Page 228 - Gas Adsorption Equilibria
P. 228

214                                                         Chapter 4


          these mixtures always  additional  measurements  of  the sorptive gas
          concentrations  by   gas-chromatography   or   mass-spectrometry   are
          recommended.

             As already  mentioned  in  Sect. 2.3  the  dispersions of  the  balance
          measurement      of  pressure   and  of  system’s temperature  are  most
          important to  get accurate values of adsorbed  masses         whereas
          the contributions of uncertainties in the compressibility factor (Z),  often are
          rather small and hence may be neglected.

          3.4      Example

             Densimetric-gravimetric measurements  of binary  coadsorption equilibria
          have been performed at IFT using the instrument shown in Figs. 4.13, 4.14 in
          2001-2002,  [4.17]. The  system chosen  was  carbon  dioxide  methane
                 and activated  carbon  (AC) D 47/3  at T = 293  K for pressures up to
          1.4 MPa. Gas mixtures were provided by mixing components of purities
                                                delivered by  Messer  Griesheim,
          Düsseldorf. The AC is manufactured by German CarboTech company, Essen.
          It is used as nearly cylindrical pellets (length: 3 mm, diameter: 1 mm) having
          a bulk density  of             and a BET-surface of                 It
          mainly is used in  industrial  adsorption  processes for  purification of  gas
          mixtures including either hydrogen or methane.

             In Figure 4.15  an example of the kinetics of the coadsorption process of a
          gas mixture           on AC D47/3 is given. The equilibrium state realized
          after  4  hours was at  p  =  0.71  MPa, T =  293.25  K,  and  sorptive gas
          concentration                              The upper curve indicates the
          increase of the total absolute mass of   and   adsorbed. As can be seen
          from the figure, adsorption occurs rapidly in an initial period of about 5 min.
          accompanied by  a  sharp  increase of sorptive’s gas  temperature (taken  by  a
          thermocouple immediately  below  the  sorbent sample)  of ca.  2.7  K and an
          almost instantaneous decrease of gas pressure  from its initial value of about
          1.1 MPa  to  0.73  MPa.  Then the  uptake of  mass  slows down  showing
          relaxational behavior of order (1) within the next 1.5 hours and reaching 99 %
          of its equilibrium value after 2 hours. At this time (135 min.) the gas circulator
          was shut  down. This is  reflected in all  3  curves by a tiny  fluctuation, most
          clearly  observable in  the (upper) mass uptake curve. The  relaxation in the
          mass uptake is accompanied  by  a  similar  relaxation of  the  sorptive gas
          temperature (lower curve) showing a small secondary decrease after circulator
          shut down of about (0.1K).
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