The earth-abundant transition metal manganese (Mn) has been shown to activate dinitrogen (N 2) and store nitrogen (N) as nitride for subsequent chemical reaction, for example, to produce ammonia (NH3). Chemical looping ammonia synthesis (CLAS) is a practical way to use Mn nitride by contacting nitride with gaseous hydrogen (H2 ) to produce ammonia (NH 3). Here, the dynamic process of N atoms penetrating into solid Mn has been investigated. Nitride layer growth was modeled to quantitate and pre- dict the storage of activated N in Mn towards designing CLAS systems. The N diffusion coefficient (DN ) and reaction rate constant K for the first-order nitridation reaction were estimated at 6.2 ± 5.5 10-11 m2/s and 4.1 ± 3.5 10-4 1/s, respectively, at atmospheric pressure and 700 °C. Assuming spherical particles of Mn with a diameter of < 10 lm, about 56.8 metric tons of Mn is sufficient to produce a metric ton of NH 3 per day using CLAS
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Green ammonia from air, water, and renewable electricity: Energy costs using natural gas reforming, solid oxide electrolysis, liquid water electrolysis, chemical looping, or a Haber–Bosch loop
The purpose of this work is to quantitatively compare the energy cost of design alternatives for a process to produce ammonia (NH3) from air, water, and renewable electricity. It is assumed that a Haber–Bosch (H–B) synthesis loop is available to produce 1000 metric tons (tonnes) of renewable NH3 per day. The overall energy costs per tonne of NH3 will then be estimated at U.S.$195, 197, 158, and 179 per tonne of NH3 when H2 is supplied by (i) natural gas reforming (reference), (ii) liquid phase electrolysis, (iii) solid oxide electrolysis (SOE) of water only, and (iv) simultaneous SOE of water and air. A renewable electricity price of U.S.$0.02 per kWh electric, and U.S.$6 per 10^6 BTU for natural gas is assumed. SOE provides some energy cost advantage but incurs the inherent risk of an emerging process. The last consideration is replacement of the H–B loop with atmospheric pressure chemical looping for ammonia synthesis (CLAS) combined with SOE for water electrolysis, and separately oxygen removal from air to provide N2, with energy costs of U.S.$153 per tonne of NH3. Overall, the most significant findings are (i) the energy costs are not substantially different for the alternatives investigated here and (ii) the direct SOE of a mixture of steam and air, followed by a H.–B. synthesis loop, or SOE to provide H2 and N2 separately, followed by CLAS may be attractive for small scale production, modular systems, remote locations, or stranded electricity resources with the primary motivation being process simplification rather than significantly lower energy cost.
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- Award ID(s):
- 1856084
- PAR ID:
- 10403371
- Publisher / Repository:
- AIP Publishing
- Date Published:
- Journal Name:
- Journal of Renewable and Sustainable Energy
- Volume:
- 14
- Issue:
- 5
- ISSN:
- 1941-7012
- Page Range / eLocation ID:
- 054701
- Subject(s) / Keyword(s):
- Ammonia Haber-Bosch renewable fossil-free fertilizer solid oxide, chemical looping
- Format(s):
- Medium: X
- Sponsoring Org:
- National Science Foundation
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