Page 123 - Adsorbents fundamentals and applications
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108   ACTIVATED CARBON

                                  1200

                                          Influent
                                  1000
                                 Concentration of TCE [ppb]  600
                                   800





                                   400
                                                              Ce
                                                              C0
                                   200    Effluent            C0  GAC(FS400)
                                                                 ACF(FT15)
                                                              Ce
                                     0
                                      0       100       200      300      400
                                                Flow volume (I/g Carbon)
                     Figure 5.20. Breakthrough curves of trichloroethylene in contaminated ground water in packed
                     beds of GAC (Filtrasorb 400) and ACF (phenolic resin-based, FT 15) (from Suzuki, 1990, with
                     permission).



                     of graphite (1.38 m -cm). The electrical resistivities of ACF clothes and fabrics
                     are, however, substantially higher. Subrenat et al. (2001) measured the electrical
                     resistivities of fabrics of a number of rayon-based ACFs and reported values as
                     high as 600 m -cm. The electrical resistivity of a ACF composite monolith was
                     130 m -cm. Comparing different ACF-clothes, the electrical resistivity increased
                     with surface area due to higher void fraction (Subrenat et al., 2001).
                       The high conductivity enables sorbent regeneration by resistance heating of
                     the beds, which has been referred to as electrothermal desorption. Electrother-
                     mal desorption has been studied by a number of groups (Petrovska et al., 1991;
                     Burchell et al., 1997; Lordgooei et al., 1998; Sullivan et al., 2001; Subrenat et al.,
                     2001). This approach is particularly promising for purification such as removal
                     of VOCs, as demonstrated by Lordgooei et al. (1998) by using a fiber-cloth
                     adsorber.
                       The graphitic nature also makes ACFs heat resistant, so they are inflammable
                               ◦
                     up to 1000 C. Lack of dust/fines from the ACF has also been claimed as
                     an advantage.
                       The high tensile strength of the activated carbon fibers gives ACF the versa-
                     tility to be formed into a large variety of different types of cloths, fabrics, papers,
                     felts, and composites. Combined with high adsorption capacities and rates, these
                     different materials are excellent candidates for fabricating low-volume, high-
                     throughput adsorption devices. For example, a rotor-type adsorber (with counter-
                     current thermal regeneration) made from corrugated ACF has been demonstrated
                     for solvent removal from air (Suzuki, 1994). This type of adsorber, or monolithic
                     wheel, has been discussed in some detail by Humphrey and Keller (1997).
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