(785b) Characterization of New Pd, Pd-Au and Pd-Au-Pt Large Scale Membranes in Actual Coal Derived Syngas Atmospheres
AIChE Annual Meeting
2013
2013 AIChE Annual Meeting
Separations Division
Metal Membranes for Hydrogen Purification
Friday, November 8, 2013 - 8:55am to 9:20am
Characterization
of new Pd, Pd-Au and Pd-Au-Pt large scale membranes
in actual coal derived syngas atmospheres
Yi Hua Ma, Federico Guazzone, Ivan Mardilovich, Jacopo
Catalano and Nikolas K. Kazantzis
Center for
Inorganic Membrane Studies
Department
of Chemical Engineering
Worcester
Polytechnic Institute
Worcester,
MA 0109, USA
Abstract
Composite Pd alloy membranes are
highly suitable for the production of H2 in membrane reactors due to
their high stability at elevated temperatures and the infinite theoretical
selectivity of dense Pd alloys towards H2. The methane steam
reforming (MSR) and water gas shift (WGS) reactions have been carried out in
Pd-alloy membrane reactors by several researchers. In the effort to develop a
WGS catalytic membrane reactor, our group at Worcester Polytechnic Institute
has been studying the characteristics and stability of several composite Pd
based membranes in actual coal derived syngas atmospheres at the National
Carbon Capture Center (NCCC) in Wilsonville, Alabama. The H2 flux, H2
permeance and H2 purity of pure Pd and Pd-Au alloy membranes have
been studied at 450°C, 12.6 bar and an average H2
feed concentration of 35%. It was demonstrated that Pd-Au membranes were
characterized by an outstanding long term permeance and selectivity stability
at 450°C
in coal derived syngas for at least 473 h and H2 purities as high as
99.9%. However, all tested membranes at NCCC showed a sharp initial decrease in
H2 permeance (in the order of 30-60% of the initial permeance)
indicating the possible adsorption of contaminants on the Pd surface. XPS
analysis of a Pd film exposed to the same syngas as that of the membranes
showed the presence of Hg, Na, Mg, O, S and C.
The study of three membranes
(Pd-Au, Pd-Au-Pt and pure Pd) at NCCC led to the
following observations: (1) extended exposure (>150 h) of pure Pd membranes
in coal derived syngas might have led to the appearance of cracks (seen in SEM micrographs)
and subsequent drastic loss in selectivity, (2) Pd-Au membranes with high Au
content at the surface did not show signs of brittleness/cracking, however, their
permeance showed to be negatively affected by H2S concentration (up
to 10.6 ppm), but it was unexpectedly recovered up to a 100% after only 30 min
in syngas without H2S, and (3) the initial H2 permeance
loss of the Pd-Au-Pt membrane was only 25% indicating
that Pt might be a possible alloy element for H2S
resistance.
Preliminary experiments in our
laboratories with the Pd-Au and the Pd-Au-Pt
membranes showed that at the operating conditions (450°C and 12.6 bar) and at the
maximum ethylene and propylene concentrations in the syngas (< 1000 ppm) at
NCCC, ethylene and propylene had no or negligible effect on the H2
permeance of Pd-Au and Pd-Au-Pt membranes. Since the
pure Pd membrane showed a 80% decrease in initial permeance when tested at
NCCC, it appeared that the main reason for the initial H2 permeance
loss were sub-ppm levels of H2S not possible to detect with the on site GC.
The
mechanical stability of composite Pd membranes was also studied with a fourth
membrane which was subjected to 150 temperature cycles between 250 and 450°C
(shown in Figure 1(a)) and 100 additional temperature cycles between 250 and 400°C.
During the first 150 cycles the H2/He ideal selectivity declined
from approximately 10,000 to around 2,000. However, during the additional 100
temperature cycles the selectivity (or N2 leak permeance as seen in
Figure 1(b)) remained unchanged indicating that the decrease in selectivity was
mainly associated with the short dwell times at 450°C and not caused by the
temperature cycles. The temperature cycling test showed the outstanding robustness
of the prepared composite Pd membranes.
Figure 1. (a) H2
permeance and temperature profile during the 150 cycles between 250-450°C. (b)
N2 leak permeation as a function of time during the first 150 cycles
between 250-450°C and the additional 100 cycles between 250-400°C