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                  4.1 Basic Principles of Adsorption and Ion Exchange  251


                     (  200 m  2  /g) and is highly porous.  Peat moss is a relatie material and v xpensi v ely ine
                     is commercially sold at a price of 0.023 $/kg in the united States.
                  •  Fly ash:  Fly ash is an industrial solid wwer plants. Fly ash aste generated in thermal po
                     can be easily solidified after the heavy metals hae been adsorbed. v
                  •  Iron (III) hydroxide waste:  v w aste al from w Especially for heavy metals remoater, iron
                     ,
                     (III) hydroxide waste and waste slurry from the fertilizer industry xanthate, rice husk,
                     carbon, and coconut shell hae been studied and can be considered as alternati v  es. v
                  In Tables 4.4–4.7, seeral important adsorbents data are tab v ulated.

                  Safety consider ations
                  Adsorption is generally an exothermic process leading to temperature rise. Although this
                  property is useful when storage of heat is desired, it is not the case in the adsorption of
                  ed,
                  v
                  VOCs. If certain hydrocarbons are in the carbon or metals on the carbon may cat-
                  olv
                  alyze the oxidation of these pollutants when the adsorbent is hot, resulting in bed f ires that
                  deteriorate the adsorbent by either altering the its pore size or conerting part of it to ash. v
                  Cooling of the bed or humidification of the air can be employed to aoid the outburst of v
                                                  Table 4.4

                             Basic characteristics of common adsorbents (Perry and Green, 1999)
                  Adsorbent     Hydrophilic  Hydrophobic  Amorphous  Structured
                  Activated carbon
                  Polymers
                  Silica gel
                  Activated alumina
                  es v Carbon molecular sie
                  Silicalite
                  Zeolites
                  (3A, 4A, 5A, 13X)


                                                  Table 4.5
                        Physical properties of common adsorbents (Perry and Green, 1999; Knaebel, 1995)
                  Adsorbent  Micropore  Internal  Bulk  Surface  Adsorption
                                   size    porosity  density  area  Capacity
                                   (Å)          (%)       (kg/m  3  )  S (m  2  /g)  Q  max  (g/g)
                                              p
                                                         b
                  Carbons            6  a     35–85  250–700  100–1800  0.3–0.7
                  Organic polymers  Varying  40–60  420–700  80–700  0.45–0.55
                  Silica gel         10     38–48  700–820  600–800  0.35–0.50
                  Aluminas           6  b     30–57  700–930  200  0.1–0.33
                  Zeolites   3.9–8  30–38  580–680  600–700  0.21–0.36
                  (3A, 4A, 5A, 13X)

                  a  Activated carbon.
                  b  Activated alumina.
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