Abstract:A Dekati® low pressure impactor (DLPI) is used to determine the mass distribution of airborne particles from 7 nm to 10 µm as a function of aerodynamic diameter. Quantification of wall deposits inside this sampling device was performed for the first time using polydisperse zinc aerosol produced by a thermal spraying process. This aerosol is more representative of the size distribution found in occupational atmospheres than aerosols usually produced in laboratories. Each experiment (3 replicates) was carried ou… Show more
“…The self-and cross-reactions of RO 2 radicals also form ROOR (C 16 H 22 O 10 ) or ROOR', which are the accretion products (Berndt et al, 2018;Molteni et al, 2018). The further O 2 adduct of BPR can form highly oxygenated RO 2 radicals and further react and finally form highly oxygenated organic molecules (HOMs; Types 1 and 2 in Scheme 1; Wang et al, 2017;Crounse et al, 2013;Ehn et al, 2014;Jokinen et al, 2015;Berndt et al, 2016). Dimethylphenol (C 8 H 10 O) and other products from the termination reaction with the benzene ring or double bond can react with OH radicals and further react to form HOMs as well.…”
Section: Proposed Mechanism Of Rh Effects On Soa Formationmentioning
Abstract. The
effect of relative humidity (RH) on secondary organic aerosol (SOA) formation
from the photooxidation of m-xylene initiated by OH radicals in the absence
of seed particles was investigated in a Teflon reactor. The SOA yields were
determined based on the particle mass concentrations measured with a scanning
mobility particle sizer (SMPS) and reacted m-xylene concentrations
measured with a gas chromatograph–mass spectrometer (GC-MS). The SOA
components were analyzed using a Fourier transform infrared (FTIR)
spectrometer and an ultrahigh-performance liquid chromatograph–electrospray
ionization–high-resolution mass spectrometer (UPLC-ESI-HRMS). A significant
decrease was observed in SOA mass concentration and yield variation with the
increasing RH conditions. The SOA yields are 14.0 %–16.5 % and
0.8 %–3.2 % at low RH (14 %) and high RH (74 %–79 %),
respectively, with the difference being nearly 1 order of magnitude. Some of
the reduction in the apparent yield may be due to the faster wall loss of
semi-volatile products of oxidation at higher RH. The chemical mechanism for
explaining the RH effects on SOA formation from m-xylene–OH system is
proposed based on the analysis of both FTIR and HRMS measurements, and the
Master Chemical Mechanism (MCM) prediction is used as the assistant. The FTIR
analysis shows that the proportion of oligomers with C-O-C groups from
carbonyl compounds in SOA at high RH is higher than that at low RH, but
further information cannot be provided by the FTIR results to well explain
the negative RH effect on SOA formation. In the HRMS spectra, it is found
that C2H2O is one of the most frequent mass differences at low
and high RHs, that the compounds with a lower carbon number in the formula at
low RH account for a larger proportion than those at high RH and that the
compounds at high RH have higher O : C ratios than those at low RH. The
HRMS results suggest that the RH may suppress oligomerization where water is
involved as a by-product and may influence the further particle-phase
reaction of highly oxygenated organic molecules (HOMs) formed in the gas
phase. In addition, the negative RH effect on SOA formation is enlarged based
on the gas-to-particle partitioning rule.
“…The self-and cross-reactions of RO 2 radicals also form ROOR (C 16 H 22 O 10 ) or ROOR', which are the accretion products (Berndt et al, 2018;Molteni et al, 2018). The further O 2 adduct of BPR can form highly oxygenated RO 2 radicals and further react and finally form highly oxygenated organic molecules (HOMs; Types 1 and 2 in Scheme 1; Wang et al, 2017;Crounse et al, 2013;Ehn et al, 2014;Jokinen et al, 2015;Berndt et al, 2016). Dimethylphenol (C 8 H 10 O) and other products from the termination reaction with the benzene ring or double bond can react with OH radicals and further react to form HOMs as well.…”
Section: Proposed Mechanism Of Rh Effects On Soa Formationmentioning
Abstract. The
effect of relative humidity (RH) on secondary organic aerosol (SOA) formation
from the photooxidation of m-xylene initiated by OH radicals in the absence
of seed particles was investigated in a Teflon reactor. The SOA yields were
determined based on the particle mass concentrations measured with a scanning
mobility particle sizer (SMPS) and reacted m-xylene concentrations
measured with a gas chromatograph–mass spectrometer (GC-MS). The SOA
components were analyzed using a Fourier transform infrared (FTIR)
spectrometer and an ultrahigh-performance liquid chromatograph–electrospray
ionization–high-resolution mass spectrometer (UPLC-ESI-HRMS). A significant
decrease was observed in SOA mass concentration and yield variation with the
increasing RH conditions. The SOA yields are 14.0 %–16.5 % and
0.8 %–3.2 % at low RH (14 %) and high RH (74 %–79 %),
respectively, with the difference being nearly 1 order of magnitude. Some of
the reduction in the apparent yield may be due to the faster wall loss of
semi-volatile products of oxidation at higher RH. The chemical mechanism for
explaining the RH effects on SOA formation from m-xylene–OH system is
proposed based on the analysis of both FTIR and HRMS measurements, and the
Master Chemical Mechanism (MCM) prediction is used as the assistant. The FTIR
analysis shows that the proportion of oligomers with C-O-C groups from
carbonyl compounds in SOA at high RH is higher than that at low RH, but
further information cannot be provided by the FTIR results to well explain
the negative RH effect on SOA formation. In the HRMS spectra, it is found
that C2H2O is one of the most frequent mass differences at low
and high RHs, that the compounds with a lower carbon number in the formula at
low RH account for a larger proportion than those at high RH and that the
compounds at high RH have higher O : C ratios than those at low RH. The
HRMS results suggest that the RH may suppress oligomerization where water is
involved as a by-product and may influence the further particle-phase
reaction of highly oxygenated organic molecules (HOMs) formed in the gas
phase. In addition, the negative RH effect on SOA formation is enlarged based
on the gas-to-particle partitioning rule.
“…et al, 2013b). In another study, 80 % of particle loss was found to concentrate around the nozzles and 20 % on the impaction plate in a stage of the DLPI (Dekati ® Low-Pressure Impactor) (Durand T. et al, 2014).…”
Section: Particle Loss Effectmentioning
confidence: 95%
“…Experimental and theoretical studies have been conducted for determining the particle losses by impaction and diffusion (Chen S.C. et al, 2007). The inertial loss of large particles normally occurs on the contractions which connect the big inlet tube to the small nozzle or on the surface of nozzle plate (Durand T. et al, 2014;Gupta T., 2015a, 2015b).…”
Section: Particle Loss Effectmentioning
confidence: 99%
“…Some commonly used cascade impactors are Andersen cascade impactor (Andersen A.A., 1966), Mer-cer cascade impactor (Mercer T.T. et al, 1970), Quartz Crystal Microbalance (QCM) cascade impactor (Hering S.V., 1987), Pilat cascade impactor (Pilat M.J. et al, 1970), Berner low-pressure cascade impactor (Berner A., 1972), Low-Pressure Impactor (Berner A., 1972), Dekati ® Low-Pressure Impactor (DLPI) (Durand T. et al, 2014), MOUDI (Marple V.A. et al, 1991;Marple V.A.…”
Section: Particle Mass Distribution Measurementmentioning
confidence: 99%
“…But several limitations are inherent to the impactors such as particle bounce and re-entrainment (Turner J.R. and Hering S.V., 1987;Fujitani Y. et al, 2006), particle overloading (Tsai C.J. and Cheng Y.H., 1995;Demokritou P. et al, 2004b), and particle loss (Fang C. et al, 1991;Durand T. et al, 2014), which can degrade their performance. Moreover, some typical characteristics of the inertial impactors such as the cutoff diameter, the sharpness of collection efficiency curve, and the properties of the impaction substrate should be understood well since PMs have different sizes, shapes, types, compositions and characteristics (Loo B.W., 1975;Hinds W.C., 1999).…”
Inertial impactors are applied widely to classify particulate matters (PMs) and nanoparticles (NPs) with desired aerodynamic diameters for further analyses due to their sharp cutoff characteristics, simple design, easy operation, and high collection ability. A few hundred papers have been published since the 1860s that addressed the characteristics and applications of the inertial impactors. In the last 30 years, our group has also carried out lots of studies to contribute to the design and the improvement of inertial impactors. With our understanding of inertial impactors, this article reviews previous studies of some typical types of the inertial impactors including conventional impactors, cascade impactors, and virtual impactors and the parameters for design consideration of these devices. The article also reviews some applications of the inertial impactors, which are mass concentration measurement, mass and number distribution measurement, personal exposure measurement, particulate matter control, and powder classification. The synthesized knowledge of the inertial impactor in this study can help researchers to design an inertial impactor with an accurate cutoff diameter, a sharp collection efficiency curve, and no particle bounce and particle overloading effects for long-term use for PM classification and control purposes.
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