(459g) Influence of Supports on Chemical Looping Methane Reforming Activity of NiO-Based Oxygen Transfer Materials | AIChE

(459g) Influence of Supports on Chemical Looping Methane Reforming Activity of NiO-Based Oxygen Transfer Materials


Silvester, L. - Presenter, Texas A & M University at Qatar
Bukur, D. - Presenter, Texas A & M University at Qatar
Antzara, A. - Presenter, Aristotle University of Thessaloniki
Heracleous, E. - Presenter, International Hellenic University (IHU)
Ipsakis, D. - Presenter, Aristotle University of Thessaloniki
Lemonidou, A. - Presenter, Aristotle University of Thessaloniki

of supports on chemical looping methane reforming activity of NiO-based oxygen
transfer materials



Hydrogen is an
energy carrier that can be used to efficiently store regenerative energy, and it
fulfills the requirements of being the most environmentally friendly fuel for
several applications. Although the steam methane reforming process is currently
the major source of hydrogen production, its high energy demands  along with 
increased CO2 production make the overall process undesirable both from
economic and environmental considerations. The Sorption Enhanced Chemical
Looping Steam Methane Reforming (SE-CL-SMR) is an emerging technology that can
simultaneously minimize the aforementioned drawbacks and produce pure hydrogen.
The stable and active oxygen transfer materials (OTMs) and CO2
sorbents are the major requirements for a viable SE-CL-SMR process. NiO
supported OTMs have been promising oxygen carriers for chemical looping methane
reforming reactions due to their superior redox reactivity, catalytic
performance, stability and negligible volatility. In this study we investigated
the influence of supports on redox activity of OTMs in the absence of steam in a
thermo-gravimetric analyzer (TGA) unit, and in conventional and chemical looping
steam methane reforming reactions (CLR) in a fixed bed flow unit.


NiO-based OTMs with 40wt% NiO loading were synthesized by wet
impregnation using commercial supports: (SiO2, TiO2, Al2O3,
ZrO2). Both pre- and post- characterizations of the OTMs such as BET,
XRD, H2-TPR, TPO and TEM were performed. Twenty redox cycles, methane
reduction at 650°C/air oxidation at 800°C, were conducted in a TGA unit connected to a mass spectrometer (MS). Conventional steam reforming
activity of the pre-reduced OTMs was tested at 650°C in a bench scale fixed bed
flow unit with a steam/methane (S/C) ratio of 3 and GHSV=105h-1.
In a second step, NiO/ZrO2 and NiO/Al2O3,
which exhibited satisfactory reforming activity and stability, were tested
under CLR conditions. The materials were initially exposed to CH4/steam
in their oxidized state at 650°C for 1h (S/C=3). At the end of reforming stage,
metallic Ni was re-oxidized with air at 850°C for 15min and the cycle was then

Results and

surface area of the 40%NiO-OTMs decreased after loading NiO compared to the
pure supports. XRD confirmed the presence of NiO phase in all OTMs, and strong metal-support
interaction compounds (NiAl2O4 and NiTiO3) were
identified in Al2O3- and TiO2- supported OTMs.
During the 20 redox cycles in TGA, all
OTMs except 40%NiO/g-Al2O3 attained very high
reduction degrees (94% - 100%) (Fig. 1a). Degree of reduction (RD, %) of NiO/Al2O3
slowly increased up to cycle 11 reaching a maximum and steady value of 86%. This
relatively low reducibility is mainly
attributed to the strong metal-support interaction, as identified by XRD. In
order to investigate the unusual trend in the reduction degree of NiO/Al2O3,
temperature programed reduction (TPR) was performed for fresh and used (after 10th
redox cycles) OTM in the TGA (not shown). Results confirmed the decomposition of
NiAl2O4 and increase
in the NiO/NiAl2O4 ratio with cycles, indicating
that re-crystallization of metallic Ni after reduction in methane weakens the
alumina-nickel oxide interaction. All four OTMs
underwent complete re-oxidation during the oxidation step of the cycling
experiments, reaching the same oxidation degree level of 100% in all cycles. The H2, CO, CO2 and H2O
were the products detected during CH4 reduction, whereas CO2
was the only oxidation product detected by MS.

Figure 1 The variation in (a) the reduction degree and (b) the
amount of carbon with cycles

The amount of carbon deposited during reduction steps, calculated from the
observed weight gain in TGA, is shown in Fig. 1b. NiO/Al2O3
OTM exhibited a volcano shape curve which is possibly caused by changes in
catalyst structure (gradual NiAl2O4 reduction) with cycles
(Fig. 1b). For all OTMs trends in hydrogen formation
(not shown) followed the same trend as C-deposition, indicating that there is a
relationship between deposited carbon and H2 formation during the
reduction step. Data analysis showed that hydrogen
production occurs primarily via CH4 split. The amount of carbon deposition
and hydrogen production was higher during initial cycles on Al2O3
and ZrO2 OTMs, followed by decrease in subsequent cycles. This
indicates deactivation of these OTMs towards the CH4 decomposition

In order to
investigate the nature and types of carbon deposited on OTMs by methane
decomposition during the reduction cycles, TPO and TEM analysis were performed.
TPO characterization of all OTMs after the first methane reduction step in TGA showed
a single CO2 peak centered at ~500⁰C ? 550⁰C indicating
the presence of one type of carbon on the surface. However the TPO profile of NiO/Al2O3
after the methane reduction step of the fourth cycle indicated the presence of
two carbon species, oxidized to CO2 at 575⁰C and 700⁰C
respectively. In order to obtain further insights into the nature of the deposited
carbon species, the samples were examined with transmission electron
microscopy. Both graphitic and filamentous carbon were observed on Al2O3
and ZrO2 supported OTMs. TEM image of Al2O3 supported
OTM after the first cycle is shown in Fig. 2 for illustration. On the other
hand, only graphitic carbon was observed on the SiO2 and TiO2
supported OTMs.

under conventional reforming conditions (with pre-reduced OTMs) showed a satisfactory
performance of NiO/Al2O3 and NiO/ZrO2 at
650°C, with a high methane conversion and less than 8% deactivation after 10 h on stream. On the other hand,
NiO/SiO2 and NiO/TiO2 were found to be inactive, with
initial CH4 conversion less than 12%. The two most promising materials were then tested
under chemical looping reforming conditions for 20
consecutive steam methane reforming/air oxidation cycles.
Methane conversion as a function of cycles is shown in Figure 3. NiO/ZrO2 exhibited a satisfactory
activity with initial CH4 conversion around 80% and less than 2%
deactivation after 20 cycles, corresponding to 20h
exposure to CH4/steam. Initial CH4
conversion on NiO/Al2O3OTM was
similar (~79%), but it deactivated
more rapidly, leading to a CH4 conversion of
59% in the 20th cycle (Fig. 3). This loss of
activity can be attributed to the lower hydrothermal stability of alumina
compared to zirconia under the steam reforming conditions.

Figure 2 TEM image of Al2O3 OTM after 1st reduction cycle

Figure 3 CH4 conversion in chemical looping reforming experiments for NiO/ZrO2 and NiO/Al2O3  (Reduction-Reforming: 650⁰C, 1h, S/C = 3,  GHSV =100000h-1;
Oxidation: 800⁰C, 15min, Air)


Support was
found to have a significant effect on performance of NiO oxygen carriers in
chemical looping steam methane reforming. All investigated OTMs supported on
silica, alumina, zirconia and titania displayed satisfactory activity and high
stability during 20 methane reduction/air oxidation cycles
in TGA experiments. The 40%NiO/Al2O3 OTM showed
unusual behavior compared to the other OTMs due to gradual reduction of
metal-support compounds to more easily reducible species with cycles. Carbon
deposition in the absence of steam in the TGA occurs primarily via CH4
decomposition on reduced Ni. Only graphitic carbon was observed on SiO2-
and TiO2- OTMs, whereas both graphitic and filamentous carbon were
observed on Al2O3- and ZrO2- OTMs. Testing of
all OTMs as reforming catalysts in conventional SMR showed that NiO on titania
and silica is inactive, while alumina and zirconia supported OTMs had high
activity and stability characteristics. The latter two materials were tested in
the chemical looping methane reforming process, where they exhibited promising
performance. NiO/ZrO2 showed good
activity with initial CH4 conversion around 80% and less than 2%
deactivation after 20 cycles. NiO/Al2O3 had also a
high initial CH4 conversion, but had higher deactivation rate with
cycles, probably due to a lower hydrothermal stability of alumina.


This work was made possible by NPRP grant
5?420?2?166 from QNRF (member of Qatar Foundation). The statements made herein
are solely the responsibility of the authors.