Summary of the invention
The object of the invention is in order further to improve the deposition efficiency of existing different orientation flowing oblique tube or inclined-plate clarifying basin, and a kind of composite sedimentation tank is provided.
Composite sedimentation tank of the present invention is comprised of horizontal flow type sloping plate component, Rinsing Area, heavy mud groove, transition region, discharge pipeline, bucket, different orientation flowing oblique tube or swash plate, clear water zone and water leg, water leg is installed on top at composite sedimentation tank, the below of water leg is clear water zone, the below of clear water zone is different orientation flowing oblique tube or swash plate, and in the bottom of composite sedimentation tank, be provided with bucket, discharge pipeline is installed above bucket, above discharge pipeline, along pond cross direction, spaced a plurality of horizontal flow type sloping plate component is set, the swash plate that horizontal flow type sloping plate component is arranged by parallel interval forms, there is inclination angle in described swash plate and horizontal plane, the region division of direction under being tilted to along swash plate between horizontal flow type sloping plate component sinks mud groove, the region division Rinsing Area of the direction being tilted to along swash plate between horizontal flow type sloping plate component, above spaced horizontal flow type sloping plate component, it is transition region, in transition region, be provided with the deflector vertical with the direction of intaking, the top of transition region is different orientation flowing oblique tube or swash plate.
The course of work of composite sedimentation tank of the present invention is: current are vertically entered in horizontal flow type sloping plate component by flocculation basin end, part current along oblique upper to flowing into Rinsing Area, and upwards flow into the transition region between horizontal flow type sloping plate component and different orientation flowing oblique tube or type sloping plate component along Rinsing Area in mobile forward; Part current flow into heavy mud groove along tiltedly lower direction in mobile forward, and upwards flow into the transition region between horizontal flow type sloping plate component and different orientation flowing oblique tube or type sloping plate component by heavy mud groove.In flow process, the floc particle in water is deposited on swash plate, along the heavy mud groove that slides into swash plate one side under swash plate, and arrives in the bucket of bottom along heavy mud groove vertical sedimentation; Do not have the small flco of sedimentation to enter transition region with current.The small flco of current and not sedimentation enters different orientation flowing oblique tube via transition region or secondary separation is carried out in swash plate inside, and clear water enters the clear water zone of inclined tube or swash plate top, through water leg, catchments, and flows out sedimentation basin; The floc particle being deposited on inclined tube or swash plate glides along inclined tube or swash plate, and through transition region, horizontal flow type sloping plate component, final settlement is in the bucket of bottom.
Composite sedimentation tank of the present invention is provided with the deflector perpendicular with the direction of intaking in transition region, further to reduce current in the disturbance of transition region along continuous straight runs, prevents that floc particle is broken.In transition region, the interaction due to the downward sedimentation of flco in mobile on the current direction of below and top inclined tube or type sloping plate component, can form a body refuse superposed layer.After tiny floc particle enters into body refuse superposed layer, meeting is collided, is condensed with other particle, form compared with big flocculating body particle, and the floc particle of growing up can be deposited in horizontal flow type sloping plate component from body refuse superposed layer, finally precipitates removal.Thereby deposition efficiency and the outlet effect of sedimentation basin have further been improved.
Composite sedimentation tank of the present invention is because horizontal flow type sloping plate component has played the effect of preformed precipitate to entering into current in different orientation flowing oblique tube or swash plate, the current turbidity that makes to enter in inclined tube or swash plate reduces, thereby can effectively improve the outlet effect of sedimentation basin, reduce the wash number of inclined tube or swash plate.And, when raw water turbidity is higher, also can guarantee good outlet effect.
When flow of inlet water is 0.5t/h, surface loading is 13.5m
3/ (m
2h), when influent turbidity is 78NTU, the delivery turbidity after processing by composite sedimentation tank can arrive below 1NTU.
The specific embodiment
Below in conjunction with accompanying drawing, the specific embodiment is described further:
The specific embodiment one: the composite sedimentation tank of present embodiment is comprised of horizontal flow type sloping plate component 1, Rinsing Area 2, heavy mud groove 3, transition region 4, discharge pipeline 5, bucket 6, different orientation flowing oblique tube or swash plate 7, clear water zone 8 and water leg 9, water leg 9 is installed on top at composite sedimentation tank, the below of water leg 9 is clear water zone 8, the below of clear water zone 8 is different orientation flowing oblique tube or swash plate 7, and in the bottom of composite sedimentation tank, be provided with bucket 6, discharge pipeline 5 is installed above bucket 6, above discharge pipeline 5, along pond cross direction, spaced a plurality of horizontal flow type sloping plate component 1 is set, the swash plate 1-1 that horizontal flow type sloping plate component 1 is arranged by parallel interval forms, there is inclination angle in described swash plate 1-1 and horizontal plane, the region division of direction under being tilted to along swash plate 1-1 between horizontal flow type sloping plate component 1 sinks mud groove 3, the region division Rinsing Area 2 of the direction being tilted to along swash plate 1-1 between horizontal flow type sloping plate component, above spaced horizontal flow type sloping plate component 1, it is transition region 4, in transition region 4, be provided with the deflector vertical with the direction of intaking 10, the top of transition region 4 is different orientation flowing oblique tube or swash plate 7.
The profile in present embodiment composite sedimentation tank B-B cross section as shown in Figure 2.
Horizontal flow type sloping plate component described in present embodiment and transition region deflector are aluminium sheet, aluminium alloy plate, corrosion resistant plate, PVC plate, UPVC plate, ABS plate, PE plate, polypropylene board, glass epoxy, steel plate, plank, composited steel and plastic decking, bamboo plate or asbestos board.
The composite sedimentation tank of present embodiment is by arranging horizontal flow type sloping plate component at traditional different orientation flowing oblique tube or inclined-plate clarifying basin water distributing area, can make sedimentation basin water distribution more even, and make flowing of current more stable, the horizontal flow velocity of controlling current in it is 5mm/s~50mm/s, is difficult for the flco precipitating to stir or smash.Horizontal flow type sloping plate component has also played the effect of preformed precipitate to entering into the water of different orientation flowing oblique tube or type sloping plate component simultaneously, has alleviated the influent load of different orientation flowing oblique tube or swash plate, makes effluent quality better, and different orientation flowing oblique tube or type sloping plate component cleaning frequency are longer.
Restriction due to horizontal flow type sloping plate component, the Reynolds number of current flow when flowing to the transition region between different orientation flowing oblique tube or type sloping plate component and horizontal flow type sloping plate component by horizontal flow type sloping plate component reduces, flow turbulence reduces, flow velocity reduces, floc particle is difficult for broken, and the distribution of current is more even simultaneously.In addition, by the floc particle that slides into heavy mud groove under swash plate, be not substantially subject to the impact of horizontal applied force, therefore precipitation is more stable, better effects if.And, the setting of horizontal flow type sloping plate component make bucket and settling zone relatively independent, the flco that is deposited to bucket is difficult for being stirred.
Present embodiment arranges the deflector perpendicular with water inlet direction in transition region, further to reduce current in the disturbance of transition region along continuous straight runs, prevents that floc particle is broken.In transition region; interaction due to the downward sedimentation of flco in mobile on the current direction of below and top inclined tube or type sloping plate component; can form a body refuse superposed layer in transition region; tiny floc particle can collide with other particle after entering into body refuse superposed layer, cohesion; formation is compared with big flocculating body particle; and the floc particle of growing up can be deposited in horizontal flow type sloping plate component from body refuse superposed layer, final precipitation is removed, thereby has further improved deposition efficiency and the outlet effect of sedimentation basin.
The specific embodiment two: present embodiment is different from the specific embodiment one is that the spacing of swash plate 1-1 is 20mm~200mm.Other is identical with the specific embodiment one.
The specific embodiment three: present embodiment is different from the specific embodiment one or two is that inclination angle between swash plate 1-1 and horizontal plane is 50 °~60 °.Other is identical with the specific embodiment one or two.
The specific embodiment four: present embodiment is different from one of specific embodiment one to three is that the volume of Rinsing Area 2 is 1/5~1/10 of horizontal flow type sloping plate component 1 volume.Other is identical with one of specific embodiment one to three.
The specific embodiment five: present embodiment is different from one of specific embodiment one to four is that the volume of heavy mud groove 3 is 1/5~1/10 of horizontal flow type sloping plate component 1 volume.Other is identical with one of specific embodiment one to four.
The specific embodiment six: what present embodiment was different from one of specific embodiment one to five is to be also provided with the dividing plate parallel with the direction of intaking 11 in transition region 4.
The specific embodiment seven: present embodiment is different from one of specific embodiment one to six is that the incline direction of the swash plate 1-1 in adjacent level stream type sloping plate component 1 is contrary.Other is identical with one of specific embodiment one to six.
The profile in present embodiment composite sedimentation tank A-A cross section as shown in Figure 3.
The specific embodiment eight: present embodiment is different from one of specific embodiment one to seven is that the incline direction of every group of swash plate 1-1 in horizontal flow type sloping plate component 1 is all identical.Other is identical with one of specific embodiment one to seven.
As shown in Figure 4, the region of now adjacent level being flowed between type sloping plate component 1 is divided into two parts to the profile in present embodiment composite sedimentation tank A-A cross section, and a side arranges Rinsing Area 2, and opposite side arranges heavy mud groove 3.
The specific embodiment nine: what present embodiment was different from one of specific embodiment one to eight is that horizontal flow type sloping plate component is only arranged in along the space of the pond length direction 1/5~1/3 of composite sedimentation tank.Other is identical with one of specific embodiment one to eight.
The profile in present embodiment composite sedimentation tank B-B cross section as shown in Figure 5.
The specific embodiment ten: what present embodiment was different from one of specific embodiment one to nine is sludge discharge way employing hydrostatic pressing spoil disposal, sludge pump spoil disposal, gas pump spoil disposal or the mud scraper spoil disposal of composite sedimentation tank.Other is identical with one of specific embodiment one to nine.
Embodiment mono-: the composite sedimentation tank of the present embodiment is comprised of horizontal flow type sloping plate component 1, Rinsing Area 2, heavy mud groove 3, transition region 4, discharge pipeline 5, bucket 6, different orientation flowing oblique tube or swash plate 7, clear water zone 8 and water leg 9, water leg 9 is installed on top at composite sedimentation tank, the below of water leg 9 is clear water zone 8, the below of clear water zone 8 is different orientation flowing oblique tube or swash plate 7, and in the bottom of composite sedimentation tank, be provided with bucket 6, discharge pipeline 5 is installed above bucket 6, above discharge pipeline 5, along pond cross direction, spaced a plurality of horizontal flow type sloping plate component 1 is set, the swash plate 1-1 that horizontal flow type sloping plate component 1 is arranged by parallel interval forms, there is inclination angle in described swash plate 1-1 and horizontal plane, the region division of direction under being tilted to along swash plate 1-1 between horizontal flow type sloping plate component 1 sinks mud groove 3, the region division Rinsing Area 2 of the direction being tilted to along swash plate 1-1 between horizontal flow type sloping plate component, above spaced horizontal flow type sloping plate component 1, it is transition region 4, in transition region 4, be provided with the deflector vertical with the direction of intaking 10, the top of transition region 4 is different orientation flowing oblique tube or swash plate 7.
The incline direction of swash plate 1-1 in the present embodiment adjacent level stream type sloping plate component 1 is contrary, the region division of direction under being tilted to along swash plate between horizontal flow type sloping plate component sinks mud groove, the region division Rinsing Area of the direction being tilted to along swash plate between horizontal flow type sloping plate component.
The composite sedimentation tank of the present embodiment, long 7.7 meters, wide 4.8 meters, high 5 meters.Horizontal flow type sloping plate component arranges 7 groups along pond length direction, along pond cross direction, arranges 5 groups, amounts to 35 groups, and in the horizontal flow type sloping plate component wherein distributing along pond length direction, the incline direction of swash plate is all identical.Every group of horizontal flow type sloping plate component grown 1.1 meters, wide 0.93 meter.Swash plate vertical interval 80mm, 60 °, inclination angle.Dark 0.95 meter of bucket, discharge pipeline caliber DN200.7.7 meters of the transition heads of district, wide 4.8 meters, high 0.45 meter, use with composite sedimentation tank water inlet direction and parallel with vertical deflector transition region is divided into uniform 35.7.7 meters of the different orientation flowing oblique tube heads of district, wide 4.8 meters, high 0.88 meter, standard cellular inclined tube is filled in inclined tube district.7.7 meters of the clear water heads of district, wide 4.8 meters, high 1.62 meters.Top, clear water zone is parallel to 5 water legs of pond cross direction spaced set.
When flow of inlet water is 0.5t/h, surface loading is 13.5m
3/ (m
2h), when influent turbidity is 78NTU, the delivery turbidity after processing by the composite sedimentation tank of the present embodiment can arrive below 1NTU.