The kinetics of the uptake of HNO3 on a series of salt powders (NaCl,
NaBr, KCl, and KBr) has been studied in a Teflon-coated, low-pressure
flow reactor. HCl and HBr are found to be the sole products of the rea
ctions, and, within experimental uncertainty, all the HNO3 taken up by
the salt is converted to HCl or HBr. Values for the uptake coefficien
ts are derived from two experimental procedures: (1) Steady-state upta
ke of constant HNO3 flows and (2) real-time monitoring of pulsed quant
ities of HNO3: The two procedures yield values in good agreement, and
it has been determined that all the salts studied, including the nonre
active NaNO3, are characterized by the same value of the uptake coeffi
cient: gamma = (2.8 +/- 0.3) x 10(-2). A discussion is given for the n
on-negligible affinity of HNO3 for the Teflon-coated walls and how thi
s effect is taken into account in our experiments. We develop a model
of the uptake kinetics, based on our experimental results, that reprod
uces the observations over a broad range of experimental conditions. I
n addition, the uptake of HCl (gamma = 3 x 10(-2)) and H2O (gamma < 2
x 10(-4)) on NaCl powder is determined in ancillary experiments. The r
esults may hold implications for the understanding of chloride displac
ement in marine aerosols.