Page 322 - Adsorption by Powders and Porous Solids
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CHAPTER 10. ADSORPTION BY METAL OXIDES                          31 1

    of hydrophobicity shown by all dehydroxylated silicas. The surface rehydroxylation
    was very slow atp/pO < 0.3, but became rapid in the multilayer range; this phenome-
    non was evidently responsible for the low-pressure hysteresis. Indeed, it was found
    that the desorprion branches of the isotherms on gels E and J were remarkably similar
    to  the  corresponding parts of  the  water  isotherms on  the  two  hydroxylated gels
    (Baker and Sing, 1976). We may conclude that the micropores in the rehydroxylated
    gel E regained their high affmity for water.


    103. Aluminas: Structure, Texture and Physisorption


    10.3.1.  Activated alumina
    The name 'activated alumina' is generally applied to an adsorbent alumina (usually
    an  industrial product) prepared  by  the  heat  treatment of  some form of  hydrated
    alumina (i.e. a crystalline hydroxide, oxide-hydroxide or hydrous alumina gel). It has
    been known for many years that certain forms of activated alumina can be used as
    powerful desiccants or for the recovery of various vapours. It was apparent at an early
    stage that the adsorbent activity was dependent on the conditions of heat treatment.
    For example, in  1934 Bayley reported that the adsorption of H,S  by a commercial
    sample of activated alumina was affected by prior heating of the adsorbent at differ-
    ent temperatures, the maximum uptake being obtained after heat treatment at 550°C.
    During an investigation of the catalytic dehydration of alcohols, Alekseevskii (1930)
    found that a calcination temperature of c. 400°C was required to optimize the adsorp-
    tion of  the alcohol reactants, whereas calcination at 600°C was preferable for the
    adsorption of the olefine products.
      Somewhat later it began to appear that there was a lack of agreement between the
    recorded dependence of  surface area on the temperature of  calcination (e.g. in the
    work of Krieger, 1941; Feachem and Swallow, 1948; Taylor, 1949; Gregg and Sink,
    1951; de Boer, 1957). In fact, such differences are not really surprising. To obtain
    reproducible adsorbent properties it is necessary to control: (a) the chemical and phys-
    ical nature of the starting material (i.e.  its st~ucture, crystal/particle size, amount of
    sample purity); (b) the conditions of heat treatment (type of furnace, atmosphere, time
    - temperature profile - preferably  by  a  controlled rate thermal analysis (CRTA)
    heating procedure); and (c) the methods used to interpret the adsorption data (BET,
    BJH, etc.).

    10.3.2.  Aluminium trihydroxides
    Although various modifications  of  aluminium trihydroxide, Al(OH),,  have  been
    described in the literature, there are only three common forms: gibbsite (originally
    also called hydrargillite) bayerite and nordstrandite. Gibbsite is the best known and
    most abundant. It is the main constituent of North and South American bauxite and
    is obtained as an intermediate product (i.e. 'Bayer Hydrate') in the Bayer process for
    the production of aluminium from bauxite.
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