CN1280205C - High efficiency air-float solid and liquid separator - Google Patents

High efficiency air-float solid and liquid separator Download PDF

Info

Publication number
CN1280205C
CN1280205C CN 200410043641 CN200410043641A CN1280205C CN 1280205 C CN1280205 C CN 1280205C CN 200410043641 CN200410043641 CN 200410043641 CN 200410043641 A CN200410043641 A CN 200410043641A CN 1280205 C CN1280205 C CN 1280205C
Authority
CN
China
Prior art keywords
air flotation
air
flotation pool
water
plate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 200410043641
Other languages
Chinese (zh)
Other versions
CN1594115A (en
Inventor
马军
王静超
刘芳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Harbin Institute of Technology Shenzhen
Original Assignee
Harbin Institute of Technology Shenzhen
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Harbin Institute of Technology Shenzhen filed Critical Harbin Institute of Technology Shenzhen
Priority to CN 200410043641 priority Critical patent/CN1280205C/en
Publication of CN1594115A publication Critical patent/CN1594115A/en
Application granted granted Critical
Publication of CN1280205C publication Critical patent/CN1280205C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Physical Water Treatments (AREA)

Abstract

本发明公开一种用于水处理的气浮固液分离装置——气浮固液分离装置。它包括气浮池(1)和气浮池(1)底部的出水管(5),它还包括垂直于气浮池(1)底部平面且间距相等的若干块竖板(2)、倾斜于气浮池(1)底部平面的斜板(3)和平行于气浮池(1)底部平面的集水板(4),斜板(3)设置在位于其上方的竖板(2)和位于其下方的集水板(4)之间,集水板(4)的表面上均布有过水孔(4-1),集水板(4)位于出水管(5)的上方并把气浮池(1)水平方向截断。由于竖板(2)的分隔导向,水力流态完成由紊流趋于层流的转变,水中的气泡粘附在斜板(3)上。水从过水孔(4-1)均匀地流过集水板(4),使气浮池(1)在整个水平截面内都得到充分利用。本发明具有工作可靠、设计合理和具有较大推广价值的优点。

Figure 200410043641

The invention discloses an air flotation solid-liquid separation device for water treatment—an air flotation solid-liquid separation device. It includes the air flotation pool (1) and the outlet pipe (5) at the bottom of the air flotation pool (1). ) the sloping plate (3) on the bottom plane and the water collecting plate (4) parallel to the bottom plane of the air flotation tank (1), the sloping plate (3) is arranged on the vertical plate (2) above it and the water collecting plate below it Between the plates (4), water holes (4-1) are evenly distributed on the surface of the water collecting plate (4), and the water collecting plate (4) is located above the outlet pipe (5) and the air flotation pool (1) is Direction truncation. Due to the separation and guidance of the vertical plates (2), the hydraulic flow state completes the transition from turbulent flow to laminar flow, and the air bubbles in the water adhere to the inclined plate (3). Water evenly flows through the water collecting plate (4) through the water hole (4-1), so that the air flotation pool (1) can be fully utilized in the entire horizontal section. The invention has the advantages of reliable operation, reasonable design and great popularization value.

Figure 200410043641

Description

The air supporting equipment for separating liquid from solid
Technical field:
The present invention relates to a kind of air supporting equipment for separating liquid from solid that is used for Drinking Water, municipal wastewater and Industrial Wastewater Treatment.
Background technology:
China's " drinking water sanitary standard " increases to existing 101 by original 88, and wherein the requirement for delivery turbidity rises to existing 1ntu by original 3ntu, and this has proposed challenge to the water technology of existing water factory undoubtedly.Improving the treatment effect of existing water factory conventional treatment process, is one of effective way that addresses this problem.Air-float technology has obtained widespread use as a kind of alternative sedimentary solid-liquid separation process in China.At present there is the problem of the following aspects in it: (1) rule of thumb, the design hydraulic load 5~10m/h of traditional air supporting solid-liquid separation process disengaging zone, in order to guarantee the security of water outlet, the normal hydraulic load that adopts does not also reach 8m/h in the design, and this just makes the floor space of disengaging zone obviously increase.(2) device of removing microbubble is not set in the traditional air-float technology, this makes in the water outlet of air-float technology and contains a large amount of microbubbles, and bubble along with the air supporting water outlet enters in the filter tank phenomenon of filtering layer gas bubble blockage takes place easily, thereby shortens the work period in filter tank.These microbubble surfaces also adhere to a large amount of organism simultaneously, have weakened the air supporting solid-liquid separation process and have removed the effect of little pollution.(3) traditional air-float technology adopts the perforated pipe water outlet, and water outlet is not very even, causes the disengaging zone overall utilization rate not high.
Summary of the invention:
Existing air-floating apparatus hydraulic load is low, floor space big in order to overcome, contain shortcoming such as a large amount of microbubbles in the air supporting water outlet, provide a kind of take up an area of little, efficient is high, the microbubble quantity that contains in the air supporting water outlet is few, the air supporting equipment for separating liquid from solid of water outlet better effects if.The present invention realizes by following proposal: a kind of air supporting equipment for separating liquid from solid, it comprises the rising pipe 5 of air flotation pool 1 and air flotation pool 1 bottom, it also comprises the some risers 2 that equate perpendicular to air flotation pool 1 base plane and spacing, favour the some swash plates 3 of air flotation pool 1 base plane and be parallel to the water collection sheet 4 of air flotation pool 1 base plane, swash plate 3 is set in place between the square thereon riser 2 and the water collection sheet below it 4, be evenly equipped with water hole 4-1 on the surface of water collection sheet 4, water collection sheet 4 is positioned at the top of rising pipe 5 and air flotation pool 1 horizontal direction is blocked.Water flows into air flotation pool 1 from the upper end, because the separation of riser 2 guiding, the waterpower fluidised form is finished by turbulent flow and is tending towards streamlined transformation, and the bubble adhesion in the water is on swash plate 3.Because water collection sheet 4 has substituted traditional tubular type captation, water flows through water collection sheet 4 equably from water hole 4-1, and air flotation pool 1 all is fully used in whole horizontal section, has improved the overall utilization rate of disengaging zone.The present invention realized under the bigger situation of air-float tank waterpower load, air flotation pool disengaging zone waterpower fluidised form by turbulent state to the transformation that is tending towards laminar flow regime, thereby strengthened air flotation pool disengaging zone solid-liquid separation function, improved the water outlet effect.This for delivery turbidity of realizing regulation in existing " drinking water sanitary standard " less than 1ntu require significant.In addition, adopt this novel air supporting equipment for separating liquid from solid, the hydraulic load in the time of can improving the operation of air supporting structures, thus saved floor space.Adopt this technology, the microbubble quantity that contains in the air supporting water outlet is reduced, thereby the air supporting water outlet is entered after the filter tank, the possibility that filtering layer produces gas bubble blockage reduces, and the work period in filter tank prolongs.And, remove the ability of little pollution thereby improved air-float technology owing to removed the microbubble that carries large amount of organic.Adopt captation of the present invention to substitute original perforated pipe, make water outlet more even.According to the difference of the hydraulic load of the different of pending source water quality and design, can adopt the water gathering system of the riser and the different parameters of different spacing.The present invention has reliable operation, reasonable in design and have an advantage of big promotional value.
Description of drawings:
Fig. 1 is a structural representation of the present invention.
Embodiment:
Embodiment one: specify present embodiment below in conjunction with Fig. 1.The some risers 2 that it equates by the rising pipe 5 of air flotation pool 1 and air flotation pool 1 bottom, perpendicular to air flotation pool 1 base plane and spacing, the water collection sheet 4 that favours the some swash plates 3 of air flotation pool 1 base plane and be parallel to air flotation pool 1 base plane are formed, swash plate 3 is set in place between the square thereon riser 2 and the water collection sheet below it 4, be evenly equipped with water hole 4-1 on the surface of water collection sheet 4, water collection sheet 4 is positioned at the top of rising pipe 5 and air flotation pool 1 horizontal direction is blocked.
Embodiment two: the difference of present embodiment and embodiment one is that the sheet material of riser 2 and swash plate 3 is aluminium sheet, stainless steel plate, PVC plate, ABS plate, precast slab.These sheet metal thicknesses are little, rigidity strong, protection against corrosion.
Embodiment three: the difference of present embodiment and embodiment one is, the spacing between riser 2 sheet materials is generally 20~500mm, and preferred spacing is 50~200mm.
Embodiment four: the difference of present embodiment and embodiment one is that riser 2 vertical heights are 800~1500mm.
Embodiment five: the difference of present embodiment and embodiment one is, swash plate 3 is 40~80 degree with the angle of inclination of air flotation pool 1 base plane, and preferred angle is 50~60 degree, and the vertical height of swash plate is 200~500mm.
Embodiment six: the difference of present embodiment and embodiment one is that water collection sheet 4 is stainless steel plate or prefabricated cement plate.The both protection against corrosions of this kind material, intensity is high again.
Embodiment seven: the difference of present embodiment and embodiment one is, the water hole 4-1 water flow velocity of water collection sheet 4 is set to 0.05~0.3m/s, and preferable flow rate is 0.1~0.2m/s.The homogeneity that can guarantee the water outlet of air supporting structures and the stability of flotation separation zone waterpower fluidised form so are set, and other is identical with embodiment one.
Embodiment eight: the difference of present embodiment and embodiment one is, water collection sheet 4 is 150~500mm to the distance at 1 end of air flotation pool, and preferred distance is 200~300mm.

Claims (10)

1, a kind of air supporting equipment for separating liquid from solid, it comprises the rising pipe (5) of air flotation pool (1) and air flotation pool (1) bottom, it is characterized in that it also comprises perpendicular to air flotation pool (1) base plane and the equal some risers (2) of spacing, favour the some swash plates (3) of air flotation pool (1) base plane and be parallel to the water collection sheet (4) of air flotation pool (1) base plane, swash plate (3) is set in place square thereon riser (2) and is positioned between the water collection sheet (4) of its below, be evenly equipped with water hole (4-1) on the surface of water collection sheet (4), water collection sheet (4) is positioned at the top of rising pipe (5) and air flotation pool (1) horizontal direction is blocked.
2, air supporting equipment for separating liquid from solid according to claim 1, the sheet material that it is characterized in that riser (2) and swash plate (3) is aluminium sheet, stainless steel plate, PVC plate, ABS plate or precast slab.
3, air supporting equipment for separating liquid from solid according to claim 1, the spacing that it is characterized in that riser (2) is 20~500mm.
4, air supporting equipment for separating liquid from solid according to claim 1 is characterized in that the spacing of riser (2) is 50~200mm.
5, air supporting equipment for separating liquid from solid according to claim 1 is characterized in that riser (2) vertical height is 800~1500mm.
6, air supporting equipment for separating liquid from solid according to claim 1 is characterized in that the swash plate (3) and the angle of inclination of air flotation pool (1) base plane are 40~80 degree, and the vertical height of swash plate is 200~500mm.
7, air supporting equipment for separating liquid from solid according to claim 1 is characterized in that the swash plate (3) and the angle of inclination of air flotation pool (1) base plane are 50~60 degree.
8, air supporting equipment for separating liquid from solid according to claim 1 is characterized in that water collection sheet (4) is stainless steel plate or prefabricated cement plate.
9, air supporting equipment for separating liquid from solid according to claim 1 is characterized in that water collection sheet (4) is 150~500mm to the distance at air flotation pool (1) end.
10, air supporting equipment for separating liquid from solid according to claim 1 is characterized in that water collection sheet (4) is 200~300mm to the distance at air flotation pool (1) end.
CN 200410043641 2004-06-23 2004-06-23 High efficiency air-float solid and liquid separator Expired - Fee Related CN1280205C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200410043641 CN1280205C (en) 2004-06-23 2004-06-23 High efficiency air-float solid and liquid separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200410043641 CN1280205C (en) 2004-06-23 2004-06-23 High efficiency air-float solid and liquid separator

Publications (2)

Publication Number Publication Date
CN1594115A CN1594115A (en) 2005-03-16
CN1280205C true CN1280205C (en) 2006-10-18

Family

ID=34665350

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200410043641 Expired - Fee Related CN1280205C (en) 2004-06-23 2004-06-23 High efficiency air-float solid and liquid separator

Country Status (1)

Country Link
CN (1) CN1280205C (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107986369A (en) * 2017-12-15 2018-05-04 上海巴安水务股份有限公司 A kind of novel water distribution device suitable for flotation tank
CN110589922B (en) * 2019-09-20 2024-06-14 无锡海拓环保装备科技有限公司 Flotation rectifying air floatation tank
CN110589923A (en) * 2019-09-23 2019-12-20 无锡海拓环保装备科技有限公司 Cocurrent flow flotation solid-liquid separation tank
CN112239244B (en) * 2020-05-07 2024-09-10 无锡中申环境保护设备有限公司 Air floatation tank and entrainment air floatation device

Also Published As

Publication number Publication date
CN1594115A (en) 2005-03-16

Similar Documents

Publication Publication Date Title
US20130292326A1 (en) Fast settling concentration tank for sewage in gangue
CN204138447U (en) A kind of aeration horizontal-flow grit chamber
CN202482103U (en) Ultrasonic air floatation oil removing device
CN101193826B (en) Anaerobic purification device
CN103990302B (en) A kind of radial-flow type sedimentation device
CN103638699B (en) Composite precipitation tank
CN1280205C (en) High efficiency air-float solid and liquid separator
CN1898001A (en) Precipitation tank
KR930001217B1 (en) High concentration organic waste water treating method and apparatus
CN1264587C (en) Precipitation pneumatically supported serial composite solid-liquid separator
CN201684443U (en) Secondary flocculation inclined plate and tube sediment device
CN202191737U (en) High-speed coagulative precipitation tank
CN207581572U (en) High-efficient sedimentation tank
CN105749592B (en) A kind of connectivity structure between treatment tank
CN205556392U (en) Sewage treatment equipment
CN201268598Y (en) Unpowered oil-water clarifier
CN2481391Y (en) High-efficiency secondary stream settler
CN208394821U (en) A kind of integration air-float sewage disposal device
CN211273682U (en) Novel high-efficient precipitator of whirl swash plate
CN205948444U (en) A efficient sedimentation tank for sewage treatment
CN2122673U (en) Sidewise flow sloping palte sink-float solid-liquid separator
CN111392910A (en) Floating and sinking integrated treatment system
CN204293914U (en) A kind of radial-flow type sedimentation device
CN220502728U (en) Improved generation air supporting pond
CN211471048U (en) Sled dress formula normal water processing system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20061018

Termination date: 20120623