CN1597042A - Moving bed filter - Google Patents
Moving bed filter Download PDFInfo
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- CN1597042A CN1597042A CN 03134006 CN03134006A CN1597042A CN 1597042 A CN1597042 A CN 1597042A CN 03134006 CN03134006 CN 03134006 CN 03134006 A CN03134006 A CN 03134006A CN 1597042 A CN1597042 A CN 1597042A
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- filtrate
- washer
- tank body
- filter
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Abstract
A moving-bed filter able to continuously run for treating water is composed of cylindrical tank, water distributor, filtering bed, fairing unit, air distributor, filtering material delivering pipe, gas separator, washer, filtering material distributor and the regulating valve for the washing water.
Description
Technical field
The present invention relates to a kind of water treatment facilities, more specifically say so and remove the filter plant of suspension in the water, particularly can carry out the moving bed filter of continuous filtration operation.
Background technology
Filtration is as one of the removal means of suspension in the water, owing to have the good removal effect and the high processing degree of depth, not only in city or trade effluent advanced treating and reusing sewage processing, be used widely, and be that the equipment that processes such as (as running water, industrial fresh water, boiler feedwater), recirculated cooling water processing generally adopt is handled in city and industrial water supply.
Filter is removed the mechanism of suspension, mainly is to utilize the micro-pore that filters bed inside, and particulate contaminants in the trap water, its course of work comprises filters and two processes of filtrate cleaning.According to different conditions such as filtrate, filtering velocity, water (flow) direction, the bed depth, current motive forces, filter can mark off number of different types.If according to whether moving of filter medium in the filter process, then can reduce two types of fixed bed and moving beds.
The fixed bed filtering device mainly relies on the filter bed top layer to hold back suspension to the filtrate of 300～400mm below the top layer, and not only pollutant holding capability is low, and in use, exists obviously and the shortcoming that can't overcome.One of shortcoming is to realize continuous filtration product water, i.e. filtration can not be carried out simultaneously with backwash, filters with backwash process manually or to automatically switch; Two of shortcoming is general washing or the air-water backwashing mode of adopting when being the filtrate cleaning, needs high-power flushing water pump; Three of shortcoming is no matter to adopt which kind of cleaning way, and filtrate all is difficult for thoroughly cleaning up, and the result is along with the prolongation of time, the filtrate conglomeration, and water-flowing amount descends, and the effluent quality variation finally quits work, and changes filtrate; Four of shortcoming is the time length of filter cycle, and the influence of being advanced concentration of suspension height in the water is bigger, can't fix or prolong, and when concentration of suspension is higher in sewage, can not keep long-time filtration, and backwash is frequent, and aquifer yield is low.Chinese patent 94217260 discloses a kind of fluid bed reversely-washing filter, adopts liftable filtrate extruding disk, and extruding disk moves up when backwash, uses high-speed water jets to wash away filtrate, makes filtrate journey fluidized state, wash away the back with extruding disk with the filtrate compacting.This filter is intermittent operation in use, and the problems referred to above do not have fine solution.
Moving bed filter not only can solve the problem that the fixed bed fixed bed exists, and can realize continued operation, prevents filtrate caking etc.US4126546 discloses a kind of moving bed filter, its filtrate circularly enhancing pipe is arranged on filter interior central authorities, its subject matter is that riser takies filter space, the result not only influences filter effect, filtrate skewness after the washing, and equipment installation, maintenance and startup operation etc. are all comparatively difficult.Disclosed moving bed filter such as US5462654, US4891142, filtrate circularly enhancing pipe also is arranged on filter interior central authorities, and filtrate is identical with the flow direction, and draining is arranged in the screen net structure in the filter material layer; Its concurrent flow makes the suspension in the waste water hold back weak effect, and suspension easily passes screen net structure with filtering water outlet, and not only effluent quality is poor, and easily causes silk screen to stop up; The filter space flow is weak even stop to cause " dead angle " below the screen net structure, does not play a role in filtering, and the filter space utilization rate is low.US5746913, US5277829 etc. disclose a kind of moving bed filter, filtrate circularly enhancing pipe is arranged on the filter outside, cofferdam overflow mode is adopted in its draining, and overflow area accounts for the filter part partial cross-section, and filtrate loops back the position deviation filter center position of filtering bed; Because the existence of overflow area, make the current skewness of in filtering tank lateral cross section; Because filtrate falls the position deviation filter center after rise, makes filtrate form uneven accumulation inclined-plane in filter, i.e. filter material layer height difference has increased the weight of the phenomenon of current skewness; The current skewness will cause filtrate not to be fully utilized, and effluent quality is affected.In addition, above-mentioned filter also has following common weak point: 1, the air sparger of filtrate riser all is arranged on the riser bottom, and when filter moved for the first time, filtrate smoothly can promote and circulate, but after filter is out of service because of some reason, restart very difficult; Its reason is that the filtrate accumulation of accumulating in the riser is closely knit, and its height has very big resistance as a result greater than filter interior filtrate bed height in the riser, air easily enters in the lower filtering tank of pressure when restarting, and passing filter bed, filtrate can't promote and circulate.2, filtrate promote with cyclic process in air without separating, directly enter washer with filtrate, not only can be because of speed greatly produce bigger impact to washing, and also it is inhomogeneous to enter the filtrate amount of washer, not of uniform size, influence the clean result and the effluent quality of filtrate.3, simple liquid-solid reflux type is all adopted in the washing of filtrate, the washer unreasonable structure, and filtrate is skewness in washer, can not fully contact with washings, the easy short circuit of rinse water, it is big not only to clean the water yield, and clean result is difficult to guarantee, and then influences effluent quality.
Summary of the invention
At the deficiencies in the prior art, the invention provides the continuous operation type filter that a kind of effluent quality is good, producing water ratio is high, startup is rapid, simple to operate.
Moving bed filter of the present invention comprises members such as tank body, overflow cofferdam, drainpipe, water inlet pipe, water-locator, filtrate washer, rectification body, filtrate distributor, filtrate circularly enhancing pipe and air sparger.Wherein tank body is a tube structure, and the filtrate outlet is arranged at the bottom; Water inlet pipe is arranged at the tank body middle and lower part, and the part of water inlet pipe in tank body is provided with water-locator; The overflow cofferdam is the sleeve circulus of upper opening, is arranged on top, tank body outside, and the cofferdam height need surpass the tank body upper edge; Drainpipe communicates with the overflow cofferdam; The filtrate washer is arranged on tank body internal upper part middle position; Filtrate circularly enhancing pipe is arranged on the tank body outside, and an end communicates with the filtrate outlet of tank body, and an end communicates with washer; Circularly enhancing pipe bottom is provided with and promotes the primary air distributor that filtrate is used, and several auxiliary air distributors are set on the riser again, amounts to 1～10.
Moving bed filter of the present invention can also be provided with gas separator between outlet of filtrate circularly enhancing pipe and washer, avoid pressure air that washer is impacted, and influences clean result.Moving bed filter of the present invention is based on tank body, and attached on the tank body relevant position, concrete structure is as follows on demand for other member.Tank body is a tube structure, and the bottom adopts the inclined-plane or the conical surface to form the filtrate outlet.The overflow cofferdam is the sleeve circulus of upper opening, is arranged on top, tank body outside, and the cofferdam height need surpass the tank body upper edge, and drainpipe communicates with the overflow cofferdam.Water inlet pipe is arranged at the tank body middle and lower part, and the part of water inlet pipe in tank body is provided with water-locator.The filtrate washer is arranged on tank body internal upper part middle position, washer top is provided with circulation filtrate inlet and washings outlet, the washings outlet communicates with the washings drainpipe, the valve of control washings consumption is set on the washings drainpipe, the washer bottom center is provided with the filtrate outlet, and lower side can be provided with the washing water inlet.Can empty barrel structure in the washer, but structure such as baffling swash plate preferably is set, filtrate forms waterfall stream between two adjacent baffling swash plates.Between the exhalant region and scrubbing section of washer, a level or acclivitous speed-raising plate washer can be set.Filtrate circularly enhancing pipe is arranged on the tank body outside, communicates with the outlet of tank body filtrate below, and the inlet of top device separated from the gas communicates.Filtrate riser bottom is provided with and promotes the primary air distributor that filtrate is used, some auxiliary air distributors are set on the riser again, and the air sparger sum can be 1～10, preferred 2～5, distance between each air sparger is same or different, and is preferably identical.Gas separator is arranged on the tank body top, the position is higher than the filtrate washer, gas separator is the empty barrel structure that a volume enlarges, open top or exhaust outlet is set, filtrate circularly enhancing pipe exports device separated from the gas middle and upper part UNICOM, and the gas separator bottom communicates with the filtrate inlet of filtrate washer.
Compared with prior art, moving bed filter of the present invention has following advantage:
(1) diverse location is provided with a plurality of air spargers on the filtrate riser, after having overcome filter and stopping work, because of filtrate in the filtrate riser closely knit, the problem that can't restart.Introduce compressed air by the air sparger of diverse location successively, can start the lifting and the cyclic process of filtrate rapidly, make the filter normal operation input, the operation of filter is very simple.This set also increased filtrate promote with the circulation course of conveying in the probability of friction mutually, help pollutant with filtrate is peeled off, prevent that filtrate is agglomerating, the filtrate after the cleaning is kept all the time as new state.
(2) increase gas separator, filtrate was discharged pressure air before entering washer, not only eliminated because of the excessive impact that washing is produced of flow velocity, and filtrate evenly flows into washer, improve the filtrate clean result, guaranteed the stability and the effluent quality of washing process.
(3) some deflection plates are set in the washer, have guaranteed that filtrate evenly distributes, and fully contacted with washings, the result not only can improve the detersive efficiency of filtrate greatly, the washing water yield is few, but also helps to reduce the scale of washer, improves the space availability ratio of whole filter.
(4) adopt outer cofferdam Overflow drainage structure, ascending current is kept evenly, prevented that effectively filter is because of the different problems that influence filter effect of different cross section flow rate of water flow.
(5) by the control valve of filtrate washing consumption, can guarantee the clean result of filtrate, therefore can adapt to the filtration requirement of different quality, keep uniform water-flowing amount and effluent quality, promptly the suitable property of filter of the present invention is stronger.
Description of drawings
Fig. 1 is the structural representation of an instantiation of moving bed filter of the present invention, by filtering tank body 2, water-locator 21, filter bed 3, rectification body 7, air sparger 10,22,24 and 25, filtrate carrier pipe 9 and 12, gas separator 13, washer 11, filtrate distributor 20, rinse water control valve 19 compositions such as grade.
The specific embodiment
Further specify the structure and the method for operation of moving bed filter of the present invention below in conjunction with accompanying drawing.
Former water enters filtering tank 2 from water inlet 1, after water-locator 21 distributes, upwards flow equably, and by filter bed layer 3, pollutants such as the suspension in the water is trapped within the filtrate.Clean water after the filtration enters the clean water storage area 4 on filtering tank top, enters exhalant region 5 after overflow, discharges through delivery port 6.
When former water is filtered, the filtrate of pollutant has been held back in filtering tank 2 bottoms, under the gravity effect, constantly move down, by rectification body 7, filtrate outlet 8, then under air sparger 10,22,24 and the 25 compressed-air actuated effects of introducing, by filtrate carrier pipe 9,12, be promoted to the gas separator 13 of filter top, fall to equably through pipeline 14 then and obtain cleaning in the washer 11.Clean the filtrate after the cleaning, after end socket 16 rectifications of washer bottom, from the washer bottom filtrate outlet 17 evenly flow out, and after 26 redistributions of filtrate distributor, be back to the top of filter bed 3, form new filter bed.The washing water outlet is discharged by the delivery port on the washer 19.
Washer 11 by cylindrical shell, end socket 16, deflection plate 15, speed-raising plate washer 18, filtrate inlet tube 14, filtrate outlet 17, and outlet pipe 19 form.The zone of speed-raising plate washer more than 18 is the washer exhalant region; Speed-raising plate washer below 18, the zone of containing several deflection plates 15 are the scrubbing section of washer; End socket 16 parts are the commutating zone of washer.
In the filtrate cleaning process, the filtrate from gas separator 13 comes out after pipeline 14 enters washer 11 continuously, relies on the gravity effect, along in 15 dropping process of deflection plate in the scrubbing section, forms waterfall stream.When filtrate falls, clean water from filtering tank top clean water storage area 4, under the water-head effect in filtering tank 2 and washer 11, as the filtrate rinse water, constantly enter from rectification end socket 15, upward to pass through the waterfall stream that filtrate forms between deflection plate, pollutant in the filtrate is carried out, and, enter the exhalant region on washer top rapidly under the effect of speed-raising plate washer 18, flow out through outlet 19.Clean water yield size by valve 20 controls.Filtrate after the cleaning cleaning is discharged through filtrate outlet 17.
Claims (8)
1, a kind of moving bed filter comprises tank body, overflow cofferdam, drainpipe, water inlet pipe, water-locator, filtrate washer, rectification body, filtrate distributor, air sparger, filtrate circularly enhancing pipe component; Wherein tank body is a tube structure, and the filtrate outlet is arranged at the bottom; Water inlet pipe is arranged at the tank body middle and lower part, and the part of water inlet pipe in tank body is provided with water-locator; It is characterized in that the overflow cofferdam is the sleeve circulus of upper opening, be arranged on tank body top, the cofferdam height need surpass the tank body upper edge, and drainpipe communicates with the overflow cofferdam; The filtrate washer is arranged on tank body internal upper part middle position; Filtrate circularly enhancing pipe is arranged on the tank body outside, and an end communicates an end and washer UNICOM with the filtrate outlet of tank body; The riser bottom is provided with and promotes the primary air distributor that filtrate is used, and several auxiliary air distributors are set on the riser again, amounts to 1～10.
2,, it is characterized in that between outlet of filtrate circularly enhancing pipe and washer, gas separator being set according to the described filter of claim 1.
3, according to the described filter of claim 2, it is characterized in that described gas separator is arranged on the tank body top, the position is higher than the filtrate washer; Gas separator is empty barrel structure, open top or exhaust outlet is set, and filtrate circularly enhancing pipe exports device separated from the gas middle and upper part UNICOM, and the gas separator bottom enters the mouth with the filtrate of filtrate washer and communicates.
4,, it is characterized in that the employing inclined-plane, described tank body bottom or the conical surface form the filtrate outlet according to the described filter of claim 1.
5, according to the described filter of claim 1, it is characterized in that described washer top is provided with circulation filtrate inlet and washings outlet, the washings outlet communicates with the washings drainpipe; The washer bottom center is provided with the filtrate outlet, and lower side is provided with the cleaning solution inlet.
6, according to claim 1 or 5 described filters, it is characterized in that being provided with in the described washer several baffling swash plates, filtrate forms waterfall stream between two adjacent baffling swash plates.
7,, it is characterized in that between interior exhalant region of described washer and the scrubbing section level or acclivitous speed-raising plate washer being set according to the described filter of claim 6.
8,, it is characterized in that being provided with on the described washings drainpipe valve of control washings consumption according to the described filter of claim 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03134006 CN1242827C (en) | 2003-09-15 | 2003-09-15 | Moving bed filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03134006 CN1242827C (en) | 2003-09-15 | 2003-09-15 | Moving bed filter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1597042A true CN1597042A (en) | 2005-03-23 |
| CN1242827C CN1242827C (en) | 2006-02-22 |
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ID=34658951
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03134006 Expired - Lifetime CN1242827C (en) | 2003-09-15 | 2003-09-15 | Moving bed filter |
Country Status (1)
| Country | Link |
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| CN (1) | CN1242827C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101952007A (en) * | 2008-01-08 | 2011-01-19 | 帕奎斯公司 | Be used for the device by the filter bed cleaning fluid and be used to measure the method for the movement degree of filter bed |
| CN101991980A (en) * | 2010-10-29 | 2011-03-30 | 黑龙江华清水务有限公司 | Fluidzed carbon filter sieve |
| CN109248642A (en) * | 2018-10-17 | 2019-01-22 | 杨松 | A kind of application method preparing hydrogen fluoride stratum granulosum moving bed filter |
| CN114772876A (en) * | 2022-06-23 | 2022-07-22 | 深圳永清水务有限责任公司北京分公司 | Bioelectrochemical system for high-salinity wastewater treatment |
-
2003
- 2003-09-15 CN CN 03134006 patent/CN1242827C/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101952007A (en) * | 2008-01-08 | 2011-01-19 | 帕奎斯公司 | Be used for the device by the filter bed cleaning fluid and be used to measure the method for the movement degree of filter bed |
| CN101952007B (en) * | 2008-01-08 | 2014-04-09 | 巴格知识产权有限公司 | Device for cleaning fluid by means of filter bed and method for determining extent of movement of filter bed |
| CN101991980A (en) * | 2010-10-29 | 2011-03-30 | 黑龙江华清水务有限公司 | Fluidzed carbon filter sieve |
| CN101991980B (en) * | 2010-10-29 | 2013-03-13 | 黑龙江华清水务有限公司 | Fluid carbon filter sieve |
| CN109248642A (en) * | 2018-10-17 | 2019-01-22 | 杨松 | A kind of application method preparing hydrogen fluoride stratum granulosum moving bed filter |
| CN109248642B (en) * | 2018-10-17 | 2020-07-28 | 杨松 | Use method of moving bed filter for preparing hydrogen fluoride particle layer |
| CN114772876A (en) * | 2022-06-23 | 2022-07-22 | 深圳永清水务有限责任公司北京分公司 | Bioelectrochemical system for high-salinity wastewater treatment |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1242827C (en) | 2006-02-22 |
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Granted publication date: 20060222 |