(559f) MOFs As Adsorbents for Gas Separations: A Comparative Study | AIChE

(559f) MOFs As Adsorbents for Gas Separations: A Comparative Study

Authors 

Wiersum, A. D. - Presenter, Laboratoire Chimie Provence, CNRS / Université d'Aix-Marseille I, II et III
Soubeyrand-Lenoir, E. - Presenter, Laboratoire Chimie Provence, CNRS / Université d'Aix-Marseille I, II et III
Vagner, C. - Presenter, Laboratoire Chimie Provence, CNRS / Université d'Aix-Marseille I, II et III
Llewellyn, P. L. - Presenter, Laboratoire Chimie Provence, CNRS / Université d'Aix-Marseille I, II et III


Separation processes and especially the separation of gases form a major
part of both the capital expenditure and the operating expenditure on many
chemical plants. Gaseous mixtures are generally separated either by cryogenic
distillation or solvent extraction, both of which are highly energy intensive
and costly. A viable alternative to these is a pressure swing adsorption (PSA)
process, but this requires an adsorbent which is capable of separating the
gases efficiently.

Many different types of porous materials are being considered for use as
adsorbents in such a process including activated carbons, mesoporous silicas,
zeolites and metal-organic frameworks (MOFs) and indeed some of these are
already being used for specific separations1. The purpose of this
study is firstly to identify which are the best parameters for comparing new
materials and deciding which ones are most likely to be of interest for a
specific separation, and secondly to see whether MOFs can compete with the more
established materials such as activated carbons and zeolites.

Ideally the most relevant data for comparing adsorbents for a PSA
process would be breakthrough curves from column experiments, either at the lab
scale or in pilot plants. However these studies often require relatively large amounts
of adsorbent and are not feasible for materials which are at the discovery
stage, as many new MOFs are. Alternatively it is possible to measure static
co-adsorption isotherms using about a gram of material, but it can be difficult
to get reliable information from these experiments and so results are not
widely available in the literature.

The data which is most readily available for new MOFs is the pure
component isotherms measured at room temperature, given in terms of amount of
gas adsorbed for a given mass of adsorbent. This is not directly relevant for a
PSA process, however from this it is possible to extract a number of parameters
which can then be used to compare the materials.

We have undertaken a study where we have measured pure gas isotherms for
CO2, CO and CH4 on a number of different MOFs as well as
a two reference materials, a zeolite and an activated carbon, and compared them
based on the following criteria:

-         
Maximum
uptake in terms of amount adsorbed per gram of material (most readily available
data)

-         
Maximum
uptake as a volume of gas adsorbed per volume of adsorbent (more relevant for a
PSA process)

-         
Working
capacity, i.e. the difference between the amounts adsorbed at two operating
pressures

-         
Separation
factors based on prediction models (IAST and VSM)

In addition to this, we have also measured the adsorption enthalpies for
these systems using a Tian-Calvet type microcalorimeter coupled with a homemade
gas dosing device. These measurements provide information as to the strength of
the host-gas interaction and therefore how easy it is likely to be to
regenerate the adsorbent. This data is also interesting for a PSA process
because it gives an indication of the amount of heat released during
adsorption, which will either have to be removed or which will significantly
heat the column, if it is run as an adiabatic process.

Finally we have done a number of experiments to study the effect of water
on the adsorption of gases in these materials, looking at both the stability of
the material at different relative humidities and the competitive adsorption of
CO2 and water.

This study has shown that different materials stand out as good
candidates depending on what criteria you use to compare them and that some
materials which appear at first glance to be ideally suited for a particular
separation in fact present some major drawbacks when you look at the complete
picture. In addition, although in many cases the MOFs studied failed to compete
with zeolites or activated carbons, some processes were identified in which
MOFs could significantly outperform the reference materials.

This work is part of the European project FP7 MACADEMIA ?MOFs as
Adsorbents and Catalysts: Design and Engineering of Materials for Industrial
Applications? (CP-IP-228862-2). Our thanks go to the laboratories of the
Institut Lavoisier in Versailles, the Christian Albrechts Universität in Kiel
and the Korean Research Institute for Chemical Technologies for the samples
provided.

References

[1] S. P.
Reynolds, A. D. Ebner, J. A. Ritter, Industrial and Engineering Chemistry
Research. 45, 3256-3264, 2006.