Electrochemical systems for total
ammonium nitrogen (TAN) recovery
are a promising alternative compared with conventional nitrogen-removal
technologies. To make them competitive, we propose a new minimal stackable
configuration using cell pairs with only bipolar membranes and cation-exchange
membranes. The tested bipolar electrodialysis (BP-ED) stack included
six cell pairs of feed and concentrate compartments. Critical operational
parameters, such as current density and the ratio between applied
current to nitrogen loading (load ratio), were varied to investigate
the performance of the system using synthetic wastewater with a high
nitrogen content as an influent (NH
4
+
≈
1.75 g L
–1
). High TAN removal (>70%) was achieved
for a load ratio higher than 1. At current densities of 150 A m
–2
and a load ratio of 1.2, a TAN transport rate of
1145.1±14.1 g
N
m
–2
d
–1
and a TAN-removal efficiency of 80% were observed. As the TAN removal
was almost constant at different current densities, the BP-ED stack
performed at a high TAN transport rate (819.1 g
N
m
–2
d
–1
) while consuming the lowest
energy (18.3 kJ g
N
–1
) at a load ratio
of 1.2 and 100 A m
–2
. The TAN transport rate, TAN
removal, and energy input achieved by the minimal BP-ED stack demonstrated
a promising new cell configuration for upscaling.