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156 Chapter 7<br />

Uppermost layer is in equilibrium with vapor phase. iii) The heat of adsorption at all sites<br />

is constant and equal to the heat of condensation from the second layer on; iv) There is no<br />

lateral interactions between molecules. v) At saturation pressure, the number of layers<br />

has infinite thickness. Hence, the BET equation could be derived:<br />

p<br />

n a (p 0 − p) = 1<br />

n a m C<br />

+<br />

(C − 1)<br />

n m a C<br />

Here n a is the amount adsorbed, p is the pressure, p0 is the saturation pressure of the<br />

adsorbed gas at a given temperature, n m<br />

a<br />

is the monolayer capacity and C an empirical<br />

constant. The value of C can be associated to the magnitude of adsorbent-adsorbate<br />

interactions. This equation is an adsorption isotherm and can be plotted as a BET plot<br />

where 1/[n a (p0/p-1)] is the y-axis and p/p0 on the x-axis. The linear relationship of the<br />

BET plot is kept only in a pressure region of p/p0= 0.05 - 0.30. For microporous materials<br />

such as MOFs, a even smaller pressure range (p/p0 = 0.02 - 0.10) is usually applied.<br />

Subsequently, the monolayer capacity n m<br />

a<br />

can be derived from the slope of the BET plot.<br />

Consequently, the specific surface area SBET can be calculated from the following equation:<br />

SBET = n m a N A a m /m<br />

p<br />

p 0<br />

where NA is the Avogadro constant and am is molecular cross-section area occupied by a<br />

single adsorbate molecule in the complete monolayer and m the mass of adsorbent. Still,<br />

we should note that the BET theory is developed on basis of the oversimplified model. In<br />

fact, SBET is greatly affected by the nature of the adsorbent as well as the strength of<br />

adsorbate-adsorbent interactions. Microporous solids including MOFs, the pore surface of<br />

which are rather heterogeneous, the above mentioned assumptions are not valid. The<br />

obtained value of the BET surface area (SBET) can be widely used to compare the porosity<br />

of different porous materials and should not be considered as a precise absolute value.<br />

The adsorption isotherms of H2 adsorption at 77 K and 87 K were independently fit with<br />

triple site Langmuir model<br />

n = q sat,Ab A p<br />

1 + b A p + q sat,Bb B p<br />

1 + b B p + q sat,Cb C p<br />

1 + b C p<br />

where n is the molar loading of adsorbate (mmol/g), qsat is the saturation loading of site<br />

A/B/C (mmol/g), b is the Langmuir parameter for A/B/C (bar -1 ), and p the pressure(bar).<br />

After the triple-site Langmuir fits, the exact pressures correspond to the same amount

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