A novel chemical absorption–biological
reduction (CABR)
integrated process, employing Fe(II)EDTA as an enhanced absorbent,
is a promising technology for nitrogen oxides removal. In this work,
we developed a new two-stage CABR system applying a mixed cultivation
model of denitrifying bacteria and iron-reducing bacteria, which consists
of a sieve-plate tower and a bioreduction tower to separate the absorption
and reduction processes. The start-up period of the two-stage system
was shortened to 19 days, while that of the one-stage CABR system
was 46 days. In addition, the two-stage CABR system featured a better
oxygen-resistance ability and a higher NO removal loading. In effort
to optimize system operation, we compared different modes of system
operation and found that (1) continuous addition of glucose was better
than the batch-type addition and that (2) the NO removal efficiency
could be maintained at >90% while the FeEDTA concentration was
higher
than 4 mmol/L; however, reducing the initial concentration of ferric
iron complex could inhibit the loss rate of Na2EDTA. Furthermore,
the optimized operating mode parameters were 4 mmol/L initial Fe(III)EDTA,
0.6 mg/min Na2EDTA, and 5 mg/min glucose with a 2 L/min
gas flow rate under a 400 ppm of NO condition, while the NO removal
efficiency was kept >90%; the corresponding operating cost in terms
of glucose was 8.4 g of glucose/g of NO. The purpose of this work
was to provide preliminary data to support future industrial application
for NO
x
removal, as well as sufficient
technological insights on the process configuration and reactor operation
of the two-stage CABR system.