Page 179 - Gas Adsorption Equilibria
P. 179

3. Gravimetry                                                    165


             From this figure it clearly can be seen that the AC is selective for   as
          both the    as  well as  the   concentration  in the adsorbed  phase are
          considerably reduced  compared  to  their values  in the  sorptive gas  phase.
          Information of this kind is very valuable for the selection of adsorbents in gas
          purification and separation processes [3.37].

             Example 2

             Adsorption of dye from an aqueous solution onto activated carbon.

             The adsorption  of dye Levafix  ® Brilliant Red E-4BA  from an aqueous
          solution onto activated  carbon  F300  (Chemviron Carbon) at  24  °C and
          ambient pressure has been investigated using a magnetic suspension balance
          (MSB) (Rubotherm  GmbH,  Bochum,  Germany)  [3.46, 3.47]. The
          experimental setup is  shown in  Figure  3.28. The  dark region within the
          adsorption vessel of the MSB indicates the volume filled with liquid solution.
          More  details of design and materials are  given in [3.47] and  literature cited
          there. Results of gravimetric measurements are given in the next Figure 3.29.
          The lower curve refers to the sorption process of pure water into the activated
          carbon. There are experimental indications that the density of the water in the
          pores is about the same as the density of ice at 0 °C       i. e. lower
          than the  density  of water in its  liquid  state. Indeed,  it  is  known that pore
          liquids can exhibit three dimensional structures [3.48] and that adsorption in
          micropores often is accompanied by kind of freezing process which also can
          be simulated by  statistical molecular models  [3.49]. The  upper curve  shows
          the increase of mass of  an activated carbon sample due to the combined
          adsorption of water and dye. Seemingly both processes are fairly slow and did
          not reach  equilibrium after  a period of obeservation of 30 hours  and  more.
          Gravimetric measurements were  complemented by traditional  beaker
          experiments allowing thus to calculate separately the masses of water and dye
          adsorbed in the activated carbon. The procedure is similar to that described in
          the next Chapter 4 (Volumetric-Gravimetric Measurements). Details are given
          [3.47].

             Though these  measurements  certainly are  of preliminary  character and
          need more detailed discussion, it should be emphasized that they demonstrate
          the possibility to explore adsorption processes of complex molecules like dye
          Levafix ® Brilliant Red E-4BA (whose chemical  formulae is classified) on
          microporous sorbents. This certainly  is of  interest not  only  for  textile
          engineering but  also  for waste  water management  and for  environmental
          protection.
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