Nothing Special   »   [go: up one dir, main page]

CN102228759A - Sewage filter - Google Patents

Sewage filter Download PDF

Info

Publication number
CN102228759A
CN102228759A CN2011101734530A CN201110173453A CN102228759A CN 102228759 A CN102228759 A CN 102228759A CN 2011101734530 A CN2011101734530 A CN 2011101734530A CN 201110173453 A CN201110173453 A CN 201110173453A CN 102228759 A CN102228759 A CN 102228759A
Authority
CN
China
Prior art keywords
filter
sedimentation
vortex
shape
cover
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.)
Granted
Application number
CN2011101734530A
Other languages
Chinese (zh)
Other versions
CN102228759B (en
Inventor
韦志锋
兰夕盈
曾小波
曾东健
卢志文
周燕
梁洁
肖林虎
赵鸿雁
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.)
Chongqing University of Science and Technology
Original Assignee
Chongqing University of Science and Technology
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 Chongqing University of Science and Technology filed Critical Chongqing University of Science and Technology
Priority to CN2011101734530A priority Critical patent/CN102228759B/en
Publication of CN102228759A publication Critical patent/CN102228759A/en
Application granted granted Critical
Publication of CN102228759B publication Critical patent/CN102228759B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0039Settling tanks provided with contact surfaces, e.g. baffles, particles
    • B01D21/0045Plurality of essentially parallel plates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0039Settling tanks provided with contact surfaces, e.g. baffles, particles
    • B01D21/0069Making of contact surfaces, structural details, materials therefor
    • B01D21/0075Contact surfaces having surface features

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

一种综合浅池理论、动态混凝、加速絮凝原理和斜板技术,沉淀能力强,水力条件好,沉淀效率高,沉淀效果稳定,提高竖流式沉淀池表面负荷,有效解决了传统斜板(管)沉淀技术容易堵塞问题,维护方便的污水过滤器。污水过滤器利用等距排列的过滤罩及其上的众多通孔结构将运动原水分割细划,保证水流均匀分布,同时利用流体在障碍物后或者凹陷处形成高速旋转漩涡的特性,使原水在过滤罩体板孔后缘产生稳定的漩涡。在漩涡的卷吸作用下,原水中的非流体物质聚集到漩涡中心,在涡核中不断接触、碰撞,黏合,发生絮凝反应。絮体经旋转流体的反复挤压作用,其质量和尺寸越来越大,最后以大质量颗粒沉降。表面积聚的薄泥层,依靠重力作用沿罩体斜面滑落,沉入集泥斗。从而达到了去除原水中悬浮物质,清洁水体的目的。污水过滤器可以绕转轴轴线转动。通过快速反复左右转动,形成强烈湍动的剪切流,即可对斜板造成高速冲刷作用,清除可能的淤积、堵塞非常方便。

Figure 201110173453

A comprehensive shallow pool theory, dynamic coagulation, accelerated flocculation principle and inclined plate technology, strong sedimentation capacity, good hydraulic conditions, high sedimentation efficiency, stable sedimentation effect, increase the surface load of the vertical flow sedimentation tank, and effectively solve the problem of traditional inclined plate (Pipe) Sedimentation technology is easy to clog the problem, and the sewage filter is easy to maintain. The sewage filter utilizes equidistantly arranged filter covers and numerous through-hole structures to divide the moving raw water into fine sections to ensure uniform distribution of the water flow. A stable vortex is generated at the rear edge of the filter housing plate hole. Under the entrainment effect of the vortex, the non-fluid substances in the raw water gather to the center of the vortex, and continuously contact, collide, and bond in the vortex core, and flocculation reactions occur. The flocs are repeatedly extruded by the rotating fluid, and their mass and size become larger and larger, and finally settle with large-mass particles. The thin mud layer accumulated on the surface slides down along the slope of the cover body by gravity and sinks into the mud collecting bucket. Thereby, the purpose of removing suspended matter in the raw water and cleaning the water body is achieved. The sewage filter can rotate around the shaft axis. By rotating left and right quickly and repeatedly, a strong turbulent shear flow is formed, which can cause high-speed scouring of the inclined plate, and it is very convenient to remove possible deposits and blockages.

Figure 201110173453

Description

污水过滤器sewage filter

技术领域 technical field

本发明涉及一种能够加快污水处理的沉淀过程,澄清水体,提高污水处理效果的污水过滤器。The invention relates to a sewage filter capable of accelerating the sedimentation process of sewage treatment, clarifying water bodies and improving the sewage treatment effect.

背景技术 Background technique

竖流式沉淀池是一种重要的污水处理构筑物,具有占地面积小,排泥方便和接触絮凝和污泥悬浮层拦截等许多优点,非常适用于中小型污水处理系统。但它池深度大,对水量冲击负荷和水温变化适应能力不强,常常出现配水、集水不均等现象,沉淀效果不稳定;池径不宜过大。The vertical flow sedimentation tank is an important sewage treatment structure, which has many advantages such as small footprint, convenient sludge discharge, contact flocculation and sludge suspension layer interception, and is very suitable for small and medium-sized sewage treatment systems. However, its depth is large, and its adaptability to water impact load and water temperature change is not strong. There are often phenomena such as water distribution and water collection, and the sedimentation effect is unstable; the pool diameter should not be too large.

斜板、斜管式沉淀池的优点是沉淀面积大,水力负荷高,效率高,为其他沉淀池的一倍以上,占地少,节省土建的投资,运行稳定、安全可靠,但斜板和斜管极易堵塞,影响沉淀,造成维护管理工作困难,也极大地大限制了它的使用范围。The advantages of inclined plate and inclined tube sedimentation tanks are large sedimentation area, high hydraulic load, high efficiency, which is more than double that of other sedimentation tanks, less land occupation, saving civil engineering investment, stable operation, safety and reliability, but inclined plates and The inclined tube is very easy to block, which affects the sedimentation, makes maintenance and management difficult, and greatly limits its scope of use.

发明内容 Contents of the invention

为了解决竖流式沉淀池池深过大,对水量冲击负荷和水温变化适应能力不强以及传统斜板(管)容易发生污泥黏附、堵塞,影响沉淀效果的缺陷,污水过滤器综合了浅池理论、动态混凝、加速絮凝原理和斜板技术,利用等距排列的过滤罩体及其上的众多通孔结构将运动原水分割细划,保证水流均匀分布;同时利用流体在障碍物后或者凹陷处形成高速旋转漩涡的特性,使原水在过滤罩通孔后缘产生稳定的漩涡。在漩涡的卷吸作用下,原水中的非流体物质聚集到漩涡中心,在涡核中不断接触、碰撞,黏合,发生絮凝反应。絮体经旋转流体的反复挤压作用,其质量和尺寸越来越大,最后以大质量颗粒沉降。表面积聚的薄泥层,依靠重力作用沿罩体斜面滑落,沉入集泥斗。从而达到了去除原水中悬浮物质,清洁水体的目的。In order to solve the defects that the depth of the vertical flow sedimentation tank is too large, the adaptability to the impact load of water volume and the change of water temperature is not strong, and the traditional inclined plate (pipe) is prone to sludge adhesion and clogging, which affects the sedimentation effect, the sewage filter integrates the shallow Pool theory, dynamic coagulation, accelerated flocculation principle and inclined plate technology, use equidistantly arranged filter covers and numerous through-hole structures to divide and divide the moving raw water to ensure uniform distribution of water flow; at the same time, use fluid to flow behind obstacles Or the characteristics of the high-speed rotating vortex formed in the depression make the raw water generate a stable vortex at the rear edge of the through hole of the filter cover. Under the entrainment effect of the vortex, the non-fluid substances in the raw water gather to the center of the vortex, and continuously contact, collide, and bond in the vortex core, and flocculation reactions occur. The flocs are repeatedly extruded by the rotating fluid, and their mass and size become larger and larger, and finally settle with large-mass particles. The thin mud layer accumulated on the surface slides down along the slope of the cover body by gravity and sinks into the mud collecting bucket. Thereby, the purpose of removing suspended matter in raw water and cleaning the water body is achieved.

多层等距周期排列的结构,使絮凝反应、浅池沉淀过程反复循环进行,悬浮物质不断地得以去除,净化效率大大提高。The structure of multi-layer equidistant periodic arrangement makes the flocculation reaction and shallow pool sedimentation process repeat cycle, the suspended matter is continuously removed, and the purification efficiency is greatly improved.

污水过滤器可以绕转轴轴线转动。通过快速反复左右转动,形成强烈湍动的剪切流,即可对过滤罩体造成高速冲刷作用,清除可能的淤积、堵塞非常方便。The sewage filter can rotate around the shaft axis. By rotating left and right quickly and repeatedly, a strong turbulent shear flow is formed, which can cause high-speed scouring of the filter cover body, and it is very convenient to remove possible deposits and blockages.

本发明解决其技术问题所采用的技术方案:The technical solution adopted by the present invention to solve its technical problems:

若干个形状相同,结构相同、罩体中空过滤罩沿轴向平行排列,中间贯以转轴连接并固定;过滤罩数量不少于1个,相邻过滤罩有间距;罩面上开有规则排列通孔;通孔在径向均匀排列成行,沿周向等距分布。Several of the same shape and structure, the hollow filter covers of the cover body are arranged in parallel in the axial direction, and the middle is connected and fixed by a rotating shaft; the number of filter covers is not less than 1, and there is a distance between adjacent filter covers; there are regular arrangements on the cover surface Through holes; the through holes are evenly arranged in rows in the radial direction and distributed equidistantly along the circumferential direction.

过滤罩形状是圆台状,或球台状、或者球冠状。The shape of the filter cover is a truncated cone, or a ball table, or a spherical crown.

过滤罩罩体中空,无下底面,圆台状和球台状过滤罩的上底面是轮毂结构。The filter cover body is hollow without a lower bottom surface, and the upper bottom surface of the circular truncated and ball table shaped filter covers is a hub structure.

转轴是空心轴结构。The rotating shaft is a hollow shaft structure.

过滤罩通孔形状是三角形、菱形、矩形、蝴蝶形、圆形、椭圆、四边形、五边形、六边形、多边形或者对称曲线图形。The shape of the through hole of the filter cover is triangle, rhombus, rectangle, butterfly, circle, ellipse, quadrilateral, pentagon, hexagon, polygon or symmetrical curve figure.

相邻过滤罩通孔与罩板交错布置。The through holes of the adjacent filter covers are alternately arranged with the cover plates.

过滤罩由若干带有轮毂和扇形罩面的组件交错叠加组合构成。The filter cover is composed of a number of components with hubs and fan-shaped covers that are staggered and combined.

本发明的有益效果是,絮凝反应充分,出水悬浮物SS大大降低;提高单位占地面积的沉淀面积,水力条件好,沉淀效率高,沉淀效果稳定;可以有效减小池深;提高池体表面负荷;减少占地面积;不积泥,不堵塞,清除积淤方便,彻底克服了传统斜板(管)沉淀技术容易堵塞问题。The beneficial effect of the present invention is that the flocculation reaction is sufficient, the SS of the effluent suspended matter is greatly reduced; the sedimentation area per unit area is increased, the hydraulic condition is good, the sedimentation efficiency is high, and the sedimentation effect is stable; the pool depth can be effectively reduced; the surface load of the pool body can be increased ; Reduce floor space; no mud, no clogging, easy to remove silt, completely overcome the problem of easy clogging of traditional inclined plate (pipe) sedimentation technology.

附图说明 Description of drawings

下面结合附图和实施例对发明进一步说明。The invention will be further described below in conjunction with the accompanying drawings and embodiments.

图1是本发明在竖流式沉淀池中应用的轴向剖视图。Fig. 1 is an axial sectional view of the application of the present invention in a vertical flow sedimentation tank.

图2是6层过滤罩结构的本发明立体图。Fig. 2 is a perspective view of the present invention with a 6-layer filter cover structure.

图3是6层过滤罩结构的本发明轴向剖视图。Fig. 3 is an axial sectional view of the present invention with a 6-layer filter housing structure.

图4是1层过滤罩结构的本发明立体图。Fig. 4 is a perspective view of the present invention with a one-layer filter housing structure.

图5是单独过滤罩立体图。Fig. 5 is a perspective view of a separate filter housing.

图6是单独过滤罩轴向剖视图。Fig. 6 is an axial sectional view of a separate filter housing.

图7是由轮毂和140°扇形罩面构成的组件的立体图。Fig. 7 is a perspective view of an assembly composed of a hub and a 140° fan-shaped cover.

图8是由图7所示的组件三个组合而成的一个过滤罩的立体图。Fig. 8 is a perspective view of a filter housing composed of three components shown in Fig. 7 .

图9是由图7所示的组件三个组合而成的一个过滤罩和转轴的立体图。Fig. 9 is a perspective view of a filter housing and a rotating shaft formed by combining three components shown in Fig. 7 .

图中:1.池体2.污水3.中心进水管4.反射板5.出水孔6.出水堰7.出水槽8.沉淀污物9.贮泥斗10.排泥管11.过滤罩12.转轴13.通孔14.基板15.轮毂16.扇形罩面In the figure: 1. Pool body 2. Sewage 3. Central water inlet pipe 4. Reflector plate 5. Water outlet hole 6. Water outlet weir 7. Water outlet tank 8. Settling dirt 9. Mud storage bucket 10. Mud discharge pipe 11. Filter cover 12. Shaft 13. Through hole 14. Substrate 15. Hub 16. Fan-shaped cover

具体实施方式 Detailed ways

在图1所示实施例中,本发明套在中心污水进水管外,由支架支撑。污水由设在池中心的进水管自上而下进入池内,管下伞形挡板使废水水平均匀扩散,受罩体空间限制,原水聚集罩面下,通过均匀分布的通孔向上流动。由于孔板效应,原水在过滤罩体通孔后缘产生漩涡。在漩涡的卷吸作用下,原水中的非流体物质聚集到漩涡中心,在涡核中不断接触、碰撞,黏合,发生絮凝反应。絮体经旋转流体的反复挤压作用,其质量和尺寸越来越大,最后以大质量颗粒沉降。所以,罩面上的通孔便构造成了一个个紊流涡旋絮凝微反应器。当通孔产生的微涡旋尺度与矾花颗粒尺度相近或相等时絮凝反应最充分,絮凝效果最佳;涡旋数量越多,涡旋强度越大,污物分离得越彻底,矾花也越密实。In the embodiment shown in Fig. 1, the present invention is sleeved outside the central sewage inlet pipe and supported by a bracket. Sewage enters the pool from top to bottom through the water inlet pipe located in the center of the pool. The umbrella-shaped baffle under the tube makes the waste water spread evenly horizontally. Limited by the space of the cover, the raw water gathers under the cover and flows upward through the evenly distributed through holes. Due to the orifice effect, the raw water generates a vortex at the rear edge of the through hole of the filter cover. Under the entrainment effect of the vortex, the non-fluid substances in the raw water gather to the center of the vortex, and continuously contact, collide, and bond in the vortex core, and flocculation reactions occur. The flocs are repeatedly extruded by the rotating fluid, and their mass and size become larger and larger, and finally settle with large-mass particles. Therefore, the through holes on the cover surface are constructed into turbulent flow vortex flocculation microreactors one by one. When the size of the micro-vortex produced by the through hole is similar or equal to the particle size of the alum flower, the flocculation reaction is the most sufficient, and the flocculation effect is the best; the more the number of vortex, the greater the vortex intensity, the more thoroughly the dirt is separated, and the alum flower is also The denser it is.

由于实行相邻罩体通孔与罩板交错布置,处于通孔流道中心不易被漩涡卷吸的颗粒正面与顶层罩板发生碰撞。由于固体壁面附近的边界层粘性大,同时受罩壁形状阻碍,运动颗粒与罩板实现了碰撞静止,即颗粒上浮运动速度瞬时降低为零。失速颗粒或者粘附在罩壁构成污泥悬浮层,等待拦截不断运动而来的颗粒,经过不断碰撞,黏合,卷扫、网捕,最后聚成大质量密实絮团沉降。部份颗粒随绕流变向避开正面罩壁运动,其上升动能降低。能量降低的颗粒则极易在下一段流程中被卷吸或拦截过滤。Due to the staggered arrangement of the through holes and the cover plates of the adjacent cover bodies, the particles in the center of the flow channel of the through holes, which are not easy to be entrained by the vortex, collide with the top layer of the cover plate. Due to the high viscosity of the boundary layer near the solid wall, and being hindered by the shape of the cover wall, the moving particles and the cover plate have achieved a stationary collision, that is, the speed of the particles' floating motion has been reduced to zero instantaneously. Stall particles or adhere to the cover wall to form a sludge suspension layer, waiting to intercept the moving particles, after continuous collision, bonding, sweeping, netting, and finally gather into a large mass of dense flocs to settle. Part of the particles move away from the front mask wall as the flow changes direction, and their upward kinetic energy decreases. Particles with reduced energy are easily entrained or intercepted and filtered in the next stage of the process.

两罩体形成的狭长空间构成一个浅层沉淀池,原水和沉降的沉泥在各沉淀浅层相互运动并分离。The long and narrow space formed by the two covers constitutes a shallow sedimentation tank, and the raw water and the settled sediment move and separate from each other in each shallow sedimentation layer.

罩体表面沉淀积聚的薄泥层,依靠重力作用沿罩体斜面滑落,沉入集泥斗。The thin mud layer deposited and accumulated on the surface of the cover body slides down along the slope of the cover body by gravity and sinks into the mud collecting bucket.

多层等距周期排列的过滤罩结构,使絮凝反应、浅池沉淀过程反复循环进行,原水中悬浮物质不断地得以去除,净化效率大大提高。The multi-layer equidistant periodic arrangement of the filter cover structure makes the flocculation reaction and the shallow pool sedimentation process repeat cycle, the suspended matter in the raw water is continuously removed, and the purification efficiency is greatly improved.

污水过滤器可以绕转轴轴线转动。在维护时,通过快速地转动转轴,即可在通孔和罩面形成强烈湍动的剪切流,对过滤罩体造成高速冲刷作用,清除可能的淤积、堵塞非常方便。The sewage filter can rotate around the shaft axis. During maintenance, by rotating the rotating shaft quickly, a strong turbulent shear flow can be formed in the through hole and the cover surface, causing high-speed scouring of the filter cover body, and it is very convenient to remove possible deposits and blockages.

Claims (7)

1. effluent filter, it is characterized in that: several shapes are identical, and structure is identical, cover body hollow filter mantle is arranged in parallel vertically, and the centre is passed through with rotating shaft and is connected and fixing; Filter mantle quantity is no less than 1, and adjacent filtration is covered with spacing; Have regularly arranged through hole on the cover; Through hole is evenly distributed embarking on journey radially, along circumferentially being equally spaced.
2. effluent filter as claimed in claim 1 is characterized in that: described filter mantle shape is round table-like, or billiard table shape or spherical crown shape.
3. effluent filter as claimed in claim 1 is characterized in that: described filter mantle cover body hollow, and no bottom surface, round table-like and upper bottom surface billiard table shape filter mantle is a wheel hub structure.
4. effluent filter as claimed in claim 1 is characterized in that: described rotating shaft is a hollow shaft structure.
5. effluent filter as claimed in claim 1 is characterized in that: described filter mantle shape of through holes is triangle, rhombus, rectangle, butterfly shape, circle, ellipse, quadrangle, pentagon, hexagon, polygon or symmetrical curve figure.
6. effluent filter as claimed in claim 1 is characterized in that: described adjacent filter mantle through hole and cover plate interlaced arrangement.
7. effluent filter as claimed in claim 1 is characterized in that: described filter mantle is made of some staggered stack combinations of assembly that have wheel hub and fan-shaped cover.
CN2011101734530A 2011-06-26 2011-06-26 Sewage filter Expired - Fee Related CN102228759B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011101734530A CN102228759B (en) 2011-06-26 2011-06-26 Sewage filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011101734530A CN102228759B (en) 2011-06-26 2011-06-26 Sewage filter

Publications (2)

Publication Number Publication Date
CN102228759A true CN102228759A (en) 2011-11-02
CN102228759B CN102228759B (en) 2013-03-13

Family

ID=44841389

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011101734530A Expired - Fee Related CN102228759B (en) 2011-06-26 2011-06-26 Sewage filter

Country Status (1)

Country Link
CN (1) CN102228759B (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103100241A (en) * 2012-12-03 2013-05-15 韦志锋 Eccentric-type arc-shaped movable slant board
CN103818983A (en) * 2012-11-19 2014-05-28 山东海吉雅环保设备有限公司 Oil-sludge-water separation device
CN107413149A (en) * 2017-06-26 2017-12-01 哥乐巴环保科技(上海)有限公司 A kind of MDF dries the modified technique and processing system of tail gas biochemical processing method
CN107473460A (en) * 2017-10-16 2017-12-15 江苏绿尚环保科技有限公司 A kind of industrial sewage purification device
CN110436539A (en) * 2019-08-16 2019-11-12 龙游卡伊环保科技有限公司 A kind of self intercepting system for sewage treatment
CN110871388A (en) * 2019-11-25 2020-03-10 株洲联信金属有限公司 Multi-wire saw with good heat dissipation function
CN112194286A (en) * 2020-10-06 2021-01-08 北京怡盛原环保科技有限公司 Sewage purification tank and sewage purification method
CN112426754A (en) * 2020-11-13 2021-03-02 江苏通用环保集团有限公司 High-efficient sedimentation tank
CN112717480A (en) * 2020-12-04 2021-04-30 周美蓉 Bury formula sewage integration treatment facility
CN117088480A (en) * 2023-07-25 2023-11-21 南通问鼎金属制品有限公司 Purifying and recycling equipment for sewage treatment and recycling method thereof
CN118993204A (en) * 2024-10-21 2024-11-22 广州弘鑫环保科技有限公司 Multistage sewage treatment equipment and application method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4325825A (en) * 1979-04-26 1982-04-20 Hoechst Aktiengesellschaft Separator
CN1069677A (en) * 1991-08-21 1993-03-10 寿技王株式会社 Sedimentation-type centrifuge
CN1390151A (en) * 1999-09-22 2003-01-08 南方水利服务有限公司 Separator for liquid suspension
CN1541130A (en) * 2001-08-10 2004-10-27 Method for separation of blood plasma particles from blood plasma suspension
US20080257819A1 (en) * 2007-04-18 2008-10-23 Tarves Robert J Dual walled dynamic phase separator
CN202155108U (en) * 2011-06-26 2012-03-07 韦志锋 Sewage filter

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4325825A (en) * 1979-04-26 1982-04-20 Hoechst Aktiengesellschaft Separator
CN1069677A (en) * 1991-08-21 1993-03-10 寿技王株式会社 Sedimentation-type centrifuge
CN1390151A (en) * 1999-09-22 2003-01-08 南方水利服务有限公司 Separator for liquid suspension
CN1541130A (en) * 2001-08-10 2004-10-27 Method for separation of blood plasma particles from blood plasma suspension
US20080257819A1 (en) * 2007-04-18 2008-10-23 Tarves Robert J Dual walled dynamic phase separator
CN202155108U (en) * 2011-06-26 2012-03-07 韦志锋 Sewage filter

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103818983A (en) * 2012-11-19 2014-05-28 山东海吉雅环保设备有限公司 Oil-sludge-water separation device
CN103100241A (en) * 2012-12-03 2013-05-15 韦志锋 Eccentric-type arc-shaped movable slant board
CN103100241B (en) * 2012-12-03 2015-05-13 韦志锋 Eccentric-type arc-shaped movable slant board
CN107413149A (en) * 2017-06-26 2017-12-01 哥乐巴环保科技(上海)有限公司 A kind of MDF dries the modified technique and processing system of tail gas biochemical processing method
CN107473460A (en) * 2017-10-16 2017-12-15 江苏绿尚环保科技有限公司 A kind of industrial sewage purification device
CN110436539A (en) * 2019-08-16 2019-11-12 龙游卡伊环保科技有限公司 A kind of self intercepting system for sewage treatment
CN110871388A (en) * 2019-11-25 2020-03-10 株洲联信金属有限公司 Multi-wire saw with good heat dissipation function
CN110871388B (en) * 2019-11-25 2020-10-27 株洲联信金属有限公司 Multi-wire saw with good heat dissipation function
CN112194286A (en) * 2020-10-06 2021-01-08 北京怡盛原环保科技有限公司 Sewage purification tank and sewage purification method
CN112194286B (en) * 2020-10-06 2021-08-24 南昌市自来水工程有限责任公司 Sewage purification tank and sewage purification method
CN112426754A (en) * 2020-11-13 2021-03-02 江苏通用环保集团有限公司 High-efficient sedimentation tank
CN112426754B (en) * 2020-11-13 2022-06-24 江苏通用环保集团有限公司 High-efficient sedimentation tank
CN112717480A (en) * 2020-12-04 2021-04-30 周美蓉 Bury formula sewage integration treatment facility
CN112717480B (en) * 2020-12-04 2022-05-27 中瑞工程设计院有限公司 Bury formula sewage integration treatment facility
CN117088480A (en) * 2023-07-25 2023-11-21 南通问鼎金属制品有限公司 Purifying and recycling equipment for sewage treatment and recycling method thereof
CN117088480B (en) * 2023-07-25 2024-04-19 南通问鼎金属制品有限公司 Purifying and recycling equipment for sewage treatment and recycling method thereof
CN118993204A (en) * 2024-10-21 2024-11-22 广州弘鑫环保科技有限公司 Multistage sewage treatment equipment and application method thereof
CN118993204B (en) * 2024-10-21 2025-01-07 广州弘鑫环保科技有限公司 Multi-stage sewage treatment equipment and use method thereof

Also Published As

Publication number Publication date
CN102228759B (en) 2013-03-13

Similar Documents

Publication Publication Date Title
CN102228759B (en) Sewage filter
CN107162239A (en) Eddy flow agglomerated air floatation removes oil column
CN103100241B (en) Eccentric-type arc-shaped movable slant board
CN104402087B (en) A kind of magnetic eddy filter
CN206008236U (en) A kind of vertical sedimentation basin
CN108525353A (en) A kind of settling tank efficiently separated
CN210698952U (en) Silt whirl deposits device suitable for sewage purification handles
CN105749619A (en) Inclined plate filter cloth filtering device and control method
CN106731047B (en) A grill type sand settling device
CN202155108U (en) Sewage filter
CN108238662A (en) Reinforced cyclone sand setting tank
CN213221092U (en) High-efficient whirl deposits water purifier
CN206454320U (en) The efficient clarifying reaction device of fine suspension in a kind of processing sewage
CN113045172A (en) Self-rotating sedimentation type sludge thickener
CN105084568B (en) Oil-contained waste water treatment device and handling process
CN112239256A (en) A large flow circulating granulation fluidized bed high-speed solid-liquid separation equipment
CN101254363A (en) A radial flow sedimentation tank with multi-layer sedimentation plates
CN112239258A (en) A peripheral drive type large flow circulating granulation fluidized bed high-speed solid-liquid separation equipment
CN107867745B (en) RJM integrated process water treatment equipment
CN216986421U (en) Inclined plate sedimentation tank with back flush
CN109354246A (en) A kind of high-concentration sewage rapid treatment device and treatment method thereof
CN204170462U (en) A kind of circular settling tank
CN203862069U (en) Imperforate atomizing tangential swirl dust remover
CN208516998U (en) A kind of vertical-flow dissolved gas floatator
CN108786193B (en) Shunting type grit chamber

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: 20130313

Termination date: 20130626