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The Langmuir Adsorption Isotherm

The Langmuir Adsorption Isotherm

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Abstract<br />

<strong>The</strong> <strong>Langmuir</strong> <strong>Adsorption</strong> <strong>Isotherm</strong><br />

Patrick Leahy<br />

November 17, 2010<br />

Six acetic acid solutions were prepared, standardized, and allowed to adsorb onto samples of activated<br />

charcoal. <strong>The</strong> concentration of each solution was measured before and after adsorption. <strong>The</strong> adsorption<br />

constant Kads was measured to be 12.61 ± 0.911.<br />

Introduction<br />

Owing to its mostly hollow structure, even a small mass of activated charcoal presents a large surface area to<br />

adsorbants. <strong>The</strong> purpose of this experiment was to measure the adsorption of acetic acid onto that surface<br />

by allowing six solutions of varying concentration to adsorb onto samples of activated carbon of known mass.<br />

<strong>The</strong> reaction between the adsorbant A and the substrate S is<br />

and the adsorption constant Kads is<br />

Noting that [AS] = 1 − [S],<br />

Relabeling [AS] as θ and [A] as C,<br />

and hence<br />

Kads =<br />

A + S ⇀↽ AS (1)<br />

Kads = [AS]<br />

[A][S]<br />

Kads =<br />

[AS]<br />

[S] (1 − [AS])<br />

θ<br />

C (1 − θ)<br />

θ = KadsC<br />

C (1 − θ)<br />

which is the form of the <strong>Langmuir</strong> adsorption isotherm. This is equal to Y<br />

Ymax , where Ymax is the maximal<br />

adsorption. Dividing C by this yields<br />

C<br />

Y =<br />

1<br />

KadsYmax<br />

+ C<br />

Ymax<br />

A low-concentration approximation of this is the Freundlich isotherm:<br />

where k and n are empirical parameters.<br />

Y = kC 1<br />

n (5)<br />

1<br />

(2)<br />

(3)<br />

(4)


Experiment<br />

Six masses of activated charcoal were measured out, each being approximately 1.5g, and added to acetic<br />

acid solutions containing between five and one hundred percent 0.4M stock solution. <strong>The</strong> stock solution<br />

itself was titrated against potassium hydrogen phthalate (KHP) and its concentration was determined to<br />

be 0.390 ± 0.007M, and the six solutions were likewise standardized. <strong>The</strong> mass of each sample of activated<br />

charcoal and the standardized molarity of each acetic acid solution is given in the following table.<br />

Solution m(g) % 0.4M AcOH / 100mL Standardized molarity<br />

1 1.5049 100 0.0390<br />

2 1.5016 75 0.02925<br />

3 1.5062 50 0.0195<br />

4 1.5028 25 0.00975<br />

5 1.5017 10 0.00390<br />

6 1.5011 5 0.00195<br />

<strong>The</strong> six flasks were stoppered, placed in a heated shaking bath, and allowed to remain there for one week,<br />

whereafter the concentrations of the solutions in the flasks were measured again and compared to their<br />

original values. A difference was thereby obtained:<br />

Results and Discussion<br />

Solution mol AcOH (initial) mol AcOH (final) Difference (mol)<br />

1 0.0390 0.0339 0.00510<br />

2 0.02925 0.0248 0.0445<br />

3 0.0195 0.0159 0.00360<br />

4 0.00975 0.00716 0.00259<br />

5 0.00390 0.00244 0.00146<br />

6 0.00195 0.00101 0.000940<br />

From the differences in the number of moles in solution before and after absorption, the number of moles<br />

adsorbed onto the charcoal in each of the six flasks was determined; from this, the parameters necessary to<br />

describe the Freundlich and <strong>Langmuir</strong> isotherms were computed:<br />

Solution Y (mol) C (molL −1 ) C<br />

Y (L−1 ) lnC<br />

1 3.39 E-3 ± 1.63 E-5 0.339 ± 0.001 100 ± 0.564 -1.082 ± 2.95 E-3<br />

2 2.96 E-3 ± 1.32 E-5 0.248 ± 4.81 E-4 83.8 ± 0.408 -1.394 ± 1.94 E-3<br />

3 2.39 E-3 ± 1.52 E-5 0.159 ± 1.22 E-4 66.5 ± 0.426 -1.839 ± 7.67 E-4<br />

4 1.74 E-3 ± 3.30 E-5 0.0716 ± 1.87 E-3 41.6 ± 1.35 -2.637 ± 2.61 E-4<br />

5 9.72 E-4 ± 1.32 E-5 0.0244 ± 5.20 E-4 25.1 ± 0.634 -3.713 ± 0.0213<br />

6 6.26 E-4 ± 9.95 E-6 0.0101 ± 2.93 E-4 16.1 ± 0.533 -4.595 ± 0.0290<br />

as a function of C to a linear least-squares regression, by<br />

which Ymax was determined to be 0.003986 ± 2.88 E-4 mol and Kads was determined to be 12.61 ± 0.911.<br />

Similarly, by fitting Y as a function of ln(C) to a linear least-squares regression, the Freundlich parameters<br />

k and n were determined to be 0.005815 ± 3.698 E-5 and 2.079 ± 0.01552, respectively.<br />

Ymax and Kads were determined by fitting C<br />

Y<br />

2


Figure 1: <strong>The</strong> <strong>Langmuir</strong> and Freundlich isotherms plotted against the data.<br />

In general, the <strong>Langmuir</strong> isotherm is further from the data than the Freundlich isotherm.<br />

If an acetic acid molecule can be assumed to require an area A on the charcoal, then the area the charcoal<br />

offers for adsorption is AYmaxNA; hence, if A is 21 ˚A, this evaluates to 504 ± 36 m 2 g −1 .<br />

Conclusions<br />

Although the Kads derived for the <strong>Langmuir</strong> isotherm does not provide as good a fit to the data as the<br />

Freundlich isotherm (which is peculiar, since the Freundlich isotherm is an approximation), the measurment<br />

of Ymax yields a value close to the 708 m 2 g −1 of Brunauer, Emmett, and Teller [1].<br />

References<br />

[1] Brunauer, S., Emmett, P. H., and Teller, Edward. <strong>Adsorption</strong> of Gases in Multimolecular Layers. Journal<br />

of the American Chemical Society, 60, page 309 (1938).<br />

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