Page 6 - Adsorption Technology & Design, Elsevier (1998)
P. 6

The development of adsorption technology  3


            1.2    EARLY COMMERCIAL PRACTICE

            Full  details  of  early  commercial  practice  can  be  found  in  the  writings  of
            Mantell (1951). The oil industry used naturally occurring clays to refine oils
            and  fats  as  long  ago  as  the  birth  of  that  industry  in  the  early  part  of the
            twentieth  century.  Clay  minerals  for  removing  grease  from  woollen
            materials (known as the practice of fulling) were used extensively. The min-
            eral came  to be  known  as fuller's  earth.  Its composition consists chiefly of
            silica with lower amounts of alumina, ferric oxide and potassium (analysed
            as  the  oxide).  Other  naturally  occurring  clays  (kaolin  and  bentonite)  also
            contain large proportions  of silica with smaller proportions  of alumina and
            were also used for bleaching oils and petroleum spirits. Two methods were
            in common use for decolouring oil and petroleum products: the oil could be
            percolated  through  a bed of granular clay or it could be directly contacted
            and agitated with the clay mineral. The oil or lubricant to be bleached was
            first treated  with sulphuric  acid  and  a little clay, filtered  and  subsequently
            run into mixing agitators containing the adsorbent clay and which decolour-
            ized the lubricant after a sufficiently long contact time (of the order of one to
            three minutes) and at a suitable temperature (usually about 60-65~
              Another  mineral,  which  was widely used  as  a  drying agent, was refined
            bauxite  which  consists  of hydrated  aluminium  oxide.  It  was  also  used  for
            decolourizing residual oil stocks. Another form of aluminium oxide mineral
            is florite which adsorbs  water rapidly and  does not swell or disintegrate  in
            water.  Consequently,  it  was,  and  still  is,  used  for  the  drying  of gases  and
            organic  liquids.  The  early  practice  was  to  utilize  beds  of  florite  at  room
            temperature  through  which  was  pumped  the  organic  liquid  containing
            moisture.  Reactivation of the bed was accomplished by applying a vacuum
            and heating by means of steam coils located within the bed.  Alternatively,
            the beds were reactivated by circulating an inert gas through the adsorbent,
            the desorbed water being condensed on emergence from the bed in cooled
            receptacles.
              Some  types  of  carbon  were  in  common  use  for  decolourizing  and
            removing odours from a wide variety of materials.  Carbons were also used
            for  treating  water  supplies.  The  decolourization  of  liquids,  including  the
            refining of sugar melts, was accomplished by mixing the  carbon  adsorbent
            with the liquid to be bleached and subsequently filtering. In some cases the
            residual adsorbent was regenerated for further use by passing steam through
            a  bed  of the  spent  adsorbent.  In  the  case  of water  treatment, non-potable
            waters were either percolated  through beds of carbonaceous  adsorbent,  or
            activated carbon was added to water in mixing tanks. The resulting effluent
            was  then  treated  with  chlorine  to  remove  toxins.  Alternatively,  the
            contaminated water was first treated with excess chlorine and then allowed
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