Journal
ACS SUSTAINABLE CHEMISTRY & ENGINEERING
Volume 7, Issue 6, Pages 5975-5985Publisher
AMER CHEMICAL SOC
DOI: 10.1021/acssuschemeng.8b06065
Keywords
Ammonia; Hydrogen; Membrane reactor; Model; Kinetics; Purification; Process intensification
Categories
Funding
- Department of Energy
- National Science Foundation [0000785]
- NSF [1512172]
- DOE Integrated University Program Graduate Fellowship
- Div Of Chem, Bioeng, Env, & Transp Sys
- Directorate For Engineering [1512172] Funding Source: National Science Foundation
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Liquid ammonia is a high-density (17.7 wt %) hydrogen carrier with a well-established production and distribution infrastructure. Efficient decomposition and purification are essential for its use as a hydrogen-storage material. Here we demonstrate the production of high-purity (>99.7%) H-2 from NH3 using a catalytic membrane reactor (CMR) in which a Ru catalyst is impregnated within a porous yttria-stabilized zirconia (YSZ) tube coated with a thin, 6 mu m Pd film by electroless deposition. The intimate proximity of catalyst and membrane eliminates transport resistances that limit performance in the conventional packed-bed membrane reactor (PBMR) configuration. The addition of a Cs promoter enabled complete NH3 conversion at temperatures as low as 400 degrees C, exceeding equilibrium constraints without the need for a sweep gas. A reactor model was developed that captured CMR performance with high fidelity. NH3 decomposition was observed to follow first-order kinetics due to efficient H-2 removal. Relative to a comparable PBMR, the Ru loading in the CMR was reduced an order of magnitude and the H-2 recovery increased 35%, enabling record volumetric productivity rates (>30 mol m(-3) s(-1)) that validate its promise for efficient, compact H-2 delivery from ammonia.
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