Page 107 - Academic Press Encyclopedia of Physical Science and Technology 3rd Chemical Engineering
P. 107

P1: ZBU 2nd Revised Pages
 Encyclopedia of Physical Science and Technology  EN002G-87  May 19, 2001  20:3







              Catalyst Characterization                                                                   505

                                                                  Hysteresis in the adsorption–desorption isotherms
                                                                (Fig. 4) is a common observation for supports with a large
                                                                fraction of small pores. It results from desorption from
                                                                the meniscus at the end of a filled pore. The vapor pres-
                                                                sure above the liquid at the pore mouth defines the pore
                                                                radius in the Kelvin equation. Therefore, it is the desorp-
                                                                tion branch of the isotherm that is preferred in calculations
                                                                of pore size distributions.


                                                                  3. Mercury Intrusion

                                                                The penetration of mercury into the pores of a material is
                                                                a function of applied pressure. At low pressures mercury
                                                                penetrates the large pores, whereas at higher pressures the
                                                                smaller pores are progressively filled. Due to the nonwet-
                                                                ting nature of mercury on oxide supports, penetration is
                                                                met with resistance. The Washburn equation relates the
                                                                pore diameter d with the applied pressure P:
                                                                                    −4γ cos θ
                                                                                d =
                                                                                        P
                                                                  The wetting or contact angle θ between mercury and
                                                                solid is usually 130 , and the surface tension of the mer-
                                                                               ◦
                                                                cury, γ , is 0.48 N/m. Pressure is expressed in atmospheres
                                                                                     ˚
                                                                and d in nanometers (10 A). This technique is satisfac-
                                                                                      ˚
                                                                tory for pores down to 50 A diameter; however, this is a
                                                                function of the instrument capability. Maximum diameters
                                                                                   6 ˚
                                                                measured are usually 10 A.
              FIGURE 3 Measurement of surface area by the BET gas adsorp-
              tion method. (A) Typical adsorption isotherm with a relatively flat
              curve in the region of monolayer adsorption. (B) Plot of the linear
              form of the BET equation between p/p 0 = 0.05 and 0.3 used to
              calculate the monolayer coverage V m .

                2. Gas Adsorption: Pore Size
              The same equipment as that for measuring surface area can
              be used to determine the pore size distribution of porous
                                            ˚
              materials with diameters of 20 to 500 A, except that high
              relative pressures are used to condense N 2 in the catalyst
              pores. The procedure involves measuring the volume ad-
              sorbed in either the ascending or the descending branch
              of the BET plot at relative pressures close to 1. Capillary
              condensation occurs in the pores in accordance with the
              Kelvin equation,
                                     2σ V cos θ
                           ln P/P 0 =−        ,
                                       rRT
              where σ is the surface tension of liquid nitrogen, θ the
              contact angle, V the molal volume of liquid nitrogen, r
              the radius of the pore, R the gas constant, T the absolute
                                                                FIGURE 4 Nitrogen adsorption and desorption isotherms at
              temperature, P the measured pressure, and P 0 the satura-  78 K. Pore size distributions in the micropore range are calcu-
              tion pressure.                                    lated from the isotherms using the Kelvin equation.
   102   103   104   105   106   107   108   109   110   111   112