CN101948196B - Cross flow air floating device with secondary filtration - Google Patents

Cross flow air floating device with secondary filtration Download PDF

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Publication number
CN101948196B
CN101948196B CN 201010283506 CN201010283506A CN101948196B CN 101948196 B CN101948196 B CN 101948196B CN 201010283506 CN201010283506 CN 201010283506 CN 201010283506 A CN201010283506 A CN 201010283506A CN 101948196 B CN101948196 B CN 101948196B
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China
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water
chamber
air
porous plate
clean water
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Expired - Fee Related
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CN 201010283506
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Chinese (zh)
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CN101948196A (en
Inventor
王晓东
陈东升
姚奋洪
李春桃
蒋亚辉
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Jiangxi Longxinding Environmental Protection Equipment Co ltd
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JIANGSU XINLONGDING COMPLETE ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd
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Priority to CN 201010283506 priority Critical patent/CN101948196B/en
Publication of CN101948196A publication Critical patent/CN101948196A/en
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Publication of CN101948196B publication Critical patent/CN101948196B/en
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Abstract

The invention discloses a cross flow air floating device with secondary filtration. The device comprises an air floating tank (8); the air floating tank (8) is partitioned into an air floating reaction chamber (9), a water collecting chamber (10) and a clean water chamber (11) through a partition plate arranged in the tank; the air floating reaction chamber (9) is connected with a water inlet (1) and a dissolved air water inlet (2); the water inlet (1) is connected with a feeding device; and the lower part of the water collecting chamber (10) is provided with a perforated water collecting pipe (3). The device is characterized in that: the lower part of the clean water chamber (11) is provided with a porous plate (12); a filter layer (7) is arranged on the porous plate (12); the water outlet end of the perforated water collecting pipe (3) passes through the partition plate from the lower part of the water collecting chamber (10), extends into the clean water chamber (11), then upwards passes through the filter layer (7) and extends to the upper part of the clean water chamber (11); the water inlet of a drain pipe (5) is positioned in the clean water chamber (11) and below the porous plate (12), and the water outlet of the drain pipe (5) is positioned outside the air floating tank (8); and a discharge orifice (14) with draining and backwashing functions is formed in the clean water chamber (11) and on the lower part of the porous plate (12). The device has a simple structure and good water quality.

Description

Cross-flow air floatation device with secondary filtration
Technical field
The present invention relates to a kind of water treating equipment, especially a kind of cross-flow air floatation device, specifically a kind of cross-flow air floatation device with secondary filtration.
Background technology
As everyone knows, the air-flotation type water treating equipment are equipment commonly used in all kinds of water technologies, and as shown in Figure 1, it is comparatively desirable for the purification of water quality of suspended substance proportion about 1.
The air-float water treatment facility mainly is by pressure water and pressure air, in molten cylinder, fully mix, suddenly decompression discharges again, in air-flotation reactor, discharge countless tiny bubbles, bubble can be adsorbed in uphill process on suspended substance or the oils, make it volume and increase and float, regularly remove by slag scraper, all the other relatively water of cleaning collect by the collecting chamber bottom.
Improve the suspended substance removal effect in order to rise to; usually also need to when water inlet, add medicament (flocculation agent) and form alumen ustum; air supporting relies on bubble absorption to reach the purpose that purifies water; but there are a large amount of bubbles to vanish voluntarily mobile the reaching in bubble rising, the stop process of water inlet; therefore having a lot of proportions to be a bit larger tham 1 suspended substance can descend gradually because of bubble-break; form secondary settlement; affect effluent quality; this problem has restricted the performance of airfloat equipment usefulness; thereby airfloat equipment is commonly used for pre-treatment or middle-chain at present domestic, and non-terminal equipment.
Summary of the invention
The objective of the invention is in the bubble uphill process, can cause proportion to be slightly larger than 1 suspended substance realization secondary settlement for existing cross-flow air floatation device because bubble breaks, affect the problem of effluent characteristics, design a kind of cross-flow air floatation device with secondary filtration.
Technical scheme of the present invention is:
A kind of cross-flow air floatation device with secondary filtration, it comprises air flotation pool 8, air flotation pool 8 is air-flotation reactor 9 by the baffle for separating of installing in the pond, collecting chamber 10 and clean water chamber 11, air-flotation reactor 9 is connected with water-in 1 and dissolved air water import 2, dissolved air water import 2 is connected with the outlet of molten cylinder, water-in 1 is connected with chemicals dosing plant, the bottom of collecting chamber 10 is equipped with perforation header 3, the bottom that it is characterized in that described clean water chamber 11 is equipped with porous plate 12, drain cap 13 is installed on the prosopyle of porous plate 12, filtering layer 7 is installed on the porous plate 12, the water side of described perforation header 3 is passed dividing plate and is stretched into and be upward through the top that filtering layer 7 stretches into clean water chamber 11 clean water chamber 11 again from the bottom of collecting chamber 10, the water-in of water shoot 5 is arranged in clean water chamber 11, the bottom of porous plate 12, the water outlet of water shoot 5 are positioned at outside the air flotation pool 8; In clean water chamber 11, the bottom of porous plate 12 is equipped with the discharge hole mouth 14 that has blowdown and back flushing concurrently.
The thickness of described filtering layer 7 is 400-600mm, and the particle diameter of filtrate is 0.6~1.2mm.
Described drain 14 is connected with outlet and the blow-off pipe of molten cylinder respectively by three-way valve.The beneficial effects of the utility model:
The present invention is by making the again process filtering layer through flocculation treatment water carry out secondary filtration, thoroughly which proportion is slightly larger than 1 fall because of the bubble contaminant filter that is deposited in the clear water zone that breaks, for improving effluent characteristics very important effect is arranged, can be used as final water through the water quality after the present invention's processing, this also so that the cross-flow type air-floated water treating apparatus can be used as the terminating unit use, greatly reduces the cost of water treatment complete equipment.
The present invention is simple in structure, is easy to realize, and need not backwashing equipment and can finish back flushing to filtering layer, and it can utilize the sewage draining exit of former usefulness to link to each other with the molten cylinder that produces high pressure water and bubble, utilizes the pressure water of molten cylinder directly to recoil.
Description of drawings
Fig. 1 is the structural representation of existing vertical-flow air flotation device.
Fig. 2 is structural representation of the present invention.
Embodiment
The present invention is further illustrated below in conjunction with drawings and Examples.
As shown in Figure 2.
A kind of cross-flow air floatation device with secondary filtration, it comprises air flotation pool 8, air flotation pool 8 is air-flotation reactor 9 by the baffle for separating of installing in the pond, collecting chamber 10 and clean water chamber 11, air-flotation reactor 9 is connected with water-in 1 and dissolved air water import 2, the outlet of dissolved air water import 2 and molten cylinder (fully mix irregularly produce a large amount of small bubbles by dissolved air water import 2 in air-flotation reactor 9 afterwards with pressure water and pressure air) is connected, water-in 1 is connected with chemicals dosing plant (structure is identical with existing chemicals dosing plant), the bottom of collecting chamber 10 is equipped with perforation header 3, the top of collecting chamber 10 is equipped with slag scraper 6 and ash pit 4, the bottom of described clean water chamber 11 is equipped with porous plate 12, ABS drain cap 13 is installed on the prosopyle of porous plate 12, filtering layer 7 is installed on the porous plate 12, the thickness of filtering layer 7 is 400-600mm, it is the quartz sand of 0.6~1.2mm that filtrate can adopt particle diameter, the water side of perforation header 3 is passed dividing plate and is stretched into and be upward through the top that filtering layer 7 stretches into clean water chamber 11 clean water chamber 11 again from the bottom of collecting chamber 10, the water-in of water shoot 5 is arranged in clean water chamber 11, the bottom of porous plate 12, the water outlet of water shoot 5 are positioned at outside the air flotation pool 8; In clean water chamber 11, the bottom of porous plate 12 is equipped with the discharge hole mouth 14 that has blowdown and back flushing concurrently, drain 14 is connected with outlet and the blow-off pipe of molten cylinder respectively by three-way valve, when needs carry out back flushing to filtering layer, only need open the road valve that is communicated with molten cylinder and can directly utilize the pressure water in the molten cylinder to carry out back flushing, the water of back flushing can be discharged by ash pit 4.
During work, the residence time of processed water in air-floating apparatus, flow velocity was 10m/h about 40min, and is basically identical with filter chamber, filtering velocity; Thereby without the filter chamber problem that blocks water.Back flushing and molten cylinder are realized interlock, need not to establish in addition water pump, and back flushing water outlet and former ash pit share.The processing water yield of utility model can be altogether: 5~200m 3/ h.
Part that the present invention does not relate to such as chemicals dosing plant, slag scraper, molten cylinder, perforation header etc. all prior art that maybe can adopt same as the prior art are realized.

Claims (4)

1. cross-flow air floatation device with secondary filtration, it comprises air flotation pool (8), air flotation pool (8) is air-flotation reactor (9) by the baffle for separating of installing in the pond, collecting chamber (10) and clean water chamber (11), air-flotation reactor (9) is connected with water-in (1) and dissolved air water import (2), dissolved air water import (2) is connected with the outlet of molten cylinder, water-in (1) is connected with chemicals dosing plant, the bottom of collecting chamber (10) is equipped with perforation header (3), the bottom that it is characterized in that described clean water chamber (11) is equipped with porous plate (12), drain cap (13) is installed on the prosopyle of porous plate (12), filtering layer (7) is installed on the porous plate (12), the water side of described perforation header (3) is passed dividing plate and is stretched into and be upward through the top that filtering layer (7) stretches into clean water chamber (11) the clean water chamber (11) again from the bottom of collecting chamber (10), the water-in of water shoot (5) is arranged in clean water chamber (11), the bottom of porous plate (12), the water outlet of water shoot (5) are positioned at outside the air flotation pool (8); In clean water chamber (11), the bottom of porous plate (12) is equipped with the drain (14) that has blowdown and back flushing concurrently.
2. the cross-flow air floatation device with secondary filtration according to claim 1, the thickness that it is characterized in that described filtering layer (7) is 400-600mm, the particle diameter of filtrate is 0.6~1.2mm.
3. the cross-flow air floatation device with secondary filtration according to claim 1 is characterized in that described drain (14) is connected with outlet and the blow-off pipe of molten cylinder respectively by three-way valve.
4. the cross-flow air floatation device with secondary filtration according to claim 1 is characterized in that the ash pit (4) that the top of described collecting chamber (10) is equipped with slag scraper (6) and matches.
CN 201010283506 2010-09-16 2010-09-16 Cross flow air floating device with secondary filtration Expired - Fee Related CN101948196B (en)

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Application Number Priority Date Filing Date Title
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CN101948196B true CN101948196B (en) 2013-04-10

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* Cited by examiner, † Cited by third party
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CN111790192A (en) * 2020-07-23 2020-10-20 新昌县以琳环保科技有限公司 Waste filtering and separating treatment device

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1364732A (en) * 2001-01-09 2002-08-21 徐景颖 Method and device for purifying slightly polluted water source by using air floated biological active carbon
CN2594264Y (en) * 2002-12-30 2003-12-24 王博涵 Household water purifier
CN101148275A (en) * 2007-07-26 2008-03-26 北京蓝海世达科技有限公司 PVC centrifugal mother liquor treatment reclaiming technique and device
CN101215060A (en) * 2007-12-27 2008-07-09 江苏工业学院 Device for treating oil field waste water
CN201292263Y (en) * 2008-12-05 2009-08-19 北京工业大学 Vertical flow type aerobic gas float filter chamber
CN201785273U (en) * 2010-09-16 2011-04-06 江苏新龙鼎环保成套工程有限公司 Cross-flow air floatation device with secondary filtration

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101323494A (en) * 2008-04-30 2008-12-17 北京能拓高科技有限公司 Carwash circulating water processing system

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1364732A (en) * 2001-01-09 2002-08-21 徐景颖 Method and device for purifying slightly polluted water source by using air floated biological active carbon
CN2594264Y (en) * 2002-12-30 2003-12-24 王博涵 Household water purifier
CN101148275A (en) * 2007-07-26 2008-03-26 北京蓝海世达科技有限公司 PVC centrifugal mother liquor treatment reclaiming technique and device
CN101215060A (en) * 2007-12-27 2008-07-09 江苏工业学院 Device for treating oil field waste water
CN201292263Y (en) * 2008-12-05 2009-08-19 北京工业大学 Vertical flow type aerobic gas float filter chamber
CN201785273U (en) * 2010-09-16 2011-04-06 江苏新龙鼎环保成套工程有限公司 Cross-flow air floatation device with secondary filtration

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Owner name: XINLONGDING HOLDING GROUP CO., LTD.

Free format text: FORMER NAME: JIANGSU XINLONGDING COMPLETE ENVIRONMENTAL PROTECTION ENGINEERING CO., LTD.

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Address after: 214215 Jiangsu city of Nanjing province Yixing city and Town Industrial Zone South

Patentee after: XINLONGDING HOLDING GROUP Co.,Ltd.

Address before: 214215 Jiangsu city of Nanjing province Yixing city and Town Industrial Zone South

Patentee before: Jiangsu Xin Longding Environmental Protection Engineering Co.,Ltd.

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Effective date of registration: 20211117

Address after: 334000 zone a, Luyang Industrial Park, Shangrao high tech Zone, Guangfeng District, Shangrao City, Jiangxi Province

Patentee after: Jiangxi longxinding environmental protection equipment Co.,Ltd.

Address before: 214215 Nanxin Industrial Zone, HeQiao Town, Yixing City, Nanjing, Jiangsu Province

Patentee before: XINLONGDING HOLDING GROUP Co.,Ltd.

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130410