Lithium-mediated nitrogen reduction is a proven method to electrochemically synthesize ammonia; yet the process has so far been unstable, and the continuous deposition of lithium limits its practical applicability. One...
Boosting ammonia with a little oxygen
Ammonia synthesis from nitrogen for fertilizer production is highly energy intensive. Chemists are therefore exploring electrochemical approaches that could draw power from renewable sources while generating less waste. One promising cycle involves the reduction of lithium ions at an electrode, with the resultant metal in turn reducing nitrogen and regenerating the ions. Li
et al
. report the counterintuitive result that small quantities of oxygen could enhance the efficiency of this process, which they attribute to diffusional effects that limit excessive lithium reduction. —JSY
The lithium-mediated ammonia synthesis is so far the only proven electrochemical way to produce ammonia with promising faradaic efficiencies (FEs). However, to make this process commercially competitive, the ammonia formation rates per geometric surface area need to be increased significantly. In this study, we increased the current density by synthesizing high surface area Cu electrodes through hydrogen bubbling templating (HBT) on Ni foam substrates. With these electrodes, we achieved high ammonia formation rates of 46.0 ± 6.8 nmol s −1 cm geo −2 , at a current density of −100 mA/cm geo −2 at 20 bar nitrogen atmosphere and comparable cell potentials to flat foil electrodes. The FE and energy efficiency (EE) under these conditions were 13.3 ± 2.0% and 2.3 ± 0.3%, respectively. Additionally, we found that increasing the electrolyte salt concentration improves the stability of the system, which is attributed to a change of Li deposition and/or solid electrolyte interphase.
Lithium-mediated non-aqueous electrochemical ammonia synthesis (LiMEAS) as an efficient and green ammonia production way was studied by GCMS in different organic electrolytes to evaluate the stability of electrochemical systems.
Experiments with the continuous precipitation of calcium carbonate
are reported in this study.
Particle size distributions were measured on-line and interpreted
by means of the simultaneous
nucleation and the transformation models developed in part 1 of this
sequence. Three regimes
of precipitation are reported in this study, governed by the
supersaturation and liquid phase
[Ca2+]/[CO3
2-]
ionic ratio. These comprise of a heterogeneous regime involving
calcite and vaterite
nucleation at moderate
[Ca2+]/[CO3
2-]
ionic ratio in an unscaled reactor, homogeneous nucleation
of vaterite followed by transformation to calcite in a scaled reactor
at low and moderate [Ca2+]/[CO3
2-] ratio, and formation of
stable vaterite at high
[Ca2+]/[CO3
2-]
ratio. The particle size
distributions in the different regimes are well fitted by the
applicable model from part 1 or
earlier studies of single-species precipitation. Where
appropriate, kinetic parameters obtained
from the fits are correlated with supersaturation by power law
models.
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