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Sand filter

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other coals. Ilmenite and garnet are heavy compared to sand. Garnet consists of several minerals, causing a shifting red colour. Ilmenite is an oxide of iron and titanium. GAC can be used in the process of adsorption and filtration at the same time. These materials can be used both alone, or combined with other media. But the filtering layers will be always arranged by density, heavier compounds will be settled in the bottom, while the lighter ones will be located on top. Different combinations give different filter classification and also different porosity throughout the filter, which is translated into different pressure drop. A very common arrangement for these filers is composed of: anthracite on top, sand and garnet, with a support of gravel at the bottom. The depth of these filters is normally between 0.6-1 m, above 1 m the pressure drop rises sharply and less than 0.6 m reduces the thickness of each filtering layer, thus reducing its efficienciy. Nomal operating flux and pressure drop are between 3-7 gpm/ft2 and 3-7 psi. When pressure drop increases above 10 psi, a backwash operation ins needed, which consist of reversing the flow (water goes upwards) in order to remove the particles trapped in the filtering media, and this will exit from the top of the filter with the backwash water. Common for the backwash is around 3 times the normal filtering flux (must be high enough to lift the filtering media to remove the particles trapped in it). Monomedia is a one layered filter, commonly consisting of sand and is today replaced by newer technology. Deep-bed monomedia is also a one layered filter which consist of either anthracite or GAC. The deep-bed monomedia filter is used when there is a consistent water quality and this gives a longer run time. Dual media (two layered) often contain a sand layer in the bottom with an anthracite or GAC layer on top. Trimedia or mixed media is a filter with three layers. Trimedia often have garnet or ilmenite in the bottom layer, sand in the middle and anthracite at the top.
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the bed is backwashed to remove the accumulated particles. For a pressurized rapid sand bed filter this occurs when the pressure drop is around 0.5 bar. The backwash fluid is pumped backwards through the bed until it is fluidized and has expanded by up to about 30% (the sand grains start to mix and as they rub together they drive off the particulate solids). The smaller particulate solids are washed away with the backwash fluid and captured usually in a settling tank. The fluid flow required to fluidize the bed is typically 3 to 10 m/m/hr but not run for long (a few minutes). Small amounts of sand can be lost in the backwashing process and the bed may need to be topped up periodically.
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flows through the filter medium and the effluent drains through the drainage system in the lower part. Large process plants have also a system implemented to evenly distribute the raw water to the filter. In addition, a distribution system controlling the air flow is usually included. It allows a constant air and water distribution and prevents too high water flows in specific areas. A typical grain distribution exits due to the frequent backwashing. Grains with smaller diameter are dominant in the upper part of the sand layer while coarse grain dominates in the lower parts.
79: 287:, however, the biggest difference between slow and rapid sand filter, is that the top layer of sand is biologically active, as microbial communities are introduced to the system. The recommended and usual depth of the filter is 0.9 to 1.5 meters. Microbial layer is formed within 10–20 days from the start of the operation. During the process of filtration, raw water can percolate through the porous sand medium, stopping and trapping organic material, bacteria, viruses and cysts such as 241: 308:, which is for slow sand filters defined to be 10 NTU (Nephelometric Turbidity Units). Slow sand filters are a good option for limited budget operations as the filtration is not using any chemicals and requires little or no mechanical assistance. However, because of a continuous growing population in communities, slow sand filters are being replaced for rapid sand filters, mostly due to the running period length. 131:. Sand bed filters are an example of a granular loose media depth filter. They are usually used to separate small amounts (<10 parts per million or <10 g per cubic metre) of fine solids (<100 micrometres) from aqueous solutions. In addition, they are usually used to purify the fluid rather than capture the solids as a valuable material. Therefore they find most of their uses in liquid effluent ( 20: 522:
reduces also the volume of the effluent. If a certain amount of water has to be delivered to e.g. a community, this water loss needs to be considered. In addition, backwashing waste needs to be treated or properly discarded. From the chemical perspective, varying raw water qualities and changes in the temperature effect, already at the entrance to the plant, the efficiency of the treatment process.
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specialist applications other sizes may be specified. Larger feed particles (>100 micrometres) will tend to block the pores of the bed and turn it into a surface filter that blinds rapidly. Larger sand grains can be used to overcome this problem, but if significant amounts of large solids are in the feed they need to be removed upstream of the sand bed filter by a process such as settling.
232:, water (and air) is pumped backwards through the filter system. Backwash water may partially be reinjected in front of the filter process and generated sewage needs to be discarded. The backwashing time is determined by either the turbidity value behind the filter, which must not exceed a set threshold, or by the head loss across the filter medium, which must also not exceed a certain value. 172:
particulate solids may become more attractive or repel addition particulate solids. This can occur if by adhering to the sand grain the particulate loses surface charge and becomes attractive to additional particulates or the opposite and surface charge is retained repelling further particulates from the sand grain.
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The main limitations of this technology would be related to the clogging, that is, the obstruction of the filter media, which requires a significant amount of water to carry out the backflush operation and the use of chemicals in the pretreatment. Furthermore, slow sand filters usually require larger
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The build-up of particulate solids causes an increase in the pressure lost across the bed for a given flow rate. For a gravity fed bed when the pressure available is constant, the flow rate will fall. When the pressure loss or flow is unacceptable and the filter is not working effectively any longer,
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Filters that have different filtering layers, are called mixed bed filters or multimedia filters. Sand is a common filter material, but anthracite, granular activated carbon (GAC), garnet and ilmenite are also common filter materials. Anthracite is a harder material and has less volatile compared to
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This filter type will capture particles down to very small sizes, and does not have a true cut off size below which particles will always pass. The shape of the filter particle size-efficiency curve is a U-shape with high rates of particle capture for the smallest and largest particles with a dip in
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At the beginning of a new filter run, the filter efficiency increases simultaneously with the number of captured particles in the medium. This process is called filter ripening. During filter ripening the effluent might not meet quality criteria and must be reinjected at previous steps in the plant.
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They can be operated either with upward flowing fluids or downward flowing fluids the latter being much more usual. For downward flowing devices the fluid can flow under pressure or by gravity alone. Pressure sand bed filters tend to be used in industrial applications and often referred to as rapid
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after a period in use. Slow sand filters are then scraped (see above) while rapid sand filters are backwashed or pressure washed to remove the floc. This backwash water is run into settling tanks so that the floc can settle out and it is then disposed of as waste material. The supernatant water is
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Rapid pressure sand bed filters are typically operated with a feed pressure of 2 to 5 bar(a) (28 to 70 psi(a)). The pressure drop across a clean sand bed is usually very low. It builds as particulate solids are captured on the bed. Particulate solids are not captured uniformly with depth, more are
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The sketch illustrates the general structure of a rapid pressure sand filter. The filter sand takes up most space of the chamber. It sits either on a nozzle floor or on top of a drainage system which allows the filtered water to exit. The pre-treated raw water enters the filter chamber on the top,
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The continuously backflushing or upflow sand filter is the newest operating regime. The clearest difference with respect to the previous ones, is that the water to be filtered is fed from the bottom and the filtered water is obtained at the top. This reverse flow allows the backwash process to be
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if the surface charge of the sand is of the same sign (positive or negative) as that of the particulate solid. Furthermore, it is possible to dislodge captured particulates although they may be re-captured at a greater depth within the bed. Finally, a sand grain that is already contaminated with
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In the process of water treatment, one should be aware of certain factors that might cause serious problems if not treated properly. Aforementioned processes such as filter ripening and backwashing influence not only the water quality but also the time needed for the full treatment. Backwashing
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Smaller sand grains provide more surface area and therefore a higher decontamination of the inlet water, but it also requires more pumping energy to drive the fluid through the bed. A compromise is that most rapid pressure sand bed filters use grains in the range 0.6 to 1.2 mm although for
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One of the advantages of sand filters is that they are useful for different applications. Moreover, the different types of operation modes: rapid, slow and Upflow, allow some flexibility to adapt the filtration method to the necessities and requirements of the users. Sand filters allow a high
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Considerable uncertainty is involved regarding models used to construct sand filters. This is due to mathematical assumptions that have to be made such as all grains being spherical. The spherical shape affects the interpretation of the size since the diameter is different for spherical and
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removal from 90% to >99% (depending on the strains), taste and odour without the need for chemical aids. Sand filters can, apart from being used in water treatment plants, be used for water purification in singular households as they use materials which are available for most people.
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Sand bed filters work by providing the particulate solids with many opportunities to be captured on the surface of a sand grain. As fluid flows through the porous sand along a tortuous route, the particulates come close to sand grains. They can be captured by one of several mechanisms:
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All of these methods are used extensively in the water industry throughout the world. The first three in the list above require the use of flocculant chemicals to work effectively. Slow sand filters produce high-quality water without the use of chemical aids.
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Sectors where sand filtration is implemented include drinking water production, swimming pools, car washes, groundwater treatment, RWZI, slaughterhouses, fruit and vegetable processing industry, drinks, food industry, surface treatment of metals, …
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Guidance on the design of rapid sand bed filters suggests that they should be operated with a maximum flow rate of 9 m/m/hr (220 US gal/ft/hr). Using the required throughput and the maximum flow rate, the required area of the bed can be calculated.
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efficiency for color and microorganisms removal, and as they are very simple, operating costs are very low. What is more, its simplicity makes the automation of the processes easier, thus requiring less human intervention.
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land areas compared to the rapid flow, especially if the raw water is highly contaminated. However, despite these limitations, they offer much more capabilities and that is why they are extensively used in the industry.
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Final purification of wastewater produced in the production of iron, steel and non-ferro alloys. Sand filtration can be preceded by processes like precipitation/sedimentation, coagulation/flocculation/sedimentation and
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and is used to mechanically remove the dried out particles on the filter. However, this process can also be done under water, depending on the individual system. Another limiting factor for the water being treated is
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1=raw water, 2=filtered water, 3=tank, 4=outlet flushing water, 5=inlet flushing water, 6=retraction line, 7=scavenging air, 8=injector, 9=supporting layer, 10=filter sand, 11=flushing funnel, 12=ventilation
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The final key design point is to be sure that the fluid is properly distributed across the bed and that there are no preferred fluid paths where the sand may be washed away and the filter be compromised.
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as a final polishing stage. In these filters the sand traps residual suspended material and bacteria and provides a physical matrix for bacterial decomposition of nitrogenous material, including
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integrated in the filtration process, thus decreasing the amount of rinse water to be used and reducing cleaning time. The maximum loading is about 5.4 lps/m2 with a constant head loss of 0.6 m.
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In some applications it is necessary to pre-treat the effluent flowing into a sand bed to ensure that the particulate solids can be captured. This can be achieved by one of several methods:
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Sand filters are one of the most useful treatment processes as the filtering process (especially with slow sand filtration) combines within itself many of the purification functions.
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plants were used to fill sieving vessels that separated solid and liquid materials. The Egyptians also used porous clay vessels to filter drinking water, wine and other liquids.
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sand bed filters. Gravity fed units are used in water purification especially drinking water and these filters have found wide use in developing countries (slow sand filters).
191:– adding small amounts of charge polymer chains which either form a bridge between the particulate solids (making them bigger) or between the particulate solids and the sand. 255:
The depth of the sand bed is recommended to be around 0.6–1.8 m (2–6 ft) regardless of the application. This is linked to the maximum throughput discussed below.
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Cooling water production, drinking water preparation, pre-filtration in active carbon treatments and membrane systems, and the filtration of swimming pool water.
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non-spherical grains. The packing of the grains within the bed is also dependent on the shape of the grains. This then affects the porosity and hydraulic flow.
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Sand filters are used in various sectors and processes, where far-reaching removal of suspended matter from water or wastewater is required.
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Final purification of wastewater, follow-up to metal precipitation and sedimentation, to remove residual traces of metal-based sludge.
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The history of separation techniques reaches far back, as filter materials were already in use during ancient periods. Rushes and
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then run back into the treatment process or disposed of as a waste-water stream. In some countries, the sludge may be used as a
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of varying grades. Where taste and odor may be a problem (organoleptic impacts), the sand filter may include a layer of
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Regeneration methods allow the reuse of the filter medium. Accumulated solids from the filter bed are removed. During
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Crittenden, John C.; Trussell, R. Rhodes; Hand, David W.; Howe, Kerry J.; Tchobanoglous, George (2012).
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Purification of wastewater containing sand-blasting grit and paint particles, at shipyards for example.
853:"Slow Sand Filter | Working, Efficiency, Advantages & Disadvantages of Slow Sand Filter" 900: 478:. Inadequate filter maintenance has been the cause of occasional drinking water contamination. 633: 108:
In addition, there are passive and active devices for causing solid-liquid separation such as
651: 798:. Developments in Aquaculture and Fisheries Science. Vol. 33. 2002. pp. 137–149. 8: 596: 151: 558:
Also used as final purification (or prior to active carbon filtration) to permit re-use.
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Two processes influencing the functionality of a filter are ripening and regeneration.
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Sewage provides a physical matrix to decompose nitrogen based compounds such ammonia.
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to work effectively while slow sand filters can produce very high quality water with
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captured higher up with bed with the concentration gradient decaying exponentially.
185:– adding small, highly charged cations (aluminium 3+ or calcium 2+ are usually used) 799: 663: 482: 475: 463: 284: 168: 42: 586: 295: 791: 104:
Depth filters, where particulates are captured within a porous body of material.
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Used in greenhouse horticulture as drain-water disinfectant (slow sand filter).
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Adjusting the surface charge on the particles and the sand by changing the pH
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Coulson, J. M.; Richardson, J. F.; Backhurst, J. R., Harker, J. H. (1991).
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In addition, particulate solids can be prevented from being captured by
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Surface filters, where particulates are captured on a permeable surface
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Introduction to Solid-Liquid Filtration and Separation Technology.
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As the title indicates, the speed of filtration is changed in the
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Iron-removal from groundwater using aeration and sand filtration.
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and removing most of the solids. The medium of the filter is
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Design and Operating Guide for Aquaculture Seawater Systems
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water through a rapid gravity sand filter strains out the
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Overall, there are several categories of sand bed filter:
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Stormwater filtration used for filtering pollutants from
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and the particles trapped within it, reducing numbers of
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There are several kinds of depth filters, some employing
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throughout the world. The first two require the use of
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K. J. Ives (1990). "Deep Bed Filtration". Chap. 11 of
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are used as a step in the water treatment process of
892: 45:. All three methods are used extensively in the 685:A. Rushton, A. S. Ward, R. G. Holdich (1996). 312:Characteristics of rapid and slow sand filters 73: 503: 774:, 3rd ed., L. Svarovsky (ed). Butterworths. 745:MWH's water treatment: principles and design 738: 736: 734: 732: 634:"Household Sand Filters for Arsenic Removal" 826: 419: 481:Sand filters are occasionally used in the 437: 278: 729: 710: 708: 706: 704: 702: 681: 679: 677: 469:Sand filters become clogged with floc or 622:. National Drinking Water Clearinghouse. 239: 77: 18: 893: 766: 764: 699: 674: 649: 831:. Geneva: World Health Organization. 792:"Chapter 10 Suspended solids removal" 517:Challenges in the application process 236:Rapid pressure sand bed filter design 139:Particulate solids capture mechanisms 428: 195: 23:Sand filter used for water treatment 761: 529: 410:Unlimited with proper pretreatment 13: 14: 922: 827:Huisman, L.; Wood, W. E. (1974). 271:between for mid-sized particles. 211:rapid (pressure) sand bed filters 82:Sand filters on a tomato farm in 582:American Water Works Association 112:, self-cleaning screen filters, 873: 859: 845: 466:to remove such taste and odor. 89:A sand bed filter is a kind of 41:, upward flow sand filters and 820: 784: 643: 626: 609: 127:material and others employing 1: 881:"Sand filtration | EMIS" 867:"Sand filtration | EMIS" 804:10.1016/S0167-9309(02)80010-2 602: 407:Maximum raw-water turbidity 208:rapid (gravity) sand filters 39:rapid (gravity) sand filters 37:There are three main types; 7: 575: 74:Sand bed filtration concept 10: 927: 504:Advantages and limitations 154:or London force attraction 61: 656:Chemie Ingenieur Technik 420:Upflow bed filter design 169:surface charge repulsion 906:Swimming pool equipment 772:Solid-Liquid Separation 650:Anlauf, Harald (2003). 438:Uses in water treatment 279:Slow sand filter design 16:Water filtration device 668:10.1002/cite.200303283 617:"Slow Sand Filtration" 248: 86: 24: 716:Chemical Engineering. 352:Media effective size 245:Rapid pressure filter 243: 81: 22: 829:Slow sand filtration 97:solids from fluids: 51:flocculant chemicals 597:Jewell water filter 396:Regeneration method 214:upflow sand filters 855:. 6 December 2021. 592:Water purification 249: 129:granular materials 87: 32:water purification 25: 695:978-3-527-28613-3 662:(10): 1460–1463. 429:Mixed bed filters 417: 416: 336:Slow sand filter 333:Rapid sand filter 217:slow sand filters 196:Operating regimes 43:slow sand filters 918: 885: 884: 877: 871: 870: 863: 857: 856: 849: 843: 842: 824: 818: 817: 788: 782: 768: 759: 758: 740: 727: 712: 697: 683: 672: 671: 647: 641: 640: 638: 630: 624: 623: 621: 613: 530:Uses in industry 483:sewage treatment 476:soil conditioner 464:activated carbon 341:Filtration rate 327: 326: 324: 323: 319: 285:slow sand filter 148:Direct collision 926: 925: 921: 920: 919: 917: 916: 915: 891: 890: 889: 888: 879: 878: 874: 865: 864: 860: 851: 850: 846: 839: 825: 821: 814: 790: 789: 785: 769: 762: 755: 741: 730: 718:Vol.2, 4th ed. 713: 700: 684: 675: 648: 644: 636: 632: 631: 627: 619: 615: 614: 610: 605: 587:Water treatment 578: 532: 519: 506: 440: 431: 422: 385:Ripening period 330:Characteristics 325: 321: 317: 315: 314: 296:Cryptosporidium 281: 238: 226: 198: 141: 76: 64: 17: 12: 11: 5: 924: 914: 913: 908: 903: 887: 886: 872: 858: 844: 838:978-9241540377 837: 819: 812: 783: 760: 753: 728: 698: 673: 642: 625: 607: 606: 604: 601: 600: 599: 594: 589: 584: 577: 574: 573: 572: 569: 566:surface runoff 562: 559: 556: 553: 549: 546: 531: 528: 518: 515: 505: 502: 439: 436: 430: 427: 421: 418: 415: 414: 411: 408: 404: 403: 400: 397: 393: 392: 389: 386: 382: 381: 378: 375: 371: 370: 367: 364: 360: 359: 356: 353: 349: 348: 345: 342: 338: 337: 334: 331: 313: 310: 280: 277: 237: 234: 219: 218: 215: 212: 209: 197: 194: 193: 192: 186: 180: 165: 164: 161: 158:Surface charge 155: 149: 140: 137: 110:settling tanks 106: 105: 102: 75: 72: 63: 60: 47:water industry 15: 9: 6: 4: 3: 2: 923: 912: 909: 907: 904: 902: 901:Water filters 899: 898: 896: 882: 876: 868: 862: 854: 848: 840: 834: 830: 823: 815: 813:9780444505774 809: 805: 801: 797: 793: 787: 781: 780:0-408-03765-2 777: 773: 767: 765: 756: 754:9780470405390 750: 746: 739: 737: 735: 733: 725: 724:0-7506-2942-8 721: 717: 711: 709: 707: 705: 703: 696: 692: 688: 682: 680: 678: 669: 665: 661: 657: 653: 646: 635: 629: 618: 612: 608: 598: 595: 593: 590: 588: 585: 583: 580: 579: 570: 567: 563: 560: 557: 554: 550: 547: 544: 543: 542: 539: 535: 527: 523: 514: 510: 501: 498: 496: 492: 488: 484: 479: 477: 472: 467: 465: 461: 457: 453: 449: 444: 435: 426: 412: 409: 406: 405: 401: 398: 395: 394: 391:Several days 390: 387: 384: 383: 379: 376: 373: 372: 368: 365: 362: 361: 357: 354: 351: 350: 346: 343: 340: 339: 335: 332: 329: 328: 320: 309: 307: 302: 298: 297: 292: 291: 286: 276: 272: 268: 264: 260: 256: 253: 246: 242: 233: 231: 223: 216: 213: 210: 207: 206: 205: 202: 190: 187: 184: 181: 178: 177: 176: 173: 170: 162: 159: 156: 153: 152:Van der Waals 150: 147: 146: 145: 136: 135:) treatment. 134: 130: 126: 121: 119: 115: 114:hydrocyclones 111: 103: 100: 99: 98: 96: 92: 85: 80: 71: 69: 59: 56: 52: 48: 44: 40: 35: 33: 29: 21: 875: 861: 847: 828: 822: 795: 786: 771: 744: 715: 686: 659: 655: 645: 628: 611: 540: 536: 533: 524: 520: 511: 507: 499: 480: 468: 445: 441: 432: 423: 388:15 min – 2 h 300: 294: 288: 282: 273: 269: 265: 261: 257: 254: 250: 244: 224: 220: 203: 199: 189:Flocculation 174: 166: 142: 122: 107: 91:depth filter 88: 65: 36: 28:Sand filters 27: 26: 689:Wiley VCH. 448:flocculated 399:Backwashing 380:1–6 months 230:backwashing 183:Coagulation 118:centrifuges 95:particulate 895:Categories 603:References 552:flotation. 471:bioclogged 374:Run length 363:Bed depth 358:0.15–0.30 347:0.08–0.25 160:attraction 133:wastewater 84:California 402:Scraping 306:turbidity 163:Diffusion 55:pathogens 639:. EAWAG. 576:See also 495:nitrogen 491:nitrates 456:bacteria 446:Passing 377:1–4 days 369:0.9–1.5 301:scraping 493:, into 487:ammonia 413:10 NTU 366:0.6–1.9 355:0.5–1.2 290:Giardia 125:fibrous 68:genista 62:History 835:  810:  778:  751:  722:  693:  316:": --> 637:(PDF) 620:(PDF) 497:gas. 911:Sand 833:ISBN 808:ISBN 776:ISBN 749:ISBN 720:ISBN 691:ISBN 489:and 460:sand 452:floc 344:5–15 318:edit 293:and 116:and 800:doi 664:doi 897:: 806:. 794:. 763:^ 731:^ 701:^ 676:^ 660:75 658:. 654:. 120:. 34:. 883:. 869:. 841:. 816:. 802:: 757:. 726:. 670:. 666:: 568:. 322:]

Index


water purification
rapid (gravity) sand filters
slow sand filters
water industry
flocculant chemicals
pathogens
genista

California
depth filter
particulate
settling tanks
hydrocyclones
centrifuges
fibrous
granular materials
wastewater
Van der Waals
Surface charge
surface charge repulsion
Coagulation
Flocculation
backwashing

slow sand filter
Giardia
Cryptosporidium
turbidity
flocculated

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