-speed stirred of vertical shaft 13, enter three grades of flocculating chambers from the opposite side outlet, slowing down step by step successively mixes the back and enters suspension flocculator 11 by the outlet of flocculating chamber 14 and carry out suspension reaction, as Fig. 1, Fig. 2, shown in Figure 4.
One side of suspension flocculator 11 is a separation container 22, the middle part of separation container is provided with separating plate 18, and separating plate is the inclination angle, fixedly installs 4 water legs 20 on the back side of separating plate 18 and collects clear water, the bottom of separating plate 18 is provided with slip plate 17, and the slip plate is the inclination angle.Separating plate 18 is the less swash plates of angle, and the flco that water forms on swash plate proceeds to tie suede, separation, and the water leg that swash plate is provided with is below collected clear water.Slip plate 17 is the bigger swash plates of angle, and the little cotton-shaped dirt that slip plate 17 is separated above slips into mud enriched chamber 16 interior concentrating, as Fig. 1, Fig. 2, shown in Figure 4.
The bottom of separation container 22 is mud enriched chamber 16, the dirt of separating is got rid of, as shown in Figure 1 and Figure 2.
3 collector pipes 19 are set on the back side of every separating plate in the top of separation container 22 18, water leg 20 is stretched in the end of collector pipe, 4 effluent troughs 20 are set in separation container 22 compile the clear water that collector pipe is collected, the upper face of collector pipe arranges that rib of slab 25 constitutes grid, the clear water that collector pipe 19 is collected is pooled in the effluent trough 21, at the end of effluent trough 21 the total groove 23 of water outlet is set.Condition according to waterpower is arranged collector pipe 19 on the back side of every separating plate, and arranges rib of slab 25 on collector pipe, and separating plate is divided into grid, makes water be in very good worker's shape condition, and the thin-slab structure to separating plate has also increased intensity simultaneously.The clear water that water leg 20 is collected collector pipe 19 is pooled in the effluent trough 21, does not produce the water burst phenomenon in order to guarantee effluent trough, at the end of effluent trough 21 the total groove 23 of water outlet is set, as Fig. 1, Fig. 2, Fig. 3, Fig. 4, shown in Figure 5.
Claims (1)
1, a kind of blue U.S.A draws high fast separator, feature of the present utility model is that flash blender 1 is column, its section is rounded or square, the top of flash blender is provided with electric gear shift(ing) 2, the output shaft of electric gear shift(ing) is fixedlyed connected with an end of vertical shaft 13, several paddles 3 are set on the vertical shaft 13, and the other end of vertical shaft 13 is connected with the top of turbine-type mixer 4, and is axis; Can several flow deflectors 5 vertically equidistantly vertically be set along inwall on the lower inner wall of flash blender 1, prevent that current are synchronous; The bottom of flash blender 1 is provided with worm gear blender 4, the worm gear shell 6 of flash blender 1 is column, and match with flash blender 1, the worm gear device top board of worm gear blender 4 and vertical shaft 13 axises, fixedly install some turbo blades 8 in worm gear device top board 15 bottoms, the central part of turbine-type mixer 4 is provided with inlet opening 7, with worm gear blender 4 lower vertical opposite positions drug tube 9 is set; Unprocessed water is entered by flash blender 1 bottom, enters the inlet opening 7 of worm gear blender 4 together with the medicament of drug tube 9, through turbo blade 8 unprocessed water and medicament is forced to mix, and enters flash blender 1 by the outlet of worm gear blender 4; Confection and unprocessed water are fully mixed the back by paddle 3 and flow deflector 5 and enter mechanical flocculator 14 by the outlet on flash container 1 top in flash container 1; Machinery flocculator 14 is by being separated into some grades of flocculating chambers 12 on the parallel staggered relatively inwalls that are fixedly installed on mechanical flocculator 14 of some dividing plate 10, and the import of each grade flocculating chamber 12 and export relative staggered; Machinery flocculator 14 upper ends are provided with electric gear shift(ing) 2, and the output shaft of electric gear shift(ing) 2 is connected with vertical shaft 13, and vertical shaft runs through dividing plate 10, some grades of flocculating chamber's 12 shared axises; Fixedly install several paddles 3 on the vertical shaft 13 of each grade flocculating chamber 12, the paddle bar is shortened to the last grade flocculating chamber step by step by elementary flocculating chamber, confection and unprocessed water enter elementary flocculating chamber 12 through after paddle 3 high-speed stirred of vertical shaft 13 by the inlet of a side of flocculating chamber 14, enter the next stage flocculating chamber from opposite side outlet, slowing down step by step mixes the back and enters suspension flocculator 11 by the outlet of flocculating chamber 14 and carry out suspension reaction; One side of suspension flocculator 11 is a separation container 22, the middle part of separation container is provided with separating plate 18, and separating plate is the inclination angle, fixedly installs several water legs 20 below the separating plate 18 and collects clear water, the bottom of separating plate 18 is provided with slip plate 17, and the slip plate is the inclination angle; The bottom of separation container is mud enriched chamber 16, and the dirt of separating is got rid of; The top of separation container 22 is provided with some collector pipes 19, water leg 20 is stretched in the end of collector pipe, in water leg 20, be provided with coattail board 24, make trough inner water continue the flco process coattail board 24 separated downslides of knot suede, several water legs 20 are set in separation container 22 compile the clear water that collector pipe is collected, the upper face of collector pipe arranges that rib of slab 25 constitutes sub-boxes 26, and the clear water that collector pipe 19 compiles focuses in the effluent trough 21, at the end of effluent trough 21 the total groove 23 of water outlet is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01225079 CN2508832Y (en) | 2001-06-01 | 2001-06-01 | High-speed separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01225079 CN2508832Y (en) | 2001-06-01 | 2001-06-01 | High-speed separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2508832Y true CN2508832Y (en) | 2002-09-04 |
Family
ID=33641228
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01225079 Expired - Fee Related CN2508832Y (en) | 2001-06-01 | 2001-06-01 | High-speed separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2508832Y (en) |
-
2001
- 2001-06-01 CN CN 01225079 patent/CN2508832Y/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |