1999
DOI: 10.1021/jp991697h
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Uptake of Gas-Phase Ammonia. 2. Uptake by Sulfuric Acid Surfaces

Abstract: The uptake of gas-phase ammonia by sulfuric acid surfaces was measured as a function of temperature (248−288 K), gas−liquid interaction time (2−15 ms), and acid concentration (20−70 wt % H2SO4) using a droplet train apparatus. The uptake coefficient increases as a function of acid concentration and reaches unity at about 55 wt % H2SO4. The increased NH3 uptake in acid solution is apparently due to reaction between NH3 and H+ at the gas−liquid interface. The results yielded parameters required to model the reac… Show more

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Cited by 79 publications
(132 citation statements)
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“…The current uptake coefficients leading to NH neutralization of sulfuric acid particle (∼ 0.5-1; Swartz et al, 1999). These results suggest that under these conditions, the formation of NOC can compete with the neutralization of acidic particles, possibly due to kinetic limitations on the uptake of NH 3 caused by the coating of SOA as has been demonstrated previously (Liggio et al, 2011).…”
Section: Reaction Kineticssupporting
confidence: 66%
“…The current uptake coefficients leading to NH neutralization of sulfuric acid particle (∼ 0.5-1; Swartz et al, 1999). These results suggest that under these conditions, the formation of NOC can compete with the neutralization of acidic particles, possibly due to kinetic limitations on the uptake of NH 3 caused by the coating of SOA as has been demonstrated previously (Liggio et al, 2011).…”
Section: Reaction Kineticssupporting
confidence: 66%
“…The applicability of β FS for trace gases in air (including species with higher molecular mass) has been confirmed by good agreement with experimental data (Li and Davis, 1996;Widmann and Davis, 1997;Seinfeld and Pandis, 1998;Swartz et al, 1999;Worsnop et al, 2001). By inserting β FS instead of β F in Eq.…”
Section: Gas Kinetic Fluxes and Uptake Coefficientssupporting
confidence: 56%
“…(15) and rearrangement using J net,Xi = F net,Xi /(d 2 p π) and Eq. (9), C g,Xi can be flexibly adapted to the approach of Fuchs and Sutugin (1971): (Li and Davis, 1996;Widmann and Davis, 1997;Seinfeld and Pandis, 1998;Swartz et al, 1999;Worsnop et al, 2001). More elaborate formalisms may be required for non-isothermal processes ), but several studies have shown that the formulation of Fuchs and Sutugin (1971) works well also under non-isothermal conditions (Kulmala and Vesala, 1991;Vesala et al, 1997;Kulmala and Wagner, 2001;Winkler et al, 2004).…”
Section: Gas Kinetic Fluxes and Uptake Coefficientsmentioning
confidence: 99%
“…It should be noted, however, that ambient ammonia concentrations tend to be an order of magnitude greater than amine concentrations (Murphy et al, 2007), and the uptake coefficient of ammonia by H 2 SO 4 , approximately 1 (Liggio et al, 2011;Shi et al, 1999;Swartz et al, 1999), is also one or two orders of magnitude greater than that of amine. Conversely, the dissociation constants of aminium nitrate are greater than or equal to that of NH 4 NO 3 (Murphy et al, 2007).…”
Section: Introductionmentioning
confidence: 94%