Page 95 - Adsorbents fundamentals and applications
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80   ACTIVATED CARBON


                               60
                                                                 Activated carbon
                              Cumulative pore volume, cm 3 /100 gm  40  Zeolite 5A
                               50
                                                                       Silica gel




                               30


                               20


                               10                                  Activated alumina
                                        MSC
                                     MSC
                                0
                                 2           5        10      20           50
                                                   Pore diameter, Å
                     Figure 5.1. Pore-size distributions for activated carbon, silica gel, activated alumina, two
                     molecular-sieve carbons (MSC), and zeolite 5A (Yang, 1997, with permission).


                     process is used primarily for gas and vapor adsorption processes. The other acti-
                     vation process that is also used commercially depends on the action of inorganic
                     additives to degrade and dehydrate the cellulosic materials and, simultaneously,
                     to prevent shrinkage during carbonization. This is called chemical activation, usu-
                     ally used for lignin-based precursors such as sawdust. No pre-carbonization step
                     is required. Lignin, usually the raw material that is blended with activators such
                     as phosphoric acid, zinc chloride, potassium sulfide, or potassium thiocyanate,
                                                               ◦
                     is carbonized at temperatures between 500 to 900 C. The remaining chemicals
                     are removed from the carbon by acid or water wash. The product, usually in
                     powder form, is used for aqueous or gas phase purposes. The inorganic material
                     contained in activated carbon is measured as ash content, generally in the range
                     between 2 and 10%. Beside granulated activated carbon (GAC), powdered acti-
                     vated carbon (PAC) is also used commercially (for example, for dioxin removal
                     from incinerators by injection of PAC; Yang et al., 1999).
                       Although the process for manufacturing activated carbon has been largely
                     empirical, a considerable understanding of the fundamental processes is now
                     available (e.g., Barton et al., 1999). During carbonization of the precursor raw
                     material, condensation of polynuclear aromatic compounds and breakage of side-
                     chain groups occur, resulting in a carbon residue. In the meantime, cross-linking
                     reactions occur that inhibit the development of a pre-graphite structure. Hence
                     activated carbon is referred to as non-graphitizing, as opposed to graphitizing. The
                     graphitizing type applies to pitches derived from petroleum, coal tar, and aromatic
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