Abstract. Oxidation flow reactors (OFRs) are frequently used to
study the formation and evolution of secondary aerosol (SA) in the
atmosphere and have become valuable tools for improving the accuracy of
model simulations and for depicting and accelerating realistic atmospheric
chemistry. Driven by rapid development of OFR techniques and the increasing
appreciation of their wide application, we designed a new all-Teflon
reactor, the Particle Formation Accelerator (PFA) OFR, and characterized it
in the laboratory and with ambient air. A series of simulations and
experiments were performed to characterize (1) flow profiles in the reactor
using computational fluid dynamics (CFD) simulations, (2) the UV intensity
distribution in the reactor and the influence of it and varying O3
concentration and relative humidity (RH) on the resulting equivalent OH
exposure (OHexp), (3) transmission efficiencies for gases and
particles, (4) residence time distributions (RTDs) for gases and particles
using both computational simulations and experimental verification, (5) the
production yield of secondary organic aerosol (SOA) from oxidation of
α-pinene and m-xylene, (6) the effect of seed particles on resulting
SA concentration, and (7) SA production from ambient air in Riverside, CA,
US. The reactor response and characteristics are compared with those of a
smog chamber (Caltech) and of other oxidation flow reactors: the Toronto
Photo-Oxidation Tube (TPOT), the Caltech Photooxidation Flow Tube (CPOT),
the TUT Secondary Aerosol Reactor (TSAR), quartz and aluminum versions of
Potential Aerosol Mass reactors (PAMs), and the Environment and Climate
Change Canada OFR (ECCC-OFR). Our studies show that (1) OHexp can be varied over a range comparable
to that of other OFRs; (2) particle transmission efficiency is over 75 %
in the size range from 50 to 200 nm, after minimizing static charge on the
Teflon surfaces; (3) the penetration efficiencies of CO2 and SO2
are 0.90 ± 0.02 and 0.76 ± 0.04, respectively, the latter of
which is comparable to estimates for LVOCs; (4) a near-laminar flow profile
is expected based on CFD simulations and suggested by the RTD experiment
results; (5) m-xylene SOA and α-pinene SOA yields were 0.22 and 0.37,
respectively, at about 3 × 1011 molec. cm−3 s OH
exposure; (6) the mass ratio of seed particles to precursor gas has a
significant effect on the amount of SOA formed; and (7) during measurements
of SA production when sampling ambient air in Riverside, the mass
concentration of SA formed in the reactor was an average of 1.8 times that
of the ambient aerosol at the same time.