CN102531150A - Biological air floating treatment device - Google Patents
Biological air floating treatment device Download PDFInfo
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- CN102531150A CN102531150A CN2012100377009A CN201210037700A CN102531150A CN 102531150 A CN102531150 A CN 102531150A CN 2012100377009 A CN2012100377009 A CN 2012100377009A CN 201210037700 A CN201210037700 A CN 201210037700A CN 102531150 A CN102531150 A CN 102531150A
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Abstract
The invention discloses a biological air floating treatment device, which comprises an air floating pond, an air dissolving system and a material collecting system, wherein a contact reaction area, a separation area and a clear water tank which are communicated mutually are formed in the air floating pond sequentially along the transverse direction; the air dissolving system comprises an air dissolving pump, an air dissolving tank and an air dissolving releaser; the material collecting system comprises a scraping device and a collection tank; and the air dissolving releaser is arranged below the contact reaction area. The biological air floating treatment device is characterized in that: a biochemical contact area and an aerating oxygenation area are formed on the lower part of the separation area sequentially. According to the biological air floating treatment device, the chemical oxygen demands (COD) of sewage are reduced effectively by combining a physicochemical method and a biochemical method organically; and aeration is performed by using the air dissolving releaser, so that the aeration efficiency is improved greatly, and energy consumption is reduced.
Description
Technical field
The present invention relates to a kind of air-floating apparatus, particularly a kind of organism gas float treatment unit.
Background technology
Flotation waste water treatment is meant manages in water, to feed or produce a large amount of micro bubbles, and it is adhered on the impurity wadding grain, causes the state of density less than water, and relies on buoyancy that it is floated to the water surface, thereby realize solid-liquid separation.Because the density of air is much littler than water, has only 1/775 of water, therefore adhered to the wadding grain of some amount microbubble, its ascent rate is much faster than the sinking velocity of former wadding grain, thereby causes the disengaging time much shorter of air supporting method than the precipitator method.In addition, the air supporting method not only go turbid, be superior to settling tank aspect discoloring, and the COD in reducing polluted source, xylogen and improve and unique advantage is all arranged aspect the oxygen in water.Lower than settling tank cost, the residence time is short, and floor space is little.
The biological filter be under aerobic condition, utilize attached to the microbial film on the carrier to water in a kind of method of removing of biodegradable material.There are ordinary biofilter (trickling filter), high-rate filter, tower biological filter, BAF etc. in biological filter commonly used at present.Its principle is: in the biological filter, sewage is evenly distributed in the surface, filter tank through water distributor, under action of gravity; Spray to drip shape, a part is adsorbed on filter material surface, becomes the water layer that adheres to that is film like; Another part is then with the form seepage flow filtering layer of film; Become mobile water layer, arrive water exhaust system at last, flow out outside the pond.During the effluent stream filter bed; Filtrate has been held back the suspended substance in the sewage; While is adsorbed on colloid in the sewage and dissolved matter on the surface of oneself; Organism is wherein utilized with growth and breeding by mikrobe, and these mikrobes have further been adsorbed the material that is suspension, colloid and dissolved state in the sewage again, have formed microbial film gradually.After the microbial film maturation; Perch on microbial film mikrobe promptly with the organism in the sewage as nutrition; Organism in the sewage is carried out the adsorption and oxidation effect; Pollutent in the water inlet contacts materialization and the biochemical action that produces with the filter tank filtrate simultaneously, and ammonia nitrogen, nitrite in the water are effectively removed, and sewage is purified.In the operational process of biological filter, hydraulic load, organic loading and oxygen supply condition are the important factors that influences the biological filter performance.In conjunction with above-mentioned analysis; The biological filter is an aerobic treatment process, if can make full use of the dissolved oxygen in leading portion treatment process (air supporting) water outlet, then can reduce aeration rate; Cut down the consumption of energy, so it can be regarded as a kind of efficient low-consume purification of water quality treatment process with Sustainable development meaning.
Summary of the invention
The objective of the invention is to organically physico-chemical process and biochemical method combined; Flat flow organism gas float treatment unit is provided; It effectively utilizes the solid-liquid separation function of traditional air flotation pool, and the space uses fully under the zone of action liquid that again can be creatively that traditional air supporting is vacant, introduces microbial film; Handle through biological chemistry, reach the purpose of removing BOD in the sewage.
For achieving the above object, the present invention adopts following technical scheme to realize:
The organism gas float treatment unit; Comprise air flotation pool, air dissolving system and material collection system, laterally be provided with reaction zone of action, disengaging zone and the Rinsing Area that is interconnected successively in the said air flotation pool, said air dissolving system comprises air dissolved pump, dissolving and dissolved air release; Said material collection system comprises scraping device and receiving tank; Below, said reaction zone of action is provided with dissolved air release, it is characterized in that bottom, said disengaging zone sets gradually biochemical zone of action and aeration aerating district.The densification that the aeration aerating district forms and trickle small bubbles provide sufficient and oxygen efficiently for biochemical zone of action.When this zone of flowing through downwards through the sewage of solid-liquid separation, the BOD in the sewage is effectively degraded at this.
Further, arrange the biofilm packing layer in the said biochemical zone of action, through COD in the biochemical method degradation water.
Further, the below of said biofilm packing layer is provided with dissolved air release, reaches high efficient aeration and prevents that biofilm detachment from influencing the purpose of system's effluent quality with this.
Further, in the said aeration aerating district micro bubble generation device is set.
Further, said scraping device comprise motor, by said motor-driven sprocket wheel and the traction scraper plate that drives by said sprocket wheel.
Further, bottom, said disengaging zone is provided with the perforation header that communicates with said Rinsing Area.
Further, be connected with liquid level on the said Rinsing Area and regulate weir plate.
The invention has the beneficial effects as follows:, reach the reduction COD of sewage effectively through the combination of physical chemistry and biochemical method; Adopt the dissolved air release aeration, greatly improved aeration efficient, energy efficient.
Description of drawings
Fig. 1 is the side-view of organism gas float treatment unit according to the invention;
Wherein:
The 1-water inlet pipe; 2-dissolved air water water inlet pipe; 3-contact reacts district; 4-aeration aerating district; The 5-disengaging zone; The biochemical zone of action of 6-; The 7-scraping device; The 8-receiving tank; The 9-header of boring a hole; The 10-Rinsing Area; The 11-water outlet; The 12-liquid level is regulated weir plate.
Embodiment
For to structure of the present invention, characteristic and effect thereof, can have and further understand and be familiar with, lift a preferred embodiment at present, and be described with reference to the accompanying drawings as follows:
Embodiment 1
As shown in Figure 1; Organism gas float treatment unit of the present invention; Comprise air flotation pool, air dissolving system and material collection system; Said air flotation pool one side is provided with water inlet pipe 1 and dissolved air water water inlet pipe 2, laterally is provided with contact reacts district 3, disengaging zone 5 and the Rinsing Area 10 that is interconnected successively in the air flotation pool, and 5 bottoms, disengaging zone are provided with the perforation header 9 that communicates with said Rinsing Area 10.5 bottoms, disengaging zone set gradually biochemical zone of action 6 and aeration aerating district 4, and aeration aerating is provided with micro bubble generation device in the district.The densification that the aeration aerating district forms and trickle small bubbles provide sufficient and oxygen efficiently for biochemical zone of action.When this zone of flowing through downwards through the sewage of solid-liquid separation, the BOD in the sewage is effectively degraded at this.Arrange the biofilm packing layer in the said biochemical zone of action 6, through COD in the biochemical method degradation water.Dissolved air release 12 is arranged on the below of said biofilm packing layer, reaches high efficient aeration and prevents that biofilm detachment from influencing the purpose of system's effluent quality with this.3 belows, contact reacts district also are provided with dissolved air release 12.Be connected with liquid level on the said Rinsing Area 10 and regulate weir plate 12.Rinsing Area 10 1 sides are provided with water outlet 11.
Said material collection system comprises scraping device 7 and material collection groove 8, and scraping device 7 comprises motor, by said motor-driven sprocket wheel and the traction scraper plate that driven by said sprocket wheel.
During use, sewage gets into the organism gas float pond via water inlet pipe 1, and dissolved air water also gets into air flotation pool from dissolved air water water inlet pipe 2 simultaneously.Sewage and dissolved air water 3 contacts mixings fully in the contact reacts district, then the mixing water of dissolved air water and sewage entering separating reaction district 5 completion flotation separation.At this, the suspended substance in the water gathers at the water surface, skims water surface scum silica frost and is concentrated to receiving tank 8 through slag scraper 7 then.Set gradually biochemical zone of action 6 and aeration aerating district 4 in the bottom, flotation separation zone.The densification that the aeration aerating district forms and trickle small bubbles provide sufficient and oxygen efficiently for biochemical zone of action.When this zone of flowing through downwards through the sewage of solid-liquid separation, the BOD in the sewage is effectively degraded at this.The water outlet of biochemical zone of action is concentrated to Rinsing Area 10 through perforation header 9 at last, most of pond body of discharging, and the small portion backflow forms dissolved air water and gets into internal recycle.
Claims (6)
1. organism gas float treatment unit; Comprise air flotation pool, air dissolving system and material collection system, laterally be provided with reaction zone of action, disengaging zone and the Rinsing Area that is interconnected successively in the said air flotation pool, said air dissolving system comprises air dissolved pump, dissolving and dissolved air release; Said material collection system comprises scraping device and receiving tank; Below, said reaction zone of action is provided with dissolved air release, it is characterized in that bottom, said disengaging zone sets gradually biochemical zone of action and aeration aerating district.
2. organism gas float treatment unit as claimed in claim 1 is characterized in that, arranges the biofilm packing layer in the said biochemical zone of action.
3. organism gas float treatment unit as claimed in claim 2 is characterized in that, the aeration aerating district, below of said biofilm packing layer is provided with dissolved air release and serves as microbubble generator.
4. organism gas float treatment unit as claimed in claim 1 is characterized in that, said scraping device comprises motor, by said motor-driven sprocket wheel and the traction scraper plate that driven by said sprocket wheel.
5. organism gas float treatment unit as claimed in claim 1 is characterized in that, bottom, said disengaging zone is provided with the perforation header that communicates with said Rinsing Area.
6. organism gas float treatment unit as claimed in claim 1 is characterized in that, is connected with liquid level on the said Rinsing Area and regulates weir plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100377009A CN102531150A (en) | 2012-02-20 | 2012-02-20 | Biological air floating treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100377009A CN102531150A (en) | 2012-02-20 | 2012-02-20 | Biological air floating treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102531150A true CN102531150A (en) | 2012-07-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012100377009A Pending CN102531150A (en) | 2012-02-20 | 2012-02-20 | Biological air floating treatment device |
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| CN (1) | CN102531150A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103663820A (en) * | 2013-12-30 | 2014-03-26 | 大连宏博水科技有限公司 | Air-flotation and membrane-filtration purification system |
| CN104310554A (en) * | 2014-11-05 | 2015-01-28 | 扬州大学 | Novel micro-nano bubble flocculation-air floatation process |
| CN107129047A (en) * | 2017-07-10 | 2017-09-05 | 湖南美奕机电科技有限公司 | A kind of drum type brake sewage disposal device |
| CN107188377A (en) * | 2017-07-13 | 2017-09-22 | 湖南美奕机电科技有限公司 | A kind of integrated sewage treating apparatus |
| CN107601653A (en) * | 2016-07-12 | 2018-01-19 | 天津宏晟新环保科技有限公司 | A kind of equipment that sewage is handled using living things catalysis |
| CN113896319A (en) * | 2021-10-14 | 2022-01-07 | 常州科德水处理成套设备股份有限公司 | Printing and dyeing sewage integrated type super-efficient dissolved oxygen treatment reactor |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2796246B2 (en) * | 1994-04-29 | 1998-09-10 | 和泉電気株式会社 | Wastewater treatment equipment |
| CN1413916A (en) * | 2002-07-17 | 2003-04-30 | 王文兵 | Air-floated biological treatment process and equipment |
| KR100578892B1 (en) * | 2003-05-02 | 2006-05-17 | 손을택 | Flotation separation treatment apparatus and method |
| CN101691266A (en) * | 2009-10-15 | 2010-04-07 | 贵州荣源环保科技有限公司 | Integral water clarifier for treating high concentrated organic wastewater and normal water |
-
2012
- 2012-02-20 CN CN2012100377009A patent/CN102531150A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2796246B2 (en) * | 1994-04-29 | 1998-09-10 | 和泉電気株式会社 | Wastewater treatment equipment |
| CN1413916A (en) * | 2002-07-17 | 2003-04-30 | 王文兵 | Air-floated biological treatment process and equipment |
| KR100578892B1 (en) * | 2003-05-02 | 2006-05-17 | 손을택 | Flotation separation treatment apparatus and method |
| CN101691266A (en) * | 2009-10-15 | 2010-04-07 | 贵州荣源环保科技有限公司 | Integral water clarifier for treating high concentrated organic wastewater and normal water |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103663820A (en) * | 2013-12-30 | 2014-03-26 | 大连宏博水科技有限公司 | Air-flotation and membrane-filtration purification system |
| CN104310554A (en) * | 2014-11-05 | 2015-01-28 | 扬州大学 | Novel micro-nano bubble flocculation-air floatation process |
| CN107601653A (en) * | 2016-07-12 | 2018-01-19 | 天津宏晟新环保科技有限公司 | A kind of equipment that sewage is handled using living things catalysis |
| CN107129047A (en) * | 2017-07-10 | 2017-09-05 | 湖南美奕机电科技有限公司 | A kind of drum type brake sewage disposal device |
| CN107188377A (en) * | 2017-07-13 | 2017-09-22 | 湖南美奕机电科技有限公司 | A kind of integrated sewage treating apparatus |
| CN113896319A (en) * | 2021-10-14 | 2022-01-07 | 常州科德水处理成套设备股份有限公司 | Printing and dyeing sewage integrated type super-efficient dissolved oxygen treatment reactor |
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Application publication date: 20120704 |