CN101830533A - V-shaped air floating filter with deslagging function - Google Patents
V-shaped air floating filter with deslagging function Download PDFInfo
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- CN101830533A CN101830533A CN201010187064A CN201010187064A CN101830533A CN 101830533 A CN101830533 A CN 101830533A CN 201010187064 A CN201010187064 A CN 201010187064A CN 201010187064 A CN201010187064 A CN 201010187064A CN 101830533 A CN101830533 A CN 101830533A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 234
- 238000005188 flotation Methods 0.000 claims abstract description 104
- 239000000463 material Substances 0.000 claims abstract description 53
- 239000002893 slag Substances 0.000 claims abstract description 36
- 238000005192 partition Methods 0.000 claims abstract description 35
- 238000009826 distribution Methods 0.000 claims abstract description 24
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- 238000000926 separation method Methods 0.000 claims abstract description 22
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- 230000000712 assembly Effects 0.000 claims description 4
- 238000000429 assembly Methods 0.000 claims description 4
- 210000005056 cell body Anatomy 0.000 claims 8
- 238000009300 dissolved air flotation Methods 0.000 claims 3
- 238000007790 scraping Methods 0.000 claims 3
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- 235000008733 Citrus aurantifolia Nutrition 0.000 claims 1
- 235000011941 Tilia x europaea Nutrition 0.000 claims 1
- 239000004571 lime Substances 0.000 claims 1
- 238000011001 backwashing Methods 0.000 abstract description 14
- 238000000746 purification Methods 0.000 abstract description 5
- 230000009466 transformation Effects 0.000 abstract description 2
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Abstract
一种具有排渣功能的V型气浮滤池,涉及一种净水厂水质处理构筑物,具体涉及一种V型气浮滤池。本发明是为了解决现有的气浮滤池中滤池水力负荷不易与气浮池的较高水力负荷进行搭配,反冲洗中浮渣层的掉渣不能被彻底冲洗掉,还出现滤料层跑料或滤料参混现象的问题。本发明的四个V型气浮滤池主体对称设置于进水分配槽的两侧,隔墙将每个滤池的上方分隔为气浮接触区和气浮分离区,每个滤池内由下至上设置有气水室、滤板支撑架、滤板、长柄滤头、砾石承托层和石英砂均质滤料,排渣槽设置于与隔墙相对的侧壁上,刮渣机通过轨道与滤池的侧壁连接,微气泡发生装置与溶气水输送主管相连。本发明尤其适用于对已采用V型滤池的老水厂的升级改造。
A V-shaped air flotation filter with slag discharge function relates to a water quality treatment structure of a water purification plant, in particular to a V-shaped air flotation filter. The present invention aims to solve the problem that the hydraulic load of the filter in the existing air flotation filter is not easy to match with the higher hydraulic load of the air flotation tank, the scum in the scum layer during backwashing cannot be completely washed away, and the filter material layer runs away. The problem of mixed phenomenon of material or filter material. The main bodies of the four V-shaped air flotation filters of the present invention are symmetrically arranged on both sides of the water inlet distribution tank, and the partition wall divides the top of each filter into an air flotation contact area and an air flotation separation area. The air-water chamber, filter plate support frame, filter plate, long handle filter head, gravel support layer and quartz sand homogeneous filter material are arranged on the top, and the slag discharge tank is set on the side wall opposite to the partition wall, and the slag scraper passes through The track is connected with the side wall of the filter tank, and the microbubble generating device is connected with the main pipe for conveying the dissolved air water. The invention is especially suitable for the upgrading and transformation of the old water works which have adopted the V-shaped filter tank.
Description
技术领域technical field
本发明涉及一种净水厂水质处理构筑物,具体涉及一种具有排渣功能的V型气浮滤池。The invention relates to a water quality treatment structure of a water purification plant, in particular to a V-shaped air flotation filter with slag discharge function.
背景技术Background technique
目前,净水厂在处理高藻水或低温低浊水时,往往采用先气浮后过滤的技术。现有将气浮池与移动罩滤池、普通快滤池或翻板阀滤池组合成一体化的水处理构筑物,由于这些不同形式的气浮滤池自身结构及运行方式的特点,都存在各自的不足之处。气浮移动罩滤池,当其移动罩运行对滤池进行反洗时,对水面浮渣层扰动特别大,影响浮渣稳定,产生的掉渣阻塞滤池滤料层,降低产水水力负荷及出水水质,缩短反冲洗周期,为保证气浮池的分离效果还需额外增加滤池滤层以上水深,同时由于移动罩滤池本身水力负荷较小,不易与气浮池的较高水力负荷进行搭配;气浮普通快滤池,由于普通快滤池的水力负荷较低,不易与气浮池的较高水力负荷进行搭配,使其占地面积较大,基建投资高,水面浮渣层产生的掉渣落到滤料上,阻塞滤池滤料层,由于只能用水进行反洗,反洗强度低时,不能把滤料层上的气浮浮渣层掉渣反洗干净,反洗强度较大时,既浪费了大量的反洗水,而且其采用中央排水槽排水又易引起滤料层跑料,为保证气浮池的分离效果也需额外增加滤池滤料层以上水深;气浮翻板阀滤池,水层表面的浮渣层易产生掉渣掉至滤池滤料层,阻塞甚至穿透滤料层,使出水水质恶化,反洗周期缩短,虽然采用气水联合反洗,但由于反洗废水采用序批式排水,滤料层的滤料会大量跑料至滤料进水槽,而浮渣层掉渣还不能被彻底地冲洗掉,其采用的多层滤料,反洗时经常出现滤料参混现象,严重影响滤池的正常过滤效果。At present, when water purification plants deal with high-algae water or low-temperature and low-turbidity water, they often adopt the technology of first air flotation and then filtration. Existing water treatment structures that combine air flotation tanks with mobile hood filters, ordinary fast filters or flap valve filters, due to the characteristics of the structures and operating modes of these different forms of air flotation filters, each has its own characteristics. inadequacies. Air floatation mobile cover filter, when the mobile cover operates to backwash the filter, the disturbance to the scum layer on the water surface is particularly large, affecting the stability of the scum, and the resulting slag blocks the filter material layer of the filter, reducing the hydraulic load of the produced water In order to ensure the separation effect of the air flotation tank, it is necessary to increase the water depth above the filter layer of the filter. At the same time, because the hydraulic load of the mobile cover filter itself is small, it is not easy to match with the higher hydraulic load of the air flotation tank. ; Ordinary air flotation fast filter, because the hydraulic load of ordinary fast filter is low, it is not easy to match with the higher hydraulic load of the air flotation tank, so that it occupies a large area, high investment in infrastructure, and the drop caused by the scum layer on the water surface The slag falls on the filter material and blocks the filter material layer of the filter. Since only water can be used for backwashing, when the backwashing intensity is low, the air-floated scum layer on the filter material layer cannot be backwashed clean. When it is large, a lot of backwash water is wasted, and the central drainage tank is used to drain water and it is easy to cause the filter layer to run out of material. In order to ensure the separation effect of the air flotation tank, it is necessary to increase the water depth above the filter layer of the filter; In the plate valve filter, the scum layer on the surface of the water layer is easy to produce scum and fall to the filter material layer of the filter, blocking or even penetrating the filter material layer, deteriorating the effluent water quality and shortening the backwash cycle. Although the air-water combined backwash is used, However, due to the sequential batch drainage of backwash wastewater, a large amount of filter material in the filter material layer will run to the filter material inlet tank, and the scum in the scum layer cannot be completely washed away. The phenomenon of filter material mixing often occurs during washing, which seriously affects the normal filtering effect of the filter tank.
发明内容Contents of the invention
本发明的目的是为了解决现有的气浮滤池中,滤池水力负荷不易与气浮池的较高水力负荷进行搭配,占地面积大,反冲洗时,浮渣层的掉渣不能被彻底冲洗掉,还出现滤料层跑料或滤料参混现象的问题,进而提供了一种具有排渣功能的V型气浮滤池。The purpose of the present invention is to solve the problem that in the existing air flotation filter, the hydraulic load of the filter is not easy to match with the higher hydraulic load of the air flotation tank, the floor area is large, and the scum in the scum layer cannot be completely removed during backwashing. If it is washed away, the problem of material running or mixing in the filter material layer also occurs, and then a V-shaped air flotation filter with slag discharge function is provided.
本发明的技术方案是:本发明包括四个V型气浮滤池主体,进水管、静态混合器、进水气动隔膜阀、薄壁堰、V型滤池进水分配槽、溶气水输送管组件、溶气水输送主管、V型槽、排水阀、石英砂均质滤料层、砾石承托层、滤板、滤板支撑架、长柄滤头、H形槽体、气水室、滤板支撑架、滤板、多个长柄滤头、砾石承托层、石英砂均质滤料层、水封井、出水堰、清水管、反冲洗进气管和反冲洗进水管,它还包括刮渣机、排渣槽、排渣管和微气泡发生装置,所述四个面积相等且横截面均为“凸”形的V型气浮滤池主体对称设置于V型滤池进水分配槽的两侧,每两个对称的V型气浮滤池主体的“几”形挡墙的凸部相对,V型气浮滤池主体内的隔墙设置在“几”形挡墙和与其相对的侧壁之间,在“几”形挡墙和隔墙之间设有薄壁堰,每个“几”形挡墙中部的下方各设置两个进水气动隔膜阀,每个V型气浮滤池主体的中部在垂直于隔墙的方向设置有贯通的H形槽体,H形槽体的中部隔板将H形槽体分隔为上部的水槽和下部的中央气水分配槽,H形槽体的中部隔板上靠近隔墙的一端向下倾斜并与隔墙底部的排水阀连接,每个V型气浮滤池主体内由下至上设置有气水室、滤板支撑架、滤板、多个长柄滤头、砾石承托层和石英砂均质滤料层,石英砂均质滤料层的上表面位于H形槽体的上端面的下方,所述多个长柄滤头均布并垂直穿过滤板和滤板支撑架,H形槽体与其两侧的气水室之间的隔墙的上、下分别设置有横向均布并贯通的配气孔和水方孔,每个V型气浮滤池主体内相对的两个侧壁的上方设置有与H形槽体平行的V型槽,V型槽下部均布有V型槽扫洗进水孔,每个V型气浮滤池主体内的石英砂均质滤料层的上方为气浮分离区,多个垂直并列设置的溶气水管项部相通成为溶气水输送管组件,溶气水输送管组件设置于每个V型气浮滤池主体的隔墙与薄壁堰之间,四个溶气水输送管组件均与一个溶气水输送主管相通,溶气水输送管组件构成气浮接触区,气浮接触区与V型气浮滤池主体的底面留有进水空隙,气浮接触区通过隔墙上方的进水口与气浮分离区相通,静态混合器设置于进水管内,进水管与V型滤池进水分配槽的一端连通,反冲洗进气管和反冲洗进水管的一端分别接入每个V型气浮滤池主体的中央气水分配槽,反冲洗进气管的另一端与鼓风机房相连,反冲洗进水管的另一端与水泵相连,两个水封井对称设置于V型气浮滤池外侧、水封井的两侧通过管路分别与相邻的两个V型气浮滤池主体的中央气水分配槽相通,两个出水堰垂直设置于水封井内,清水管设置于两个出水堰之间的水封井的侧壁上,所述排渣槽设置于V型气浮滤池主体内与隔墙相对的侧壁上,排渣槽垂直于V型槽并位于其上方,排渣槽的底部通过排渣管与V型气浮滤池池外相通,刮渣机通过两侧的轨道与V型气浮滤池主体的侧壁连接,刮渣机平行于排渣槽并位于其上,所述微气泡发生装置与溶气水输送主管相连。The technical solution of the present invention is: the present invention includes four V-shaped air flotation filter main bodies, water inlet pipes, static mixers, water inlet pneumatic diaphragm valves, thin-walled weirs, V-shaped filter inlet distribution tanks, dissolved air water delivery Pipe assembly, main pipe for dissolved air and water delivery, V-shaped groove, drain valve, quartz sand homogeneous filter material layer, gravel support layer, filter plate, filter plate support frame, long handle filter head, H-shaped tank body, air-water chamber , filter plate support frame, filter plate, multiple long-handle filter heads, gravel support layer, quartz sand homogeneous filter material layer, water seal well, water outlet weir, clean water pipe, backwash inlet pipe and backwash water inlet pipe, it It also includes a slag scraper, a slag discharge tank, a slag discharge pipe and a micro-bubble generating device. The main bodies of the four V-shaped air flotation filters with equal areas and "convex" cross-sections are symmetrically arranged in the inlet of the V-shaped filter. On both sides of the water distribution tank, the convex parts of the "several"-shaped retaining walls of the main body of every two symmetrical V-shaped air flotation filters face each other, and the partition walls in the main body of the V-shaped air flotation filter are set on the "several"-shaped retaining walls Between the "several" shaped retaining wall and the partition wall, there are thin-walled weirs between the opposite side wall, and two water inlet pneumatic diaphragm valves are set under the middle of each "several" shaped retaining wall, each The middle part of the main body of the V-shaped air flotation filter is provided with a through H-shaped tank in the direction perpendicular to the partition wall. The middle partition of the H-shaped tank separates the H-shaped tank into the upper water tank and the lower central air-water distribution. The end of the middle partition of the H-shaped tank, which is close to the partition wall, is inclined downward and connected to the drain valve at the bottom of the partition wall. Each V-shaped air flotation filter body is equipped with an air-water chamber and a filter plate from bottom to top. Support frame, filter plate, multiple long handle filter heads, gravel support layer and quartz sand homogeneous filter material layer, the upper surface of the quartz sand homogeneous filter material layer is located below the upper end surface of the H-shaped tank body, the multiple Two long-handle filter heads are evenly distributed and vertically pass through the filter plate and the filter plate support frame, and the upper and lower partition walls between the H-shaped tank body and the air-water chambers on both sides are respectively provided with horizontally uniform and penetrating air distribution holes and Water square holes, V-shaped grooves parallel to the H-shaped groove body are arranged above the two opposite side walls in the main body of each V-shaped air flotation filter, and V-shaped grooves are evenly distributed with V-shaped grooves sweeping water inlet holes at the lower part of the V-shaped grooves , the top of the quartz sand homogeneous filter material layer in the main body of each V-shaped air flotation filter is the air flotation separation zone, and the tops of a plurality of vertically juxtaposed dissolved air water pipes are connected to form a dissolved air water delivery pipe assembly, and the dissolved air water The conveying pipe assembly is arranged between the partition wall and the thin-walled weir of each V-shaped air flotation filter main body, and the four dissolved air water conveying pipe assemblies communicate with one dissolved air water conveying main pipe. Flotation contact area, the air flotation contact area and the bottom surface of the main body of the V-shaped air flotation filter leave a water inlet gap, the air flotation contact area communicates with the air flotation separation area through the water inlet above the partition wall, and the static mixer is set in the water inlet pipe , the water inlet pipe is connected to one end of the water inlet distribution tank of the V-shaped filter. The other end of the water sealing well is connected to the blower room, and the other end of the backwashing water inlet pipe is connected to the water pump. Two water sealing wells are symmetrically arranged outside the V-shaped air flotation filter, and the two sides of the water sealing well are respectively connected to the adjacent two through pipelines. The central air-water distribution tanks of the main body of the V-shaped air flotation filter are connected, and the two outlet weirs are vertically arranged in the water seal well Inside, the clear water pipe is set on the side wall of the water seal well between the two outlet weirs, and the slag discharge tank is set on the side wall opposite to the partition wall in the main body of the V-shaped air flotation filter, and the slag discharge tank is perpendicular to the The V-shaped groove is located above it. The bottom of the slag discharge tank communicates with the outside of the V-shaped air flotation filter through the slag discharge pipe. The slag machine is parallel to the slag discharge tank and located on it, and the microbubble generating device is connected with the main pipe for dissolving air water delivery.
本发明具有以下有益效果:第一,V型滤池水力负荷较高,可以与较高水力负荷的气浮池很好的搭配使用并能充分发挥气浮池的高水力负荷的优势,解决了气浮池与V型滤池的高程衔接问题,并进一步降低构筑物占地面积,保证出水水质的安全稳定,同时采用气液两相流混合溶气泵产生微气泡的方式,达到提高产水水力负荷;第二,V型滤池滤料层以上水深能达到2.0m~2.5m,能很好地保证气浮处理的分离效果,不需额外增加滤料层以上水深,这点特别适用于采用V型滤池的老水厂进行气浮滤池的改造;第三,V型滤池采用均值滤料,滤料层较厚,反洗时不会有滤料参混的现象,有效地保证出水水质;第四,V型滤池采用气水联合反洗再加其独特的表面扫洗,一方面可以节约大量反洗水量,另一方面一直持续的表面扫洗可以将水面气浮浮渣层在滤料层上产生的掉渣扫洗干净,避免了气浮浮渣层掉渣而引起的穿孔集水管/板的阻塞问题,保证了滤池的反洗效果,延长滤池反洗周期,保证滤池出水水质;第五,通过加设V型槽进水闸阀可以实现对气浮-过滤和过滤两种工艺间的切换,以适应净水厂待处理水水质一年中交替出现高藻、高浊及低温低浊等水质类型的变化,使其适用范围增强。本发明简化了生产管理流程,优化净水工艺流程,减少了投资和运行费用,节约成本。The present invention has the following beneficial effects: First, the V-shaped filter has a relatively high hydraulic load, can be used in conjunction with an air flotation tank with a relatively high hydraulic load, and can give full play to the advantages of the high hydraulic load of the air flotation tank, solving the problem of the air flotation tank The problem of connecting with the elevation of the V-shaped filter tank, and further reducing the occupied area of the structure, ensures the safety and stability of the effluent water quality, and at the same time adopts the method of gas-liquid two-phase flow mixed dissolved air pump to generate micro-bubbles to increase the hydraulic load of water production; the second , the water depth above the filter material layer of the V-shaped filter can reach 2.0m~2.5m, which can well ensure the separation effect of the air flotation treatment, and there is no need to increase the water depth above the filter material layer, which is especially suitable for the V-shaped filter. The old water plant carried out the transformation of the air flotation filter; thirdly, the V-type filter adopts the average filter material, the filter material layer is thicker, and there will be no mixing of the filter material during backwashing, effectively ensuring the quality of the effluent water; Fourth, the V-shaped filter adopts air-water combined backwashing plus its unique surface sweeping. On the one hand, it can save a lot of backwashing water. On the other hand, the continuous surface sweeping can remove the air-floated scum layer on the water surface The slag generated on the layer is swept and cleaned, avoiding the blockage of the perforated water collection pipe/plate caused by the scum layer of the air flotation scum layer, ensuring the backwashing effect of the filter, prolonging the backwashing cycle of the filter, and ensuring that the filter Outlet water quality; Fifth, by adding a V-groove inlet gate valve, the switch between air flotation-filtration and filtration can be realized, so as to adapt to the high algae and high turbidity of the water to be treated in the water purification plant alternately throughout the year Changes in water quality types such as low temperature and low turbidity increase the scope of application. The invention simplifies the production management process, optimizes the water purification process, reduces investment and operating costs, and saves costs.
附图说明Description of drawings
图1为本发明的平面图(图示的四个V型气浮滤池主体为由不同高度水平剖切的示意图);图2为图1的A-A剖面图;图3为图1的B-B剖面图;图4是本发明过滤工况示意图;图5是本发明反冲洗工况示意图;图6为本发明中水封井的结构示意图;图7为图6的F-F剖面图;图8为图3中本发明中V型槽的局部放大图E;图9为本发明的微气泡发生装置结构示意图。Fig. 1 is a plan view of the present invention (the four V-type air flotation filter main bodies shown in the figure are schematic diagrams cut horizontally by different heights); Fig. 2 is the A-A sectional view of Fig. 1; Fig. 3 is the B-B sectional view of Fig. 1 ; Fig. 4 is a schematic diagram of the filtration working condition of the present invention; Fig. 5 is a schematic diagram of a backwashing working condition of the present invention; Fig. 6 is a structural schematic diagram of a water-sealed well in the present invention; Fig. 7 is a F-F sectional view of Fig. 6; Fig. 8 is Fig. 3 Partial enlarged view E of the V-shaped groove in the present invention; FIG. 9 is a schematic structural diagram of the microbubble generating device of the present invention.
具体实施方式Detailed ways
具体实施方式一:结合图1至图9说明本实施方式的具有排渣功能的V型气浮滤池,它包括四个V型气浮滤池主体11,进水管1、静态混合器2、进水气动隔膜阀11-16-1、薄壁堰4、V型滤池进水分配槽6、溶气水输送管组件7、溶气水输送主管7-1、V型槽11-1、排水阀11-1-3、石英砂均质滤料层11-2、砾石承托层11-3、滤板11-4、滤板支撑架11-5、长柄滤头11-6、H形槽体11-7、气水室11-14、滤板支撑架11-5、滤板11-4、多个长柄滤头11-6、砾石承托层11-3、石英砂均质滤料层11-2、水封井8、出水堰8-1、清水管8-2、反冲洗进气管12和反冲洗进水管13,它还包括刮渣机11-15、排渣槽11-8、排渣管11-9和微气泡发生装置10,所述四个面积相等且横截面均为“凸”形的V型气浮滤池主体11对称设置于V型滤池进水分配槽6的两侧,每两个对称的V型气浮滤池主体11的“几”形挡墙11-16的凸部相对,V型气浮滤池主体11内的隔墙11-17设置在“几”形挡墙11-16和与其相对的侧壁之间,在“几”形挡墙11-16和隔墙11-17之间设有薄壁堰4,每个“几”形挡墙11-16中部的下方各设置两个进水气动隔膜阀11-16-1,每个V型气浮滤池主体11的中部在垂直于隔墙11-17的方向设置有贯通的H形槽体11-7,H形槽体11-7的中部隔板11-7-3将H形槽体11-7分隔为上部的水槽11-7-1和下部的中央气水分配槽11-7-2,H形槽体11-7的中部隔板11-7-3上靠近隔墙11-17的一端向下倾斜并与隔墙11-17底部的排水阀11-1-3连接,每个V型气浮滤池主体11内由下至上设置有气水室11-14、滤板支撑架11-5、滤板11-4、多个长柄滤头11-6、砾石承托层11-3和石英砂均质滤料层11-2,石英砂均质滤料层11-2的上表面位于H形槽体11-7的上端面的下方,所述多个长柄滤头11-6均布并垂直穿过滤板11-4和滤板支撑架11-5,H形槽体11-7与其两侧的气水室11-14之间的隔墙的上、下分别设置有横向均布并贯通的配气孔11-11和水方孔11-12,每个V型气浮滤池主体11内相对的两个侧壁的上方设置有与H形槽体11-7平行的V型槽11-1,V型槽11-1下部均布有V型槽扫洗进水孔11-1-2,每个V型气浮滤池主体11内的石英砂均质滤料层11-2的上方为气浮分离区b,多个垂直并列设置的溶气水管项部相通成为溶气水输送管组件7,溶气水输送管组件7设置于每个V型气浮滤池主体11的隔墙11-17与薄壁堰4之间,四个溶气水输送管组件7均与一个溶气水输送主管7-1相通,溶气水输送管组件7构成气浮接触区a,气浮接触区a与V型气浮滤池主体11的底面留有进水空隙,气浮接触区a通过隔墙11-17上方的进水口11-17-1与气浮分离区b相通,静态混合器2设置于进水管1内,进水管1与V型滤池进水分配槽6的一端连通,反冲洗进气管12和反冲洗进水管13的一端分别接入每个V型气浮滤池主体11的中央气水分配槽11-7-2,反冲洗进气管12的另一端与鼓风机相连,反冲洗进水管13的另一端与水泵相连,两个水封井8对称设置于V型气浮滤池外侧、水封井8的两侧通过管路分别与相邻的两个V型气浮滤池主体11的中央气水分配槽11-7-2相通,两个出水堰8-1垂直设置于水封井8内,清水管8-2设置于两个出水堰8-1之间的水封井8的侧壁上,所述排渣槽11-8设置于V型气浮滤池主体11内与隔墙11-17相对的侧壁上,排渣槽11-8垂直于V型槽11-1并位于其上方,排渣槽11-8的底部通过排渣管11-9与V型气浮滤池池外相通,刮渣机11-15通过两侧的轨道与V型气浮滤池主体11的侧壁连接,刮渣机11-15平行于排渣槽11-8并位于其上,所述微气泡发生装置10与溶气水输送主管7-1相连。气浮接触区a底部的空隙为待处理水的入口,在气浮接触区a待处理水与微气泡顺流接触形成泡絮体,气浮接触区a的出口设在其上方,泡絮体溢流出水进入位于V型气浮滤池主体11上部的气浮分离区b,刮渣机11-15与数控设备相连。利用石英砂均质滤料层11-2较大的水头损失,可以使气浮出水水量及水质均匀稳定,节省了集水穿孔管,避免了泡絮体沉降阻塞穿孔管。V型气浮滤池过滤时采用恒水位过滤,有利于浮渣的稳定,采用气水联合反冲洗同时伴有表面扫洗,一直持续的表面扫洗有利于对落渣到滤料表面的浮渣进行冲洗,避免传统气浮滤池可能存在的表层滤料容易阻塞的问题,有效延长滤池的反冲洗周期,节省水厂自用水量。同时,石英砂均质滤料层11-2上高达2m的有效水深作为气浮分离区b可以较好地保障气浮分离效果,为了进一步提高V型气浮滤池的水力负荷,可以在增加石英砂均质滤料层的基础上增加滤料层上的有效水深。另外,由于滤池滤料层过水水头损失高达1.5m~2.0m,避免了采用穿孔集水管/板及气浮浮渣层掉渣而引起的穿孔集水管/板的阻塞问题。Embodiment 1: The V-type air flotation filter with slagging function of this embodiment is illustrated in conjunction with Fig. 1 to Fig. 9, which includes four V-type air flotation filter
具体实施方式二:结合图9说明本实施方式的具有排渣功能的V型气浮滤池,所述微气泡发生装置10由气液两相流溶气泵10-3、气液分离罐10-4、真空表10-2、压力表10-6、减压阀10-7、排气阀10-5和排水阀10-1组成,输水管依次通过排水阀10-1和真空表10-2与气液两相流溶气泵10-3连接,气液分离罐10-4的一端与气液两相流溶气泵10-3连接,气液分离罐10-4的另一端通过压力表10-6与减压阀10-7连接,气液分离罐10-4的上方设置有排气阀10-5。微气泡发生装置10的溶气部分是气液两相流溶气泵10-3,为避免大气泡产生,在气液两相流溶气泵10-3后加气液分离罐10-4,并经减压阀10-7减压产生微气泡,以产生足够数量小而均匀的微气泡,还可以节省使用价格昂贵且容易阻塞的微气泡释放器,避免了对溶气释放器装置进行检修,便于日常操作及设备的运行管理。本实施方式的其它组成与连接关系与具体实施方式一相同。Specific embodiment two: The V-type air flotation filter with slagging function of this embodiment is illustrated in conjunction with FIG. 4. Vacuum gauge 10-2, pressure gauge 10-6, pressure reducing valve 10-7, exhaust valve 10-5 and drain valve 10-1, the water pipe passes through drain valve 10-1 and vacuum gauge 10-2 in turn It is connected with the gas-liquid two-phase flow dissolved air pump 10-3, one end of the gas-liquid separation tank 10-4 is connected with the gas-liquid two-phase flow dissolved air pump 10-3, and the other end of the gas-liquid separation tank 10-4 passes through the pressure gauge 10- 6 is connected with the decompression valve 10-7, and the top of the gas-liquid separation tank 10-4 is provided with an exhaust valve 10-5. The dissolved gas part of the
具体实施方式三:结合图1和图2说明本实施方式的具有排渣功能的V型气浮滤池,它还包括折流板5,所述折流板5设置于溶气水输送管组件7与薄壁堰4之间,折流板5的上部固定于V型气浮滤池主体11顶板的内壁上,折流板5的下部与V型气浮滤池主体11的底板之间留有进水空隙。折流板5用于改变待处理水的流向。本实施方式的其它组成与连接关系与具体实施方式一或二相同。Specific Embodiment Three: The V-shaped air flotation filter with slagging function of this embodiment is described in conjunction with Fig. 1 and Fig. 2, which also includes a
具体实施方式四:结合图1至图5说明本实施方式的具有排渣功能的V型气浮滤池,它还包括V型槽进水闸阀11-1-1,所述隔墙11-17上与V型槽11-1相接处设有V型槽进水口11-1-4,V型槽进水口11-1-4位于V型槽11-1上端面的上方,V型槽进水口11-1-4的外侧设有V型槽进水闸阀11-1-1。通过控制V型槽进水闸阀11-1-1的开启,实现对气浮-过滤和过滤两种处理工艺间的切换,以适应待处理水水质的交替变化。本实施方式的其它组成与连接关系与具体实施方式一、二或三相同。Specific Embodiment Four: The V-type air flotation filter with slagging function of this embodiment is described in conjunction with Fig. 1 to Fig. 5, which also includes a V-shaped groove inlet valve 11-1-1, and the partition wall 11-17 A V-shaped groove water inlet 11-1-4 is arranged at the junction with the V-shaped groove 11-1, and the V-shaped groove water inlet 11-1-4 is located above the upper end surface of the V-shaped groove 11-1. The outside of the water port 11-1-4 is provided with a V-shaped groove water inlet gate valve 11-1-1. By controlling the opening of the V-groove water inlet valve 11-1-1, the switching between the two treatment processes of air flotation-filtration and filtration is realized, so as to adapt to the alternate change of the water quality to be treated. The other components and connections of this embodiment are the same as those of
本发明的工作原理:高藻水或低温低浊水气浮过滤时,先关闭V型槽进水闸阀11-1-1,进水管1的一端与沉淀池相连,其另一端与V型滤池进水分配槽6相通,经进水管1中静态混合器2混合的待处理水由V型滤池进水分配槽6,待处理水先后经进水气动隔膜阀11-16-1、薄壁堰4和折流板5均匀分配进入四个V型气浮滤池主体11,由气液两相流溶气泵10-3和气液分离罐10-4形成的溶气水经减压阀10-7减压产生足量小而均匀的微气泡,产生的微气泡在气浮接触区a底部与进入的待处理水碰撞接触形成泡絮体,泡絮体向上流经气浮接触区a出口进入气浮分离区b,泡絮体在气浮分离区b分离上升至表面形成浮渣,形成的浮渣由设在V型气浮滤池主体11顶部的刮渣机11-15刮至排渣槽11-8并经排渣管11-9定期排出,气浮处理后的水经V型气浮滤池主体11的石英砂均质滤料层11-2、砾石承托层11-3、滤板11-4和多个长柄滤头11-6流入滤池底部的气水室11-14,再经过水方孔11-12汇入中央气水分配槽11-7-2,最后经由水封井8、出水堰8-1、清水管8-2流至下一处理构筑物或供用户使用。Working principle of the present invention: when high-algae water or low-temperature and low-turbidity water is air flotation filtered, first close the V-shaped groove water inlet gate valve 11-1-1, one end of the
当待处理水水质不适合采用气浮处理时,比如高浊水的过滤,将待处理水经混凝、沉淀后出水由进水管1进入V型滤池进水分配槽6,先打开V型槽进水闸阀11-1-1,不启动微气泡发生装置10,经混合絮凝的待处理水再经气动隔膜阀11-16-1、薄壁堰4和折流板5均匀分配进入到四个V型气浮滤池主体11的气浮接触区a,再经由V型槽进水闸阀11-1-1进入V型槽11-1,再通过V型槽11-1底部的V型槽扫洗进水孔11-1-2出水和槽顶溢流均匀进入滤池,而后通过石英砂均质滤料层11-2、砾石承托层11-3、滤板11-4和多个长柄滤头11-6流入滤池底部的气水室11-14,再经过水方孔11-12汇入中央气水分配槽11-7-2,最后经由水封井8、出水堰8-1、清水管8-2流至下一处理构筑物或供用户使用。When the quality of the water to be treated is not suitable for air flotation treatment, such as the filtration of highly turbid water, the water to be treated is coagulated and precipitated and then the effluent enters the water inlet distribution tank 6 of the V-shaped filter through the water inlet pipe 1, and the V-shaped tank is first opened to enter The sluice valve 11-1-1 does not start the micro-bubble generating device 10, and the water to be treated after mixing and flocculation is evenly distributed into the four V The air flotation contact area a of the main body 11 of the type air flotation filter enters the V-shaped groove 11-1 through the V-shaped groove inlet valve 11-1-1, and then sweeps through the V-shaped groove at the bottom of the V-shaped groove 11-1 The water outlet from the water inlet hole 11-1-2 and the overflow from the top of the tank evenly enter the filter tank, and then pass through the quartz sand homogeneous filter material layer 11-2, gravel support layer 11-3, filter plate 11-4 and multiple long handles The filter head 11-6 flows into the air-water chamber 11-14 at the bottom of the filter, then flows into the central air-water distribution tank 11-7-2 through the water square hole 11-12, and finally passes through the water seal well 8 and the outlet weir 8-1 , The clean water pipe 8-2 flows to the next processing structure or for users to use.
V型气浮滤池反冲洗前,为防止反冲洗对浮渣的破坏,用刮渣机11-15对滤池表面的浮渣进行刮除,同时调小进水气动隔膜阀11-16的开启度,使进水量恰好满足V型槽11-1底部V型槽扫洗进水孔11-1-2所需水量,打开V型槽进水闸阀11-1-1使一部分待处理水由V型槽扫洗进水孔11-1-2进入滤池,然后开启排水阀11-1-3将滤料表面的水经过排水槽11-7排出直至滤池水面与排水槽11-7的顶端相平。V型气浮滤池反冲洗过程如下:第一步,启动鼓风机,打开进气阀,空气经由反冲洗进气管12、中央气水分配槽11-7-2的配气孔11-11均匀进入V型气浮滤池主体11的底部,由多个长柄滤头11-6喷出,喷出的气体将滤料层表面的杂质剪切擦洗下来并悬浮于滤料层表面;另外通过V型槽11-1底部V型槽扫洗进水孔11-1-2继续向滤池进水,在滤料层表面产生的横向水流形成表面扫洗,横向水流将杂质推向排水槽11-7-1,同时启动水泵,打开反冲洗进水阀,此时空气和水同时经由反冲洗进水管13进入中央气水分配槽11-7-2,再分别经过配气孔11-11和水方孔11-12均匀进入气水室11-14,再经过多个长柄滤头11-6进入滤料层,使滤料得到进一步冲洗,同时,表面扫洗仍继续进行;第二步,关闭反冲洗进气阀12-1,停止气冲,单独用水再反冲洗几分钟,加上一直持续的表面扫洗,最后将悬浮于滤料层表面的杂质全部冲入排水槽11-7-1。其中气冲强度15L/(s·m2),水冲强度为6L/(s·m2),横向扫洗强度为1.8L/(s·m2)。Before the backwashing of the V-type air flotation filter, in order to prevent the damage to the scum caused by the backwashing, use the scum scraper 11-15 to scrape off the scum on the surface of the filter, and at the same time turn down the water inlet pneumatic diaphragm valve 11-16 The degree of opening is such that the water intake just satisfies the amount of water required by the V-shaped groove sweeping water inlet 11-1-2 at the bottom of the V-shaped groove 11-1, and the V-shaped groove inlet valve 11-1-1 is opened so that a part of the water to be treated is The V-shaped groove sweeps and washes the water inlet 11-1-2 into the filter tank, and then opens the drain valve 11-1-3 to discharge the water on the surface of the filter material through the drain tank 11-7 until the filter tank water surface and the drain tank 11-7 Flat top. The backwash process of the V-type air flotation filter is as follows: first step, start the blower, open the intake valve, and the air enters the V evenly through the backwash intake pipe 12 and the air distribution holes 11-11 of the central air-water distribution tank 11-7-2 The bottom of the main body 11 of the type air flotation filter is sprayed by a plurality of long handle filter heads 11-6, and the jetted gas shears and scrubs the impurities on the surface of the filter material layer and suspends them on the surface of the filter material layer; The V-groove sweeping and washing inlet hole 11-1-2 at the bottom of the tank 11-1 continues to feed water into the filter tank, and the horizontal water flow generated on the surface of the filter material layer forms a surface sweeping, and the horizontal water flow pushes impurities to the drainage tank 11-7 -1, start the water pump at the same time, open the backwash water inlet valve, at this time, air and water enter the central air-water distribution tank 11-7-2 through the backwash water inlet pipe 13 at the same time, and then pass through the air distribution hole 11-11 and the water square hole respectively 11-12 evenly enters the air-water chamber 11-14, and then enters the filter material layer through a plurality of long-handled filter heads 11-6, so that the filter material is further washed, and at the same time, the surface cleaning continues; the second step is to close the reverse filter. Flush the intake valve 12-1, stop the air flushing, backwash with water alone for a few minutes, add continuous surface cleaning, and finally flush all the impurities suspended on the surface of the filter material layer into the drainage tank 11-7-1. Among them, the air flushing intensity is 15L/(s·m 2 ), the water flushing intensity is 6L/(s·m 2 ), and the lateral sweeping intensity is 1.8L/(s·m 2 ).
规模为7万m3/d的具有排渣功能的V型气浮滤池,气浮池接触区a内待处理水的上升流速为20mm/s,气水接触时间为1.5min,气浮分离区b内待处理水的向下流速为3mm/s,泡絮体与水的分离时间为15min,滤速10.8m/h,反冲洗周期48h,四个V型气浮滤池主体11的长分别为3.5m,宽分别为9.7m,占地面积共33.95m2,取滤后水作为气液两相流溶气泵10-3的溶气进水,回流比在8%~12%范围内调节,其中,石英砂的粒径为0.95~1.35mm,不均匀系数K80=1.0~1.3。V-shaped air flotation filter with slag discharge function with a scale of 70,000 m 3 /d. The rising flow rate of the water to be treated in the contact area a of the air flotation tank is 20mm/s, the air-water contact time is 1.5min, and the air flotation separation area The downward flow velocity of the water to be treated in b is 3mm/s, the separation time of foam floc and water is 15min, the filtration rate is 10.8m/h, the backwash cycle is 48h, and the lengths of the four V-shaped air flotation filter
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CN109513245A (en) * | 2019-01-18 | 2019-03-26 | 浙江联池水务设备股份有限公司 | High-precision exempts from the stainless steel filter tank of filter |
CN109626709A (en) * | 2018-11-13 | 2019-04-16 | 湖北汇环保科技有限公司 | River water body comprehensive purifying processing system |
CN111569518A (en) * | 2020-05-15 | 2020-08-25 | 营口德瑞化工有限公司 | Liquid ammonia filter equipment |
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