CN201111438Y

CN201111438Y - Transverse flow filtering tank

Info

Publication number: CN201111438Y
Application number: CNU2007201150073U
Authority: CN
Inventors: 俞建德; 王建峰
Original assignee: DEAN NEW-TECHNOLOGY DEVELOPMENT Co Ltd ZHEJIANG
Current assignee: DEAN NEW-TECHNOLOGY DEVELOPMENT Co Ltd ZHEJIANG
Priority date: 2007-09-21
Filing date: 2007-09-21
Publication date: 2008-09-10
Anticipated expiration: 2017-09-21

Abstract

The utility model relates to a filter tank of transverse flow filtration, comprising a tank body, a water inlet pipe, a water outlet pipe, a water inlet trench, a water outlet trench and a filter material layer; the water inlet trench and the water outlet trench are crossly and intermittently erected on the bottom of the tank body; the filter material layer is arranged between the water inlet trench and the water outlet trench; furthermore, a backwashing device is arranged inside the filter material layer; the backwashing device comprises an air inlet pipe, an air lifting pipe, a sand separator and a sand distributor; the sand separator comprises a ring-shaped backwashing chamber and a central sewage collecting chamber; the sand separator is also externally connected with a sewage discharging pipe; the inlet of the sewage discharging pipe passes through the backwashing chamber to be communicated with the central sewage collecting chamber. Compared with the prior art, the filter tank creates a completely novel filter tank which transversely filtrates on a same horizontal plane; as the transverse filtration mode is adopted, under the condition of the same tank body dimension, the filtration area is far greater than that by adopting the longitudinal filtration mode; the filtration area is increased by the transverse filtration of the water flow, thus greatly improving the water output of the filter tank.

Description

A kind of filtering ponds of transverse stream filtering

Technical field

The utility model relates to the technical field of the filtering ponds that are used for water treatment, relates in particular to a kind of filtering ponds of transverse stream filtering.

Background technology

In the at present conventional filtering ponds, its water (flow) direction of water that needs to filter generally be longitudinally from the overhead stream in filter tank to the bottom in filter tank, i.e. longitudinal stream, present most widely used filtering ponds-this mode is adopted in the V-type filter tank exactly.This filtering ponds have the air-water backwashing function, and water purification water quality after filtering is better, and the filtration life cycle is also longer, but its actual rate of filtration is lower, generally about 8～12m/h.Usually, after filtering ponds have been laid, the filter area of filtering ponds is just fixing, according to formula: Q (flow)=S (filter area) * V (rate of filtration), under the situation that filter area is fixed,, must improve the rate of filtration as improving the aquifer yield that water purification, therefore, improving the filtering ponds aquifer yield by the raising rate of filtration is the most general a kind of means that adopt at present.But when practical application, the rate of filtration also is limited, can not unconfined raising according to perfect condition, as improving speed again, the water quality of water purification of coming out after the filtration will not reach standard, perhaps, the filtrate in the filtering ponds is because of intensive work, and make filtering ponds become filter cycle very short, be uneconomic, also make the working condition of filtering ponds become disorderly easily, even out of control, be unfavorable for the conventional maintenance of filtering ponds.

In fact, can draw,, also can realize improving the purpose of aquifer yield by increasing filter area S from above-mentioned formula: Q (flow)=S (filter area) * V (rate of filtration).

Summary of the invention

Technical problem to be solved in the utility model is to provide a kind of filtering ponds that adopt transverse stream filtering at above-mentioned prior art present situation, and it laterally filters by current and can increase filter area, thereby increases substantially the aquifer yield of filtering ponds.

The utility model solves the problems of the technologies described above the technical scheme that is adopted: the filtering ponds of this transverse stream filtering, and include Chi Tihe and be distributed in the interior inlet channel of pond body, go out water channel and filter material layer, it is characterized in that:

Described inlet channel and go out water channel and be separated by first filter plate that is positioned at its both sides, second filter plate respectively, described inlet channel and go out the water channel compartment of terrain that crosses one another and be erected on the pond body bottom, described filter material layer is then at inlet channel and go out between the water channel, and, an external side is provided with the water inlet pipe that the port of export is connected with inlet channel in described pond, and the external opposite side in pond then is provided with arrival end and goes out the outlet pipe that water channel is connected;

Simultaneously, among described filter material layer, also be provided with back purge system, it comprises air inlet pipe, air-lift unit pipe, sand separator and sand distributor, wherein, be inserted among the filter material layer to the relative pond of described air-lift unit pipe body bottom vertical, the lower part of this air-lift unit pipe is connected with described air inlet pipe;

Two-layer annular sidewall surrounded inside and outside described sand separator included, the top has venthole, the ring-type backwash chamber of bottom opening and internal layer annular sidewall surround, bottom lock, dirty chamber is gathered by open-topped central authorities, the top of described air-lift unit pipe is connected with the top in the ring-type backwash chamber of this sand separator, and this sand separator also is circumscribed with a blow-off pipe, this blow-off pipe inlet passes described inside and outside two-layer annular sidewall and is connected with described central authorities poly-dirty chambeies, and, have the intercommunicating pore that is higher than described blow-off pipe porch on the described internal layer annular sidewall;

And described sand distributor is the conduction pipe that two ends connect, and the one end is connected with the opening of bottom, backwash chamber in the sand separator, and the other end is then towards described filter material layer.

Wherein, the filtrate in the described filter material layer can adopt existing various filter materials, comparatively common genus quartz sand.

For make in sand separator backwash filtrate later can be comparatively slowly, falling back among the filter material layer progressively, make filtrate, dirt and current can separate fully, precipitate, rather than directly fall among the filter material layer quickly, described sand distributor sand separator relatively is provided with obliquely, like this, filtrate after the flushing can be step by step along past whereabouts, the bottom side that this sand distributor is a conduction pipe, reduced the falling speed of filtrate in sand separator, filtrate is after fully precipitating, become cleaner, fall back filter material layer from the outlet of this sand distributor at last among.

Be the filter plate of using the water channel both sides water purification after can more uniform collection filtering, go out the water channel both sides and can be provided with the slight drag water dispensing apparatus described, this slight drag water dispensing apparatus can be existing various technical scheme, as the patent No. is the disclosed technical scheme of Chinese utility model patent " a kind of slight drag water dispensing apparatus that is used for fibrous filtering pool " of ZL200520102021.0 (notification number is CN2785681Y), but for making structure simpler, be easy to actual enforcement, described second filter plate that goes out the water channel both sides can be dividing plate, and is uniformly distributed with filter on dividing plate.

When passing through the filter plate lateral flow of inlet channel both sides for the former water of avoiding need to filter, flow to out water channel directly, produce short flow phenomenon, can be uniformly distributed with permeable hole on first filter plate of described inlet channel both sides, and can also tilt down to be provided with baffle plate on first filter plate, like this, former water must be earlier to dirty because of stopping of baffle plate, horizontal flow is to going out water channel again, and this has just strengthened former water and toss about in bed the distance that flows through in filter material layer, thereby improves its purification effects.

For making the filtrate in the filter material layer all can participate in backwash, particularly can carry out backwash as much as possible to the filtrate that is positioned at filter material layer top, described sand distributor is just in time to be positioned on the filter material layer for good, filtrate after the backwash can straightwayly be fallen back among the filter material layer, and the water level in the body of pond will be higher than the water level in the poly-dirty hole of central authorities in the sand separator, like this, water level in the body of pond need be positioned at the top of sand separator all the time, promptly upwards is followed successively by the water level in filter material layer, sand distributor, sand separator and the pond body from pond body bottom; Like this, if inlet channel, the height that goes out water channel is higher than the interior water level of pond body, inlet channel so, go out between the top of water channel and the filter material layer top and just have a segment distance, the inlet channel of this part, go out water channel and can't not filter work normally owing to have filter material layer between the two, therefore, this part has just been wasted, for improving inlet channel, go out the utilization rate of water channel, reduce the construction cost of filtering ponds, described inlet channel can not be too high with the top that goes out water channel, is good with the water level that is lower than in the body of pond, generally is higher than the top of filter material layer a little, and this moment, water in the body of pond will inevitably climingly be crossed inlet channel, go out the top of water channel, cause the confusion of sewage and hydrostatic, described inlet channel, the top that goes out water channel just need be provided with cover plate, with inlet channel, seal at the top that goes out water channel, forbids that current arbitrarily circulate.

Because the water level in the body of pond need reach certain height, and apparently higher than the top that goes out water channel, the flow that goes out water channel so just needs control, otherwise it is less to be buffered in water outlet channel water amount, makes the water level in the body of pond keep higher height with regard to being difficult to, therefore, can be provided with valve by described outlet pipe, this valve can be adjustable pneumatic or electrically operated valve, also can be the valve of manual or switching mode, thereby realizes the constant of the interior water level of pond body.

For ease of grasping the height of water level in the body of pond at any time, can also be provided with liquid level gauge on the body inwall of described pond.

Compared with prior art, the utility model broken through existing filtering ponds distribute successively from top to bottom former water layer, filter material layer, catchment layer and adopt the pattern of vertically filtering, a kind of brand-new filtering ponds that lateral flow is filtered on same horizontal plane have been started, owing to adopted horizontal filtered model, under the identical situation of pond body size, its filter area is bigger than the pattern that adopts vertical filtration far away, laterally filters by current to have increased filter area, thereby has increased substantially the aquifer yield of filtering ponds; Simultaneously, the back purge system that in filter material layer, is provided with special structure, as long as just can make backwash gas, current each self-forming flow cycle in back purge system to air inlet pipe input backwash gas, thereby filtrate is washed, and have backwash effect preferably, saved equipment such as needed backwash pump of usual backwash or elevated tank; Filtering ponds with a long 10m, wide 4m, high 4.5m are example, as adopt existing conventional sand filter to filter, and filtering velocity is 10m/h, and then water flow Q is 400m ³/ h is if adopt the filtering ponds of transverse stream filtering of the present utility model for the same pond type of scale, with filtering layer width 0.75m, inlet channel with to go out water channel respectively be that 0.5m, cross-sectional area are 16m ²Meter, water flow Q can reach 1280m ³/ h is 3.2 times of conventional filter tank.

Description of drawings

Fig. 1 is the structural representation of the utility model embodiment;

Fig. 2 be among Fig. 1 A-A to cutaway view;

Fig. 3 is the enlarged drawing of I portion among Fig. 2;

Fig. 4 is the enlarged drawing of II portion among Fig. 2;

Fig. 5 is the cutaway view of back purge system among the utility model embodiment;

Fig. 6 is the structural representation of back purge system among the utility model embodiment.

The specific embodiment

Embodiment describes in further detail the utility model below in conjunction with accompanying drawing.

As Fig. 1～shown in Figure 6, the filtering ponds of this transverse stream filtering include pond body 1 and are distributed in inlet channel 2 in the pond body 1, go out water channel 3 and filter material layer 4;

In the present embodiment, the filtrate in the filter material layer 4 adopts quartz sand, and quartz sand particle size is 0.7mm～2mm, and for guaranteeing to filter the water quality of back water purification, filter material layer 4 width in the horizontal direction generally can be made as 0.7m～1.5m, and the degree of depth generally can be made as 2.5m～4m;

Described inlet channel 2 is separated by first filter plate 21 that is positioned at its both sides, on first filter plate 21, be uniformly distributed with permeable hole 22, and on first filter plate 21, also tilt down to be provided with baffle plate 23, referring to Fig. 4, direction shown in the arrow is the flow direction, and describedly goes out water channel 3 and be separated by second filter plate 31 that is positioned at its both sides, second filter plate 31 is a dividing plate, be uniformly distributed with filter 32 on second filter plate 31, referring to Fig. 3, direction shown in the arrow is the flow direction;

Described inlet channel 2 and go out water channel 3 compartment of terrain that crosses one another and be erected on pond body 1 bottom, described filter material layer 4 is then at inlet channel 2 and go out between the water channel 3, and, a side is provided with the water inlet pipe 6 that the port of export is connected with inlet channel 2 outside pond body 1, and body 1 outer opposite side in pond then is provided with arrival end and goes out the outlet pipe 7 that water channel 3 is connected;

Simultaneously, among described filter material layer 4, also be provided with back purge system 9, it comprises air inlet pipe 91, air-lift unit pipe 92, sand separator 93 and sand distributor 94, wherein, be inserted among the filter material layer 4 to air-lift unit pipe 92 relative pond body 1 bottom vertical, the position of air inlet pipe 91 is near the bottom of pond body 1, and this air inlet pipe 91 is connected with the lower part of air-lift unit pipe 92, also is that backwash gas can flow toward the top of air-lift unit pipe 92 from the bottom of air-lift unit pipe 92 by air inlet pipe 91;

Described sand separator 93 includes that internal layer annular sidewall 93a and outer annular sidewall 93b surround, the top has venthole 93c, the ring-type backwash chamber 93d of bottom opening and internal layer annular sidewall 93a surround, bottom lock, dirty chamber 93e gathers in open-topped central authorities, the top of described air-lift unit pipe 92 is connected with the top of the ring-type backwash chamber 93d of this sand separator 93, circulus characteristics in conjunction with ring-type backwash chamber 93d, make the dirty filtrate of bringing up from air-lift unit pipe 92 can enter ring-type backwash chamber 93d with circling round, and in ring-type backwash chamber 93d, fully rub with clear water, flushing, the top of described air-lift unit pipe 92 are to communicate with backwash chamber 93d with the tangent mode of the outer annular sidewall 93b of sand separator 93;

This sand separator 93 also is circumscribed with a blow-off pipe 8, these blow-off pipe 95 inlets pass described inside and outside two-layer

annular sidewall

93a, 93b and are connected with the poly-dirty chamber 93e of described central authorities, and, have the intercommunicating pore 93a1 that is higher than described blow-off pipe 95 porch on the described internal layer annular sidewall 93a;

And described sand distributor 94 is conduction pipes that two ends connect, and the relative sand separator 93 of this conduction pipe is provided with obliquely, and an end of this conduction pipe is connected with the opening of backwash chamber 93d bottom in the sand separator 93, and the other end is then towards described filter material layer 4;

Described inlet channel 2 and the top that goes out water channel 3 are lower than the water level in the pond body 1, and inlet channel 2, the top that goes out water channel 3 all are provided with cover plate 5;

All be provided with valve on described water inlet pipe 6, outlet pipe 7, air inlet pipe 91, the blow-off pipe 8;

Also be provided with liquid level gauge 10 on body 1 inwall of described pond.

When the utility model embodiment carries out normal filtration at sewage, former water enters into inlet channel 2 from water inlet pipe 6, flow to filter material layer 4 by the permeable hole 22 on first filter plate 21 of inlet channel 2 both sides, former water becomes clear water through the filtration of filtrate, and laterally flow toward the contiguous water channel 3 that goes out, collect out among the water channel 3 by going out filter 32 on second filter plate 31 of water channel 3 both sides, last clear water after filtering flows out from outlet pipe 7, thereby realizes sewage water filtration with the filter type that current are laterally walked about;

When carrying out backwash, backwash gas with certain pressure enters into air-lift unit pipe 92 bottoms from air inlet pipe 91, dirty filtrate under air-lift unit pipe 92 bottoms fills the top that gas washing is promoted to air-lift unit pipe 92 along with counter, this moment, dirty filtrate carried out preliminary scouring with backwash gas in whole air-lift unit pipe 92, dirty filtrate and backwash gas continue and enter into the top of sand separator 93 backwash chamber 93d from the top of air-lift unit pipe 92, and backwash gas is discharged from the venthole 93c at 93d top, backwash chamber; Because the poly-dirty chamber 93e of central authorities is communicated with and the extraneous blow-off pipe 95 that communicates, water level is higher than the water level in the poly-dirty chamber 93e of central authorities all the time in the pond body 1, the clear water of sand distributor 94 bottoms can be drawn in the sand distributor 94 automatically, then upwards flow into backwash chamber 93d, flow into the poly-dirty chamber 93e of central authorities through the intercommunicating pore 93a1 on the sand separator 93 internal layer annular sidewall 93a, in this flow process of clear water, filtrate is because deadweight, can drop from sand separator 93 toward sand distributor 94 automatically, and among the conduction pipe that sand distributor 94 tilts falls back filter material layer 4, fully friction takes place between clear water and the dirty filtrate, filtrate is washed, at last, the water that flows into the poly-dirty chamber 93e of central authorities is exactly the sewage that washed dirty filtrate, flows out from blow-off pipe 95 then, referring to Fig. 5 and Fig. 6, wherein be the flow direction of current shown in Fig. 5 hollow core arrow, be the flow direction of filtrate shown in the filled arrows; Like this, filtrate is through after circulating several times, and the filtrate in the whole pond body 1 all has been rinsed totally.

Claims

1, a kind of filtering ponds of transverse stream filtering include pond body (1) and are distributed in inlet channel (2) in the pond body (1), go out water channel (3) and filter material layer (4), it is characterized in that:

Described inlet channel (2) and go out water channel (3) and be separated by first filter plate (21) that is positioned at its both sides, second filter plate (31) respectively, described inlet channel (2) and go out water channel (3) compartment of terrain that crosses one another and be erected on pond body (1) bottom, described filter material layer (4) then is positioned at inlet channel (2) and goes out between the water channel (3), and, a side is provided with the water inlet pipe (6) that the port of export is connected with inlet channel (2) outside described pond body (1), and the outer opposite side of pond body (1) then is provided with arrival end and goes out the outlet pipe (7) that water channel (3) is connected;

Simultaneously, among described filter material layer (4), also be provided with back purge system (9), it comprises air inlet pipe (91), air-lift unit pipe (92), sand separator (93) and sand distributor (94), wherein, described air-lift unit pipe (92) is inserted among the filter material layer (4) to pond body (1) bottom vertical relatively, and the lower part of this air-lift unit pipe (92) is connected with described air inlet pipe (91);

Described sand separator (93) includes inside and outside two-layer annular sidewall (93a, 93b) surround, the top has venthole (93c), the ring-type backwash chamber (93d) of bottom opening and internal layer annular sidewall (93a) surround, bottom lock, dirty chamber (93e) is gathered by open-topped central authorities, the top of described air-lift unit pipe (92) is connected with the top in the ring-type backwash chamber (93d) of this sand separator (93), and this sand separator (93) also is circumscribed with a blow-off pipe (8), this blow-off pipe (8) inlet passes described inside and outside two-layer annular sidewall (93a, 93b) gathering dirty chamber (93e) with described central authorities is connected, and, have the intercommunicating pore (93a1) that is higher than described blow-off pipe (8) porch on the described internal layer annular sidewall (93a);

And described sand distributor (94) is the conduction pipe that two ends connect, and the one end is connected with the opening of bottom, backwash chamber (93d) in the sand separator (93), and the other end is then towards described filter material layer (4).

2, the filtering ponds of transverse stream filtering according to claim 1 is characterized in that: described sand distributor (94) sand separator (93) relatively is provided with obliquely.

3, the filtering ponds of transverse stream filtering according to claim 1 is characterized in that: described second filter plate (31) that goes out water channel (3) both sides is a dividing plate, and is uniformly distributed with filter (32) on dividing plate.

4, the filtering ponds of transverse stream filtering according to claim 1, it is characterized in that: be uniformly distributed with permeable hole (22) on first filter plate (21) of described inlet channel (2) both sides, and also tilt down to be provided with baffle plate (23) on first filter plate (21).

5, according to the filtering ponds of the described transverse stream filtering of arbitrary claim in the claim 1 to 4, it is characterized in that: described inlet channel (2) and the top that goes out water channel (3) are lower than the water level in the pond body (1), and described inlet channel (2), the top that goes out water channel (3) all are provided with cover plate (5).

6, the filtering ponds of transverse stream filtering according to claim 5 is characterized in that: described outlet pipe (7) is provided with valve.

7, the filtering ponds of transverse stream filtering according to claim 5 is characterized in that: also be provided with liquid level gauge (10) on described pond body (1) inwall.