| Originally Published 1994 - (Costs Are Outdated) | | | | The disadvantages include slow system throughput |
| Companies should consider such factors as space and | | | | and high costs associated with the filter media, which |
| capital requirement, desired filtrate quality, and level | | | | must be applied continuously to the batch |
| of automation when selecting water and wastewater | | | | pretreatment tank immediately before vacuum |
| filters. | | | | filtration. In addition, the filtering media increase total |
| Filtration is the easiest way to remove solids from | | | | sludge volume as much as 60%. Because vacuum |
| water and wastewater streams. In wastewater | | | | filter cost usually includes the pretreatment system, a |
| systems, filtration is used to decrease suspended | | | | unit that processes 19 m3/d (5000 gal/d) can cost |
| solids entering the publicly owned treatment works or | | | | $60,000. |
| water-reuse systems or to increase solids in sludge | | | | Cyclone Separators |
| dewatering applications. | | | | Cyclone separators are relatively new. Because they |
| Filter selection begins after a company determines | | | | have higher rotating speeds than vacuum filters, they |
| the required level of filtration or filtered water quality; | | | | create a significant amount of centrifugal energy to |
| decides whether filtrate will be disposed or reused; | | | | filter wastewater through various media sizes. The |
| identifies how much space is available; calculates the | | | | rotating filter uses a fixed-micronsize medium, such as |
| amount of capital available to purchase, operate, and | | | | diatomaceous earth, to filter the wastestream. The |
| maintain the system; decides whether the system | | | | benefits of cyclone separators include their ability to |
| should be automatic or manual; and considers any | | | | handle variable throughputs, filter varying particle |
| pertinent water conservation requirements. | | | | sizes, and produce drier sludge cake than vacuum |
| The level of solids removal or filtered-water quality | | | | filters for about the same cost (around $60,00). heir |
| desired defines the type and size of filter necessary; | | | | drawbacks are similar to those of vacuum filters, |
| most are available with varying automation levels and | | | | namely high filter media costs and sludge volume. |
| price ranges. | | | | Plate-and-frame Presses |
| Proper filter size is determined by flow rate and the | | | | Plate-and-frame presses are batch processes in which |
| amount, size, and type of solids to be removed. | | | | fixed plates held together in a hydraulic press are |
| Particle sizes and filtration levels can be determined | | | | pre-coated with diatomaceous earth filtering media. |
| by filtering water and solids through varying sizes of | | | | The press size depends on the total solids volume |
| filter paper and measuring the total solids content of | | | | per load. Liquid is loaded into the presses with an |
| filtered water. | | | | air-driven diaphragm pump in increments of 172, 345, |
| Solids remaining in filtered water will be the same size | | | | 517, and 690 kPa (25, 50, 75, and 100 psi). The press |
| or smaller than the last filter paper used and will | | | | is pressurized at 690 kPa (100 psi) causing water to |
| indicate which filter media opening size to use. (A | | | | be squeezed out. After water is removed, the filter |
| filter manufacturer or laboratory can be hired to | | | | is "blown down" with air and opened so sludge can |
| perform this procedure.) The quantity of solids in | | | | be removed from the plates. The cake usually is at |
| water or wastewater can be determined by a | | | | least 35% solids. The limitations of plate-and-frame |
| laboratory analysis of total solids; flow can be | | | | presses include a processing time of at least 4 hours, |
| determined from plant records or an in-line flow | | | | a large footprint, an ability to dewater only the |
| meter. | | | | volume of the plates, and the operating time required |
| The following equation is used to calculate solids | | | | to clean the plates. Therefore, if wastewater |
| loadings (how quickly a filter will load with solids): | | | | contains high solids levels, the press must be large. |
| solids (lb/h) = flow (gal/min) x total solids (ppm) x | | | | Filter presses range in size from 0.014 to more than |
| (8.34/60/1,000,000). | | | | 2.8 m3 (0.5 to more than 100 ft3). An.028-m3 (1-ft3) |
| After solids loading, filter area, and filter media | | | | press costs $3,500, and a 2.3-m3 (80-ft) press costs |
| opening size have been determined, the amount of | | | | $100,000. Large presses also require automatic loading |
| time required before cleaning, or back-washing, should | | | | controls, plate shifters, sludge carts, and other |
| be calculated, and the fate of filtrate waste must he | | | | equipment that can cost an additional $100,000. The |
| determined. | | | | advantage of filter presses is their ability to produce |
| In other words, after a filter is backwashed, where | | | | steady, dry cake, which often is required for landfill |
| will wastewater go? Backwashing often requires up | | | | disposal. |
| to 10% of the total filtered volume, a 10:1 ratio. For | | | | Multiplate Spring-loaded Filters |
| example, 379 m3 (100,000 gal) of filtered water | | | | Multiplate spring-loaded filters use specially fitted disks |
| would generate 38 m3 (10,000 gal) of backwash that | | | | with machined gradations that provide the required |
| contains concentrated solid and may require additional | | | | micron-size opening. The disks, which are held |
| treatment. | | | | together with a preloaded spring, allow water to flow |
| Some wastewater must be pretreated before | | | | through while holding back filtered particles as small as |
| filtration. Oily wastewater, for example, tends to | | | | 2 microns. These filters are backwashed with water |
| agglomerate quickly between or over filter media and | | | | based on a preset pressure differential and come |
| requires conditioning before filtration. Fine-grade | | | | with an option for all- water or airassisted |
| filtration systems are susceptible to fouling from | | | | backwashing, which saves water and greatly |
| biological growth, yeast, and other microorganisms; | | | | increases filter-plate scouring. These continuous |
| performing bench tests or consulting with filter | | | | on-line filters usually are configured in pairs (one for |
| manufacturers about specific applications is | | | | filtration, one for backwashing). The amount of water |
| recommended. | | | | used for backwashing is about 10% of the total |
| Y-Strainers | | | | filtered flow. Air-assisted filter backwash saves an |
| Y-strainers are the simplest, least expensive ($30 to | | | | additional 3% to 5% of water but requires |
| $100) filters, but they have a small filter area and | | | | compressed air. The programmable logic |
| require frequent maintenance. They typically are used | | | | control-based filters enable adjustments in the time |
| on small pipes to protect such equipment as seals, | | | | between backwashes and backwash duration. The |
| pumps, and nozzles from solids buildup. | | | | filters cost $4,500 per pair, and the controller costs |
| Bag Filters | | | | an additional $5,000 but can control a bank of up to |
| Bag filters basically are larger Y-strainers. These filters | | | | 12 filters. |
| are bags of selected pore sizes that are enclosed in | | | | Multimedia Sand Filters |
| a pressure housing with a removable cover for | | | | Multimedia sand filters traditionally are used to treat |
| cleaning. They are easy to use, come in variable | | | | water but also can be used to treat wastewater |
| filtering sizes, and are relatively low in cost, especially | | | | that has non-uniform solids loadings. These |
| for final filtration or applications with low solids | | | | threedimensional systems provide much greater |
| loadings. Bag filters do not exceed 203 mm (8 in.) in | | | | filtering volume than other filters because they use |
| diameter; for larger diameters, an inline bank with | | | | both the bed surface and depth to remove particles |
| multiple filters in one housing is used. | | | | as small as 0.45 microns. |
| The price of carbon or stainless steel bag filter | | | | An on-line suspended solids analyzer measures the |
| housings varies according to size, from $100 for a | | | | amount of particles coming through the filter. As |
| 51-mm (2-in.) housing to $3000 for a 1219 mm (48-in.) | | | | solids levels increase past, or break through, the filter, |
| housing. Filter bags range in price from $6 to $10 for | | | | a preset suspended solids level initiates backwash. |
| pore sizes of 25 to 800 microns. Bags are available | | | | Backwash can be air assisted to save water, but |
| straight or pleated. Pleated bags provide added | | | | care must be taken not to blow the media out with |
| surface area but cost more than twice as much as | | | | the filtrate material. These filters usually come in pairs |
| flat ones. The disadvantages of bag filters include | | | | to provide continuous on-line service. They work well |
| high maintenance requirements for systems that are | | | | as final filters for water with uniform solids. Water |
| underdesigned or have high solids loads and the cost | | | | savings is accomplished when the right control |
| of bag replacement. | | | | scheme and air-assisted backwashing system are |
| Vacuum Filters | | | | used, A 0.19-nil/min (50-gal/rnin) pair of multimedia |
| Vacuum filters use a slowly rotating vacuum | | | | sand filters with a controller and backwashing header |
| (negative pressure) drum that pulls dirty liquid from | | | | assembly costs approximately $15,000. |
| the outside of the drum and media to the inside of | | | | With the vast array of available filters and control |
| the drum. The vacuum filter usually is packaged with | | | | scenarios, companies willing to perform some |
| a pre-batch treatment system to coagulate the | | | | advance research on their wastestreams should have |
| wastestream before filtration. The advantage of this | | | | no difficulty finding a system to meet their needs. |
| filter is its ability to filter a variety of wastewaters. | | | | |