Saudi Arabia-based Aramco, one of the world’s
leading integrated energy and chemicals companies, and Linde
Engineering, a global leader in the production and processing of
gases, signed an
agreement jointly to develop a new ammonia cracking technology. The
collaboration between the two companies will combine Linde Engineering
and Aramco’s experience and capabilities in industrial research and
development, lower-carbon hydrogen, and ammonia cracking technology.
A potential differentiator of this new technology
is the ammonia cracking catalyst, jointly developed by Aramco and the
King Abdullah University of Science and Technology (KAUST), which will
be evaluated against other catalysts.
Through this agreement, Aramco and Linde
Engineering plan to build a demonstration plant in northern Germany to
showcase this new ammonia cracking technology. Linde Engineering
intends to offer this ammonia cracking technology to current and new
customers, creating new commercial opportunities within the global
lower-carbon energy supply chain.
The emerging lower-carbon ammonia business may
prove to be key in bridging the gap between a country’s domestic
renewable energy production capacity and total energy demand.
This
agreement is part of our ongoing technology and business development
efforts to establish a commercially viable lower-carbon hydrogen
supply chain. We believe the advanced ammonia cracking technology we
are co-developing with Linde Engineering will play a key role in
realizing our objectives.
—Ahmad Al-Khowaiter, Senior Vice
President and Chief Technology Officer at Aramco
In 2020, a team from Aramco and KAUST reported in
an open-access paper in the RSC journal Catalysis
Science & Technology that a potassium-promoted ruthenium supported
on CaO is a very efficient catalyst for ammonia decomposition,
surpassing the performance of other Ru-supported solids.
At an optimum Ru loading of 3% wt, catalysts with a
K/Ru atomic ratio of 0.9 showed the best catalytic performance under
a wide range of operating conditions, P = 1–40 bar, T = 250–550 °C
and WHSV = 9000–30000 mL g−1 h−1.
Although NH3 conversion
levels decrease considerably upon increasing the reaction pressure
(X550
°C, 40 bar = 0.8), high pressure ammonia
decomposition offers the possibility of COx-free
compressed hydrogen and hydrogen productivities and TOFs 40 times
bigger than when applying atmospheric pressure.
—Savas et
al.
Green Play Ammonia™, Yielder® NFuel Energy.
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