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Powder activated carbon

Fig. 1. Alternative wastewater treatment technologies, where GAC = granular activated carbon, PAC = powdered activated carbon, POTW = publicly owned treatment works, and RBC = rotating biological contactor (— ), wastewater return flows (—— ), sludge. Fig. 1. Alternative wastewater treatment technologies, where GAC = granular activated carbon, PAC = powdered activated carbon, POTW = publicly owned treatment works, and RBC = rotating biological contactor (— ), wastewater return flows (—— ), sludge.
Specifications. Activated carbon producers furnish product bulletins that Hst specifications, usually expressed as a maximum or minimum value, and typical properties for each grade produced. Standards helpful in setting purchasing specifications for granular and powdered activated carbon products have been pubHshed (33,34). [Pg.531]

Production capacity was almost equally spHt between powdered and nonpowdered activated carbon products. Powdered activated carbon, a less expensive form used in Hquid-phase appHcations, is generally used once and then disposed of. In some cases, however, granular and shaped products are regenerated and reused (35). In 1990 production capacity for granular and shaped products was spHt with about two-thirds for Hquid-phase and one-third for gas-phase appHcations (37). [Pg.531]

Because powdered activated carbon is generally used in relatively small quantities, the spent carbon has often been disposed of in landfills. However, landfill disposal is becoming more restrictive environmentally and more costiy. Thus large consumers of powdered carbon find that regeneration is an attractive alternative. Examples of regeneration systems for powdered activated carbon include the Zimpro/Passavant wet air oxidation process (46), the multihearth furnace as used in the DuPont PACT process (47,48), and the Shirco infrared furnace (49,50). [Pg.532]

Batch-stirred vessels are most often used in treating material with powdered activated carbon (72). The type of carbon, contact time, and amount of carbon vary with the desired degree of purification. The efficiency of activated carbon may be improved by applying continuous, countercurrent carbon—Hquid flow with multiple stages (Fig. 3). Carbon is separated from the Hquid at each stage by settling or filtration. Filter aids such as diatomaceous earth are sometimes used to improve filtration. [Pg.533]

Fig. 3. Multistage countercurrent appHcation of powdered activated carbon. Fig. 3. Multistage countercurrent appHcation of powdered activated carbon.
AWWA Standardfor Powdered Activated Carbon, ANSI/AWWA B600, American Water Works Association, Denver, Colo., 1990, 32 pp. [Pg.536]

The most popiilar dry scrubbing systems for incinerators have involved the spray drying of hme slurries, followed by dry coUection in electrostatic precipitators or fabric filters. Moller and Christiansen [Air Poll. Cout. Assoc. 84-9.5 (1984)] published data on early European technology. Moller et al. [U.S. Patent no. 4,889,698 (1989)] describe the newer extension of that technology to include both spray-dryer absorption and dry scrubbing with powdered, activated carbon injection. They claim greatly improved removal of mercury, dioxins, and NOx. [Pg.1599]

One such monolithic carbon has been produced by Sutcliffe Speakman Carbons and is described by Tamainot-Telto and Critoph [17]. Powdered activated carbon is mixed with a polymeric binder, compressed in a die and fired to produce a monolith of the desired shape, with a density of 713 kg/m and conductivity of 0.33 W/mK. A heat transfer coefficient of 200 W/m K has been measured between the blocks and aluminium fins. [Pg.336]

Fluidized-bed powdered activated carbon systems represent another important process. The use of activated carbon for the tertiary treatment of secondary sewage effluents has been used extensively. Powdered carbon is as effective as granular activated carbon for removing the organic impurities from the wastewater. [Pg.318]

For organic contaminant removal from surface water packed-tower aeration, granular activated carbon (GAC), powdered activated carbon (PAC), diffused aeration, advanced oxidation processes, and reverse osmosis (RO). [Pg.9]

Powder Activated Carbon (PAC) - pulverized carbon with a size predominantly less than 0.18mm (US Mesh 80). These are mainly used in liquid phase applications and for flue gas treatment. [Pg.404]

With powder activated earbon, in most cases, the carbon is dosed into the liquid, mixed and then removed by a filtration process. In some cases, two or more mixing steps are used to optimise the use of powder carbon. Powder activated carbon is used in a wide range of liquid phase applications and some specific gas phase applications such as Incinerator flue gas treatment and where it is bonded into filters sueh as fabrics for personnel protection. [Pg.407]

To enhance the purification process and increase the degree of purification, powdered activated carbon (PAC) may be added directly to the aeration tank, or the biologically treated wastewater may be filtered through granulated activated carbon (GAC) for posttreatment. [Pg.168]

Oil-Water Separation, Biological Treatment, Powdered Activated Carbon Adsorption, and Clarification... [Pg.281]

Once the micropore surfaces of activated carbon are saturated with target material, the spent carbon must be replaced or regenerated. Granular activated carbon (GAC) is favored over powder activated carbon (PAC) in most cases, because the former is considered to be capable of regeneration and sustainable to flow, although the costs of both carbons and the cost of regeneration are high. [Pg.624]

Monkiedje et al. [10] investigated the fate of niclosamide in aquatic system both under laboratory and field conditions. The octanol/watcr partition coefficient (Kaw) of niclosamide was 5.880 x 10 4. Adsorption isotherm studies indicated that the Freundlich parameters (K, n) for niclosamide were 0.02 and 4.93, respectively, for powder activated carbon (PAC), and 9.85 x 10 5 and 2.81, respectively, for silt loam soil. The adsorption coefficient (Aoc) for the drug was 0.02 for PAC, and 4.34 x 10-3 for the same soil. Hydrolysis of niclosamide occurred in distilled water buffer at pH above 7. No photolysis of the drug was observed in water after exposure to long-wave UV light for 4 h. Similarly, neither chemically volatilized from water following 5 h of sample aeration. Under field conditions, niclosamide persisted in ponds for over 14 days. The half-life of niclosamide was 3.40 days. [Pg.70]


See other pages where Powder activated carbon is mentioned: [Pg.717]    [Pg.807]    [Pg.178]    [Pg.193]    [Pg.280]    [Pg.531]    [Pg.532]    [Pg.534]    [Pg.384]    [Pg.1540]    [Pg.2220]    [Pg.35]    [Pg.10]    [Pg.57]    [Pg.373]    [Pg.373]    [Pg.563]    [Pg.259]    [Pg.281]    [Pg.662]    [Pg.725]    [Pg.731]    [Pg.754]    [Pg.850]    [Pg.916]    [Pg.1054]    [Pg.590]    [Pg.591]    [Pg.277]    [Pg.49]   
See also in sourсe #XX -- [ Pg.404 ]

See also in sourсe #XX -- [ Pg.624 , Pg.725 , Pg.732 , Pg.916 , Pg.1240 ]




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